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  • Biochemistry and Biotechnology  (670)
  • 2020-2022
  • 1995-1999  (670)
  • 1970-1974
  • 1999
  • 1996  (670)
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  • 2020-2022
  • 1995-1999  (670)
  • 1970-1974
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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 204-216 
    ISSN: 0006-3592
    Keywords: expanded bed adsorption ; bakers' yeast ; G6PDH ; STREAMLINE ion exchange adsorbents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of expanded beds of STREAMLINE ion exchange adsorbents for the direct extraction of an intracellular enzyme glucose-6-phosphate dehydrogenase (G6PDH) from unclarified yeast cell homogenates has been investigated. It has been demonstrated that such crude feedstocks can be applied to the bed without prior clarification steps. The purification of G6PDH from an unclarified yeast homogenate was chosen as a model system containing the typical features of a direct extraction technique. Optimal conditions for the purification were determined in small scale, packed bed experiments conducted with clarified homogenates. Results from these experiments were used to develop a preparative scale separation of G6PDH in a STREAMLINE 50 EBA apparatus. The use of an on-line rotameter for measuring and controlling the height of the expanded bed when operated in highly turbid feedstocks was demonstrated. STREAMLINE DEAE has been shown to be successful in achieving isolation of G6PDH from an unclarified homogenate with a purification factor of 12 and yield of 98% in a single step process. This ion exchange adsorbent is readily cleaned using simple cleaning-in-place procedures without affecting either adsorption or the bed expansion properties of the adsorbent after many cycles of operation. The ability of combining clarification, capture, and purification in a single step will greatly simplify downstream processing flowsheets and reduce the costs of protein purification. © 1996 John Wiley & Sons, Inc.
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  • 2
    Electronic Resource
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 259-265 
    ISSN: 0006-3592
    Keywords: hepatocytes ; lactose-derivatized polystyrene ; polystyrene ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hepatocytes isolated from male Fisher 344VF rats were cultured on two substrates, collagen I and a lactose-derivatized polystyrene (PS-lactose), to compare morphological and functional differences. Hepatocyte morphology changed dramatically depending upon the substrate, shown through actin cytoskeletal staining and scanning electron microscopy. Functional assays performed included albumin secretion, reduced glutathione content, UDP-glucuronosyl transferase, and cytochrome P4501A1 activity. The presence of dexamethasone and dimethylsulfoxide (DMSO) in the media was required for the maintenance of several differentiated functions for cells cultured on collagen. In general, cells cultured on the PS-lactose substrate showed a much slower loss of function over the same period of time. The maintenance of differentiated function of cells on PS-lactose was enhanced with the addition of dexamethasone and DMSO. This is the first report of a culture system in which hepatocytes, cultured on a polymer substrate without additional protein coatings or media additives, have been able to maintain differentiated functions for up to 1 week. © 1996 John Wiley & Sons, Inc.
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  • 3
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 290-299 
    ISSN: 0006-3592
    Keywords: proteins, modified ; partitioning in aqueous system ; thaumatin ; β-lactoglobulin ; BSA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Relatively conservative modifications of three proteins were carried out to alter their surface properties. The protein properties modified were hydrophobicity and charge. This was done by acylation of amino groups with anhydrides. For the hydrophobic modification experiments, two proteins (β-lactoglobulin and bovine serum albumin [BSA]) and four anhydrides (hexanoic, butyric, succinic, acetic) were used. For the modification of surface charge the protein thaumatin was selected and various proportions of the free amino groups were blocked with acetic anhydride to give a series of proteins with differing isoelectric points. Detailed characterization and purification of selected modified proteins was carried out including molecular weight measurements and conformational analysis. The criteria used for selecting the modified proteins for subsequent investigation of their partitioning in aqueous two-phase systems (ATPS) is described. With a judicious choice of starting material it was found that limited chemical modifications to proteins could effectively alter surface hydrophobicity or charge almost independently, with little effect on other molecular properties. It appears, however, that the method for chemical modification and the reaction conditions must also be carefully controlled. © 1996 John Wiley & Sons, Inc.
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  • 4
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 309-315 
    ISSN: 0006-3592
    Keywords: surface charge ; proteins, modified ; partitioning in aqueous system ; thaumatin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A series of charge-modified thaumatins with different values of surface charge were partitioned in aqueous two-phase systems (ATPS) to study the effect of surface charge as a single property on partitioning. Electrophoretic mobility of the proteins in titration curves was used as a measure of surface charge. Four modified proteins derived from thaumatin with the following values of isoelectric point: 8.70, 8.15, 5.60, and 4.50 were used for partitioning. The resolution of the systems in terms of protein surface charge was calculated. Partitioning of modified thaumatins in PEG 4000/dextran systems with phosphate buffer, Tris buffer, NaCl, KCl, and sulfate salts was carried out. Among the sulfate salts tested, the addition of 50 mM Li2SO4 to the system buffered with phosphate gave the highest value of resolution for differences in surface protein charge (RSPC). It shows a decrease in the value of K (partition coefficient) with an increase in the protein's charge. The addition of 100 mM KCl to the system promoted the opposite effect on the RSPC value. Charge-modified proteins were partitioned in PEG/salt systems to investigate the ability of these systems for resolving differences in surface charge. The PEG/citrate system seemed to have almost no ability for resolving proteins on the basis of surface charge differences; PEG/phosphate systems had some capability for resolving differently charged proteins. The more negative proteins tended to have higher values of K than the more positively charged fractions. The use of charge-modified proteins allowed the investigation of the effect of protein surface charge on partitioning in aqueous two-phase systems independently from other protein parameters as they were prepared from a common parent protein thaumatin. This technique provides an interesting novel tool to investigate the effect of protein surface charge on partitioning in ATPS taking protein charge as an independent parameter. © 1996 John Wiley & Sons, Inc.
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  • 5
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 348-354 
    ISSN: 0006-3592
    Keywords: oxygenator ; NMR spectroscopy ; organ perfusion ; mammalian cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A compact, reusable membrane oxygenator has been constructed for the perfusion of cultured cells and isolated organs. While the oxygenator was designed to be compatible with nuclear magnetic resonance (NMR) spectroscopy studies, it can also be used for any experiment which requires warming and oxygenation of perfusates. For the NMR studies, the oxygenator can be positioned at the opening of the magnet bore which allows oxygenation and warming of the perfusate immediately prior to delivery to the tissue, therefore eliminating problems with heat or oxygen loss which may occur with the long perfusion lines. © 1996 John Wiley & Sons, Inc.
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  • 6
    ISSN: 0006-3592
    Keywords: c-fos protein ; endothelium ; hemodynamics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The c-fos protein belongs to a family of transcriptional cofactors that can complex with proteins of the Jun family and activate mRNA transcription from gene promoters containing an activator protein 1 (AP-1) binding element. The shear stress inducibility of the c-fos protein was studied in human and animal cell lines of vastly different origins. Primary human umbilical vein endothelial cells (HUVEC), bovine aortic endothelial cells (BAEC, passage 2-14), HeLa cells, and Chinese hamster ovary (CHO) cells were subjected to steady laminar shear stress using a parallel plate flow apparatus. After 1 h of flow exposure at 25 dyn/cm2, the c-fos levels in nuclei of shear stress HUVEC, BAEC, HeLa, and CHO were 5.4 ± 2.0 (n = 3), 2.25 ± 1.38 (n = 6), 2.14 ± 0.07 (n = 8), 1.92 ± 0.58 (n = 2) times higher, respectively, than in matched stationary controls. Flow exposure at 4 dyn/cm2 caused no enhancement of c-fos levels in any of the cell lines tested, but caused significant reduction in c-fos expression in the HeLa cells. The c-fos induction by shear stress could be blocked by pharmacological agents. For example, the flow induction of the c-fos protein levels was blocked by 50% with the preincubation of HUVEC with a protein kinase C inhibitor, H7 (10 μM) and blocked completely in HeLa cells preincubated with the phospholipase C inhibitor, neomycin (5 mM). The minimum time of shear stress exposure required to induce the c-fos protein expression in HeLa cells was found to be as low as 1 min. By Northern analysis, the c-fos mRNA levels were found to be elevated in BAEC, CHO, and HeLa cells exposed to 25 dyn/cm2 for 30 min. These studies indicate that c-fos induction is a consistent genetic response in a variety of mammalian cells that may alter cellular phenotype in mechanical environments. © 1996 John Wiley & Sons, Inc.
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  • 7
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    Biotechnology and Bioengineering 49 (1996), S. 412-420 
    ISSN: 0006-3592
    Keywords: Amycolatopsis orientalis ; vancomycin production ; chemostat culture ; phosphate inhibition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Production of the glycopeptide antibiotic vancomycin by two Amycolatopsis orientalis strains was examined in batch shake flask culture in a semidefined medium with peptone as the nitrogen source. Different growth and production profiles were observed with the two strains; specific production (Yp/x) was threefold higher with strain ATCC 19795 than with strain NCIMB 12945. A defined medium with amino acids as the nitrogen source was developed by use of the Plackett-Burman statistical screening method. This technique identified certain amino acids (glycine, phenylalanine, tyrosine, and arginine) that gave significant increased specific production, whereas phosphate was identified as inhibitory for high specific vancomycin production. Experiments made with the improved medium and strain ATCC 19795 showed that vancomycin production kinetics were either growth dissociated or growth associated, depending on the amino acid concentration. In chemostat culture at a constant dilution rate (0.087 h-1), specific vancomycin production rate (qvancomycin) decreased linearly as the medium phosphate concentration was increased from 2 to 8 mM. In both phosphate and glucose limited chemostats, qvancomycin was a function of specific growth rate; the maximum value was observed at D = 0.087 h-1 (52% of the maximum specific growth rate). Under phosphate limited growth conditions, qvancomycin was threefold higher (0.37 mg/g dry weight/h) than under glucose limitation (0.12 mg/g dry weight/h). © 1996 John Wiley & Sons, Inc.
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  • 8
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    Biotechnology and Bioengineering 50 (1996), S. 36-48 
    ISSN: 0006-3592
    Keywords: insect cell culture ; Sf-9 cells ; respiration ; bioreactor ; on-line monitoring ; baculovirus expression vector system ; recombinant proteins ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Respiration rates in Spodoptera frugiperda (Sf-9) cell bioreactor cultures were successfully measured on-line using two methods: The O2 uptake rate (OUR) was determined using gas phase pO2 values imposed by a dissolved oxygen controller and the CO2 evolution rate (CER) was measured using an infrared detector. The measurement methods were accurate, reliable, and relatively inexpensive. The CER was routinely determined in bioreactor cultures used for the production of several recombinant proteins. Simple linear relationships between viable cell densities and both OUR and CER in exponentially growing cultures were used to predict viable cell density. Respiration measurements were also used to follow the progress of baculoviral infections in Sf-9 cultures. Infection led to increases in volumetric and per-cell respiration rates. The relationships between respiration and several other culture parameters, including viable cell density, cell protein, cell volume, glucose consumption, lactate production, viral titer, and recombinant β-galactosidase accumulation, were examined. The extent of the increase in CER following infection and the time postinfection at which maximum CER was attained were negatively correlated with the multiplicity of infection (MOI) at multiplicities below the level required to infect all the cells in a culture. Delays in the respiration peak related to the MOI employed were correlated with delays in the peak in recombinant protein accumulation. DO levels in the range 5-100% did not exert any major effects on viable cell densities, CER, or product titer in cultures infected with a baculovirus expressing recombinant β-galactosidase. © 1996 John Wiley & Sons, Inc.
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  • 9
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 50 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 10
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    Biotechnology and Bioengineering 50 (1996), S. 169-183 
    ISSN: 0006-3592
    Keywords: liposomes ; biotin ; aggregation kinetics ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The aggregation of biotinylated phospholipid vesicles (liposomes) cross-linked by antibiotin IgG was studied experimentally and theoretically. The liposomes were either low density liposomes that contained 0.4 mol% biotinylated phospholipid (≈100 exposed biotin molecules per liposome), or high density liposomes that contained 2.7 mol% biotinylated phospholipid (≈1000 exposed biotin molecules per liposome). The solution turbidity and mean particle size measured by quasi-elastic light scattering (QLS) were monitored throughout the aggregation. Three different lots of antibiotin antibodies, each with different association constants and binding heterogeneities, were used. The antibody binding characteristics affected the aggregation rates. The aggregation kinetics were analyzed using a model based on the Smoluchowski theory of aggregation, fractal concepts of aggregate microstructure, and Rayleigh and Mie light scattering theory. The experimental conditions of liposome concentration, protein concentration, and ligand density under which aggregation occurred correlated well with calculated sticking probabilities based on isotherms describing the adsorption of antibiotin antibody to the liposomes. These results are compared with prior observations made when avidin was used as the cross-linking protein. © 1996 John Wiley & Sons, Inc.
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  • 11
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 50 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 12
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    Biotechnology and Bioengineering 50 (1996), S. 211-216 
    ISSN: 0006-3592
    Keywords: microgravity ; bioprocessing ; sedimentation ; turbulence ; collagenase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of a quiescent microgravity fluid environment on the activity of collagenase directed at demineralized bone fragments was investigated over a period of 10 days. Enzyme treatment resulted in greater mass loss in microgravity, with nearly three times the loss of mass during Space Shuttle mission STS-62 compared to the stationary ground control. Clinorotation enhanced the loss of mass relative to a stationary control, but this increase was still significantly less than the increase with exposure to microgravity. This suggests the detrimental influence of turbulence on the enzyme function and the benefit of using microgravity to provide both low turbulence and uniformity of unequally dense materials within the reaction chamber. The results are considered for their general applicability to a variety of bioprocessing applications that may be enhanced in microgravity. © 1996 John Wiley & Sons, Inc.
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  • 13
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    Biotechnology and Bioengineering 50 (1996), S. 430-437 
    ISSN: 0006-3592
    Keywords: cartilage ; tissue regeneration ; chondrocytes ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the last 5 to 10 years, tissue engineering has revolutionized the way in which medical researchers and clinicians are thinking of and, in some cases, actually treating diseases involving tissue damage and destruction. One such disease, osteoarthritis, results from progressive degeneration of articular cartilage, which has a limited ability to repair itself. With tissue engineering, scientists are now able to regenerate cartilage in vitro from isolated mature chondrocytes. While the regeneration process is still not fully understood, enough has been learned that physicians are already implanting cultured chondrocytes into humans and other animals in the hopes of effecting joint repair. One aspect which has not been fully explored is the effect of mechanical stress on developing and implanted cartilage, especially over the long term. This article will review in brief what is now known about the mechanical factors affecting cartilage regeneration in vitro and what still remains to be determined for optimum tissue engineering of cartilage constructs. © 1996 John Wiley & Sons, Inc.
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  • 14
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    Biotechnology and Bioengineering 50 (1996), S. 443-451 
    ISSN: 0006-3592
    Keywords: osteoblast ; migration ; poly(αhydroxy esters) ; poly(DL-lactic-co-glycolic acid) ; PLGA ; biodegradable polymers ; tissue engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We investigated the migration of rat calvaria osteoblast populations on poly(α-hydroxy ester) films for up to 14 days to determine effects of substrate composition and culture conditions on the migratory characteristics of osteoblasts. Initial osteoblast culture conditions included cell colonies formed by seeding a high (84,000 cells/cm2) or low (42,000 cells/cm2) density of isolated osteoblasts on the polymer films, and bone tissue cultures formed by plating bone chips directly on the substrates. High density osteoblast colonies cultured and allowed to migrate and proliferate radially on 85:15 poly(DL-lactic-co-glycolic acid) (PLGA) films, 75:25 PLGA films, and tissue culture polystyrene controls demonstrated that the copolymer ratio in the polymer films did not affect the rate of increase in substrate surface area (or culture area) covered by the growing cell colony. However, the rate of increase in culture area was dependent on the initial osteoblast seeding density. Initial cell colonies formed with a lower osteoblast seeding density on 75:25 PLGA resulted in a lower rate of increase in culture area, specifically 4.9 ± 0.3 mm2/day, versus 14.1 ± 0.7 mm2/day for colonies seeded with a higher density of cells on the same polymer films. The proliferation rate for osteoblasts in the high and low density seeded osteoblast colonies did not differ, whereas the proliferation rate for the osteoblasts arising from the bone chips was lower than either of these isolated cell colonies. Confocal and light microscopy revealed that the osteoblast migration occurred as a monolayer of individual osteoblasts and not a calcified tissue front. These results demonstrated that cell seeding conditions strongly affect the rates of osteoblast migration and proliferation on biodegradable poly(α-hydroxy esters). © 1996 John Wiley & Sons, Inc.
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  • 15
    ISSN: 0006-3592
    Keywords: bone marrow ; hematopoiesis ; perfusion ; culture optimization ; stroma ; stem cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Hematopoiesis, the formation of mature blood cells from stem (LTC-IC) and progenitor (CFU-GM) cells in the bone marrow, is a complex tissue-forming process that leads to many important physiological functionalities. Consequently, a functioning ex vivo hematopoietic system has a variety of basic scientific and clinical uses. The design and operation of such a system presents the tissue engineer with challenges and choices. In this study, three culture variables were used to control ex vivo human hematopoiesis. Systematic variation of inoculum density (ID), medium exchange interval (MEI), and the use of preformed stroma (PFS) showed that (1) all three variables significantly influenced culture performance, (2) the three variables interacted strongly, and (3) the variables could be manipulated to achieve the optimization of different performance criteria. Donor-to-donor variability in culture performance was great at low ID but was minimized at higher ID. PFS had a large positive effect on cell and CFU-GM output at low ID, but had minimal effect at higher ID. In fact, PFS caused a decrease in LTC-IC output at high ID. The effects of PFS indicated that stromal cell elements became more limiting than proliferative cell elements as ID was reduced.In cultures without PFS, maximum cell output was obtained with high ID using a short MEI, whereas the greatest cell expansion ratio was obtained at low ID with an intermediate MEI. Maximum CFU-GM output was obtained from cultures with high ID using a short to intermediate MEI, whereas the greatest CFU-GM expansion ratio was obtained at intermediate ID with an intermediate MEI. The addition of PFS altered the locations of these maxima. In general, PFS moved the maxima to lower ID, and culture output became more sensitive to MEI. Therefore, the optimization of one performance criterion always resulted in a decline of the others. This study demonstrates that ex vivo tissue function is sensitive to many culture variables in an interactive fashion and that systematic multivariable studies are required to characterize tissue function. Once the effects of individual variables and their interactions are known, this knowledge can be used to optimize tissue performance with respect to desired criteria. © 1996 John Wiley & Sons, Inc.
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  • 16
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    Biotechnology and Bioengineering 50 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
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  • 17
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    Biotechnology and Bioengineering 51 (1996), S. 410-421 
    ISSN: 0006-3592
    Keywords: lysozyme ; thermal stability ; 1H NMR ; conformational flexibility ; melting temperature ; PEG ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The reversible folding destabilization of hen lysozyme has been confirmed by a melting temperature (Tm) decrease in aqueous poly(ethylene glycol) (PEG). The percent denatured, extracted from the histidine 15 C2H (H15 C2H) native and denatured peak areas from 500-MHz one-dimensional proton nuclear magnetic resonance (1D 1H NMR) spectra in D2O, was analyzed through denaturation temperatures at 0% and 20% (w/w) PEG 1000. The lysozyme (3.5 mM) Tm decreased by 4.2°C and 7.1°C in 20% (w/w) PEG 1000 at pH 3.8 and 3.0, respectively. The Tm decreased with increasing lysozyme concentration. Additionally, the temperature-induced resonance migrations of 17 protons from 8 residues indicate that the native lysozyme structure undergoes temperature-induced conformational changes. The changes were essentially identical in both 0% and 20% (w/w) PEG 1000 at both pH 3.0 and 3.8. This small, local restructuring of the hydrophobic box region may be a manifestation of temperature-dependent solution hydrophobicity, whereas active-site cleft fluctuations may be due to the inherent active-site flexibility. The lysozyme structure in PEG at 35°C was determined to be essentially native from the 1H nuclear Overhauser effect spectroscopy (NOESY) fingerprint regions. Additionally, lysozyme chemical shifts, from 1D spectra, in PEG 200, 300, and 1000 at 35°C and various concentrations were essentially identical, further confirming that the conformation remains native in various PEG solutions. © 1996 John Wiley & Sons, Inc.
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  • 18
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    Biotechnology and Bioengineering 51 (1996), S. 375-383 
    ISSN: 0006-3592
    Keywords: cellulase ; enzyme recycling ; enzyme adsorption ; lignocellulosic hydrolysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Past technoeconomic modeling work has identified the relatively large contribution that enzymatic hydrolysis adds to the total cost of producing ethanol from lignocellulosic substrates. This cost was primarily due to the high concentration of enzyme and long incubation time that was required to obtain complete hydrolysis. Although enzyme and substrate concentration and end-product inhibition influenced the rate of hydrolysis, the effect was less pronounced during the initial stages of hydrolysis. During this time most of the cellulases were adsorbed onto the unhydrolyzed residue. By recycling the cellulases adsorbed to the residual substrate remaining after an initial 24 h, a high rate of hydrolysis, with low overall residence time and minimal cellulase input, could be achieved for several rounds of enzyme recycle. A comparison of the front end (pretreatment, fractionation, and hydrolysis) of a softwood/hardwood to ethanol process indicated that the lignin associated with the softwood-derived cellulose stream limited the number of times the cellulose containing residue could be recycled. © 1996 John Wiley & Sons, Inc.
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  • 19
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    Biotechnology and Bioengineering 51 (1996), S. 399-409 
    ISSN: 0006-3592
    Keywords: cell damage ; cell culture ; bubble aeration ; agitation ; bubble coalescence and breakup ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: It has been established that the forces resulting from bubbles rupturing at the free air (gas)/liquid surface injure animal cells in agitated and/or sparged bioreactors. Although it has been suggested that bubble coalescence and breakup within agitated and sparged bioreactors (i.e., away from the free liquid surface) can be a source of cell injury as well, the evidence has been indirect. We have carried out experiments to examine this issue. The free air/liquid surface in a sparged and agitated bioractor was eliminated by completely filling the 2-L reactor and allowing sparged bubbles to escape through an outlet tube. Two identical bioreactors were run in parallel to make comparisons between cultures that were oxygenated via direct air sparging and the control culture in which silicone tubing was used for bubble-free oxygenation. Thus, cell damage from cell-to-bubble interactions due to processes (bubble coalescence and breakup) occurring in the bulk liquid could be isolated by eliminating damage due to bubbles rupturing at the free air/liquid surface of the bioreactor. We found that Chinese hamster ovary (CHO) cells grown in medium that does not contain shear-protecting additives can be agitated at rates up to 600 rpm without being damaged extensively by cell-to bubble interactions in the bulk of the bioreactor. We verified this using both batch and high-density perfusion cultures. We tested two impeller designs (pitched blade and Rushton) and found them not to affect cell damage under similar operational conditions. Sparger location (above vs. below the impeller) had no effect on cell damage at higher agitation rates but may affect the injury process at lower agitation intensities (here, below 250 rpm). In the absence of a headspace, we found less cell damage at higher agitation intensities (400 and 600 rpm), and we suggest that this nonintuitive finding derives from the important effect of bubble size and foam stability on the cell damage process. © 1996 John Wiley & Sons, Inc.
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  • 20
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    Biotechnology and Bioengineering 51 (1996), S. 434-438 
    ISSN: 0006-3592
    Keywords: polyphosphate ; Escherichia coli ; phosphate starvation ; gene expression ; heterologous ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of intracellular polyphosphate on the phosphate-starvation response in Escherichia coli was studied by genetically manipulating the intracellular polyphosphate levels and by performing phosphate shifts on the genetically engineered strains. Strains that produced large quantities of polyphosphate and were able to degrade it induced the phosphate-starvation response to a lesser extent than wild-type strains, whereas strains that were unable to degrade a large intracellular polyphosphate pool induced the phosphate-starvation response to a greater extent than wild-type strains. These results have important implications for expression of heterologous genes under control of the phoA promoter. © 1996 John Wiley & Sons, Inc.
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  • 21
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    Biotechnology and Bioengineering 51 (1996), S. 458-465 
    ISSN: 0006-3592
    Keywords: concentric-cylinder shear device ; rotor/stator homogenization ; shear ; shear rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Shear is present in almost all bioprocesses and high shear is associated with processes involving agitation and emulsification. The purpose of this study is to investigate the effect of high shear and high shear rate on proteins. Two concentric cylinder-based shear systems were used. One was a closed concentric-cylinder shear device (CCSD) and the other was a homogenizer with a rotor/stator assembly. Mathematical modeling of these systems allowed calculation of the shear rate and shear. The CCSD generated low shear rates (a few hundred s-1), whereas the homogenizer could generate very high shear rates (〉 105 s-1). High shear could be achieved in both systems by increasing the processing time. Recombinant human growth hormone (rhGH) and recombinant human deoxyribonuclease (rhDNase) were used as the model proteins in this study. It was found that neither high shear nor high shear rate had a significant effect on protein aggregation. However, a lower melting temperature and enthalpy were detected for highly sheared rhGH by using scanning microcalorimetry, presumably due to some changes in protein's conformation. Also, SDS-PAGE indicated the presence of low molecular-weight fragments, suggesting that peptide bond breakage occurred due to high shear. rhDNase was relatively more stable than rhGH under high shear. No conformational changes and protein fragments were observed. © 1996 John Wiley & Sons, Inc.
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  • 22
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    Biotechnology and Bioengineering 51 (1996), S. 494-499 
    ISSN: 0006-3592
    Keywords: cell metabolism ; baculovirus ; insect cells ; recombinant protein OSF-2 ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The properties of Sf9 and Tn5 insect cells were analyzed comparatively under serum-free culture conditions. Sf9 cells in SF900II medium apparently utilized sucrose as a primary nutrient both before and after virus infection, yielding small amounts of lactate and ammonia. Tn5 cells in Excell 401 medium consumed all the nutrients examined, including sucrose. The productivity of a recombinant glycoprotein, OSF-2, by Tn5 cells, was moderate in both monolayer and spinner cultures, but the ability to secrete it was compromised in the former case. Relative to the Tn5 cultures, Sf9 produced 30-fold more OSF-2 in either culture mode. © 1996 John Wiley & Sons, Inc.
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  • 23
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    Biotechnology and Bioengineering 51 (1996), S. 538-543 
    ISSN: 0006-3592
    Keywords: NMR imaging ; biosorption ; alginate ; shrinking core model ; Laminaria ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In this contribution, an NMR imaging study of heavy metal absorption in alginate, immobilized-cell biosorbents, and kombu (Laminaria japonica) algal biomass is presented. This method provides the good possibility of directly monitoring the time evolution of the spatial distribution of the ions in the materials. From these results, we demonstrate that rare earth ions are absorbed with a steep reaction front that can be described very well with a modified shrinking core model, while copper ions are absorbed with a more diffuse front.
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  • 24
    ISSN: 0006-3592
    Keywords: oxidoreductase ; chiral alcohol ; racemic resolution ; membrane reactor ; continuous extraction ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Oxidations of alcohols by alcohol dehydrogenases often suffer from low conversions and slow reaction rates due to severe product inhibition. This can be overcome by continuous product extraction, because only the concentrations, but not the kinetic parameters, can be changed. As a consequence, it is favorable to apply a differential circulation reactor with continuous product extraction, where only a small amount of product is formed per cycle. The product is then directly extracted using a microporous hydrophobic hollow fiber membrane. This results in an increase of the relative activity of the dehydrogenase at a given conversion. The reaction investigated is the kinetic resolution of racemic 1-phenyl-1,2-ethanediol by glycerol dehydrogenase (GDH). The resulting oxidation product, 2-hydroxyacetophenone, causes a strong product inhibition. Additionally, it reacts in a chemical reaction with the cofactor lowering its active concentration. Because the GDH needs β-nicotinamide adenine dinucleotide (NAD+) as a cofactor, lactate dehydrogenase is used to regenerate NAD+ from NADH by reducing pyruvate to (L)-lactate. A conversion of 50% with respect to the racemate and an enantiomeric excess 〉99% of the (S)-enantiomer was reached.
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  • 25
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    Biotechnology and Bioengineering 51 (1996), S. 581-590 
    ISSN: 0006-3592
    Keywords: microfiber ; graft polymerization ; DNA immobilization ; immunoadsorbent ; DNA ; anti-DNA antibody ; systemic lupus erythematosus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Immobilization of DNA to the surface of poly(ethylene terephthalate) (PET) microfibers with a high specific surface area of 0.83 m2/g was carried out to give the fiber surface an affinity for anti-DNA antibody. Following ozone oxidation, the microfibers were subjected to graft polymerization of monomers including acrylic acid, methacryloyloxyethyl phosphate, N,N-dimethylaminoethyl methacrylate, N-vinylformamide, and glycidyl methacrylate. Calf thymus DNA was immobilized to the grafted fiber surface through either covalent binding or polyion complexation with the grafted polymer chains. The highest surface density of DNA immobilized (0.6 μg/cm2) was obtained when DNA was immobilized through formation of phosphodiester linkage between the hydroxyl group of DNA and the phosphate group in grafted poly(methacryloyloxyethyl phosphate) using 1,1-carbonyldiimidazole, or through polyion complexation between the anionic DNA and the cationic grafted poly(N,N-dimethylaminoethyl methacrylate) chains. Batch adsorption of anti-DNA antibody to the grafted PET fibers with and without DNA immobilized on their surface was conducted with serum obtained from systemic lupus erythematosus model mice. The DNA-immobilized PET fibers exhibited a higher adsorption capacity and specificity than the others. In addition, the DNA-immobilized fibers effectively adsorbed human anti-DNA antibody.
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  • 26
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    Biotechnology and Bioengineering 49 (1996), S. 20-25 
    ISSN: 0006-3592
    Keywords: filamentous fungi ; immobilization ; biofilm bioreactor ; oil emulsion ; degradation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A new type of horizontal biofilm bioreactor for continuous bioconversion of emulsified oily substrate by immobilized growing biofilm of filamentous fungi was designed, constructed, and feasibility tested. The new reactor design provides “self”-immobilization of homogenized mycelium leading to even biofilm development. This was accomplished by using stainless steel screens of optimal mesh, mounted in parallel and stretching outward from a main rotating axis of a biological rotating contractor. Each screen was equipped with a pair of stainless steel blades mounted on supports allowing for continuous biofilm “shaving” beyond a predetermined thickness, thus retaining freshly growing active biofilm surface. The feasibility of the new bioreactor was demonstrated by decalactone production from emulsified castor oil by immobilized filamentous fungi (Tyromyces sambuceus). The combination of oriented metal screens and moving blades was found to be highly effective for a model system in maintaining stable substrate emulsion in the reactor in either batchwise or continuous processing, as well as maintaining biofilm thickness with continuous removal of excess growing hyphae. © 1996 John Wiley & Sons, Inc.
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  • 27
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    Biotechnology and Bioengineering 49 (1996), S. 284-289 
    ISSN: 0006-3592
    Keywords: organic phase biocatalysis ; esterification ; water activity ; lipase ; biocatalysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Packed bed hollow fiber membrane reactors were used to carry out organic phase biocatalysis at constant water activity. The performance of the device was tested by carrying out the esterification of dodecanol and decanoic acid in hexane. Lipase from Candida rugosa, immobilized on microporous polypropylene and packed in the shell space of the reactor, was used to catalyze the reaction. In situ water activity control was accomplished by pumping appropriate saturated salt solutions through the microporous hollow fiber polypropylene membranes. Water generated by reaction in the organic phase, pumped continuously through the shell of the reactor, was transferred into the bulk of the aqueous phase under the water activity gradient. The reactor performance was found to be strongly dependent on the controlling water activity. By carefully selecting this control activity it was found possible to obtain complete esterification. The water activity of the organic phase could be maintained very close to that of the saturated salt solution used. The reactor could be operated in the continuous mode for 100 h without any degradation in its performance. © 1996 John Wiley & Sons, Inc.
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  • 28
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    Biotechnology and Bioengineering 49 (1996), S. 328-333 
    ISSN: 0006-3592
    Keywords: disaccharides ; lipase ; organic solvent ; trans-esterification ; regioselectivity ; fatty acid ester ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The acylation of several disaccharides by ethyl butanoate and ethyl dodecanoate was catalyzed by Candida antarctica lipase in tert-butyl alcohol, at temperatures ranging from 40° to 82°C (reflux temperature). The relative reaction rates of the various disaccharides were directly related to their solubility. The primary products were the monoesters derived from acylation of the primary alcohol groups. At higher conversions diesters were formed, and the ratio of diester to monoester was markedly dependent on the structure of the disaccharide. Thus, reaction of maltose with ethyl dodecanoate in refluxing tert-butyl alcohol afforded the 6′-monododecanoate even at high conversions. Trehalose, in contrast, afforded the 6,6′-diester. Acylation of the less soluble sucrose and lactose was much slower, but a moderate (37%) conversion of sucrose was observed after a prolonged reaction time (7 days). A number of other lipases and proteases were tested but C. antarctica lipase was unique in catalyzing the acylation of sucrose in refluxing tert-butyl alcohol. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 341-347 
    ISSN: 0006-3592
    Keywords: water reuse ; fermentation ; lysine ; Corynebacterium glutamicum ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: L-Lysine is produced commercially by fermentation. As is typical for fermentation processes, a large amount of liquid waste is generated. To minimize the waste, which is mostly the broth effluent from the cation exchange column used for l-lysine recovery, we investigated a strategy of recycling a large fraction of this broth effluent to the subsequent fermentation. This was done on a labscale process with Corynebacterium glutamicum ATCC 21253 as the l-lysine-producing organism. Broth effluent from a fermentation in a defined medium was able to replace 75% of the water for the subsequent batch; this recycle ratio was maintained for three sequential batches without affecting cell mass and l-lysine production. Broth effluent was recycled at 50% recycle ratio in a fermentation in a complex medium containing beet molasses. The first recycle batch had an 8% lower final l-lysine level, but 8% higher maximum cell mass. In addition to reducing the volume of liquid waste, this recycle strategy has the additional advantage of utilizing the ammonium desorbed from the ion-exchange column as a nitrogen source in the recycle fermentation. The major problem of recycling the effluent from the complex medium was in the cation-exchange operation, where column capacity was 17% lower for the recycle batch. The loss of column capacity probably results from the buildup of cations competing with l-lysine for binding. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 377-382 
    ISSN: 0006-3592
    Keywords: hybridoma ; batch culture ; dichloroacetate ; metabolism ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have studied the effect of the pyruvate dehydrogenase (PDH) activator, dichloroacetate (DCA), on the growth, metabolism, and productivity of the PQXB ½ hybridoma cell line. In control batch cultures, cessation of growth and the onset of decline phase coincided with the time at which the media became exhausted of glutamine. Supplementation of the media with DCA (1 mM) extended the growth phase of this cell line by approximately 20 h without affecting its growth rate. This prolonged period of growth resulted in an increased maximum cell density (16%) and final antibody yield (55%). Repeat experiments showed these effects to be reproducible, with the increases in antibody yield being between 50 and 60%. DCA did not affect the specific rates of glucose utilization and lactate production. However, it decreased the specific glutamine consumption rate. This characteristic of DCA action appeared, at least in part, to provide an explanation for the extended growth phase exhibited by DCA-treated cultures, since it delayed the time at which the media became depleted of glutamine. The consumption and production kinetics for various nutrients and their metabolites in both control and DCA-treated cultures suggested that: (1) glutamine catabolism proceeded by a pathway involving conversion to glutamate by glutaminase followed by subsequent transamination by alanine aminotransferase, and (2) DCA decreased the specific glutamine consumption rate by directly or indirectly inhibiting the transamination. It is expected that the routine inclusion of DCA in media used for hybridoma cultivation will be valuable for enhancement of monoclonal antibody (Mab) yields on a laboratory scale. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 399-404 
    ISSN: 0006-3592
    Keywords: subtilisin ; hydration ; catalytic activity ; supercritical fluids ; solvent effects ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We studied a model transesterification reaction catalyzed by subtilisin Carlsberg suspended in carbon dioxide, propane, and mixtures of these solvents under pressure. To account for solvent effects due to differences in water partitioning between the enzyme and the bulk solvents, we measured water sorption isotherms for the enzyme in each solvent. We measured catalytic activity as a function of enzyme hydration and obtained bell-shaped curves with maxima at the same enzyme hydration (12%) in all the solvents. However, the activity maxima were different in all media, being much higher in propane than in either CO2 or the mixtures with 50 and 10% CO2. Considerations based on the solvation ability of the solvents did not offer an explanation for the differences in catalytic activity observed. Our results suggest that CO2 has a direct adverse effect on the catalytic activity of subtilisin. © 1996 John Wiley & Sons, Inc.
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  • 32
    ISSN: 0006-3592
    Keywords: Streptomyces virginiae ; autoregulator ; virginiae butanolide ; virginiamycin fermentation ; optimization ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A strategy for optimization of non-growth-associated production in batch culture employing an empirical approach was developed through the study of virginiamycin production. The strategy is formulated with two aims: attaining a high cell concentration at the beginning of the production phase without decrease in production activity; and enhancing the production activity during the production phase. As a practical example, the goal of a maximum virginiamycin (M and S) production in the batch culture of Streptomyces virginiae was set. To attain a high cell concentration in the production phase of the batch culture, that is, to extend the growth phase for as long as possible, the optimum composition and concentration of the complex medium, especially the yeast extract (YE) concentration, were first investigated. Dissolved oxygen (DO) concentration control was also a parameter considered in maintaining the production activity during the production phase. In addition, to enhance the production activity, an optimum addition strategy of an autoregulator, virginiae butanolide-C (VB-C), was investigated. Combining these measures, the optimum cultivation conditions were found to be an initial YE concentration in the complex medium of 45 g/L, the shot addition of 300 μg/L of VB-C 11.5 h after the start of the batch culture, and a DO concentration maintained above 2 mg/L. The maximum concentrations of virginiamycin M and S were about ninefold those obtained under nonoptimum cultivation conditions. Nonoptimum cultivation conditions consisted of an initial YE concentration one sixth (7.5 g/L) that of the optimum cultivation conditions, and no VB-C addition. These conditions were used as representative of the standard cultivation of virginiamycin in this study. The strategy developed here will be applicable to the production of other antibiotics, especially to the cultivation of Streptomyces species, in which a hormonelike signal material (an autoregulator) plays an important role in antibiotic production. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 34
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    Biotechnology and Bioengineering 49 (1996), S. 504-511 
    ISSN: 0006-3592
    Keywords: cellulose ; cellulase ; simultaneous saccharification and extractive fermentation ; ethanol ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Alcohol fermentation has traditionally been carried out in aqueous environments because of the ready solubility of reactant (sugar) and product (ethanol). However, extraction of the product ethanol into a nonmiscible phase can result in kinetic benefits due to reduced inhibition of the fermentation reactions. In this study, we report the development of a novel simultaneous saccharification and extractive fermentation (SSEF) process. Ethanol productivity was increased by up to 65% over conventional (nonextractive) fed-batch simultaneous saccharification systems when calculated on the basis of aqueous phase volume. The amount of water required for SSEF reactions was dramatically reduced from that required for conventional SSF. In batch SSEF reactors with 2.5% aqueous phase, 50% conversion of 25% (aqueous phase concentration) Solka Floc could be achieved in 48 h using 2 FPU/g cellulase. © 1996 John Wiley & Sons, Inc.
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  • 35
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    Biotechnology and Bioengineering 49 (1996), S. 535-543 
    ISSN: 0006-3592
    Keywords: whole cell biotransformation ; biocatalyst ; baker's yeast ; immobilization ; microencapsulation ; organic solvents ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Stable, semipermeable polyamide microcapsules were prepared by interfacial polymerization from a mixture of 1,6-hexanediamine and poly(allylamine) crosslinked with di-acid chlorides and were used to encapsulate baker's yeast. The size and distribution of cells within the capsules were investigated by a combination of laser confocal, electron scanning, and transmission electron microscopy. The encapsulated cells were studied as a biocatalyst for the model reduction of 1-phenyl-1,2-propanedione to 2-hydroxy-1-phenyl-1-propanone in a number of organic solvents. The polymerization conditions were extensively investigated and were found to greatly influence the product yield. Microencapsulated yeast cells, prepared under optimized conditions, carried out the reduction more efficiently than free cells as well as those immobilized in alginate and κ-carrageenan beads. The developed methodology should be broadly applicable to other biotransformations of interest. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 587-598 
    ISSN: 0006-3592
    Keywords: gas phase bioreactor ; dynamic behavior ; waste air ; MEK ; MIBK ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the work reported here, selected aspects of the dynamic behavior of biofilters for waste air treatment have been investigated. Emphasis was placed on transient state elimination of mixtures of methyl ethyl ketone (MEK) and methyl isobutyl ketone (MIBK) vapors and on explanation of the observed phenomena. The initial startup, the response of the biofilter to step changes in the pollutant loadings, responses to pollutant pulses, restarting after starvation, and the influence of step changes in gaseous phase oxygen partial pressure are presented and discussed. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 621-628 
    ISSN: 0006-3592
    Keywords: Kluyveromyces ; Candida utilis ; Kluyver effect ; chemostat ; biomass ; whey ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Many facultatively fermentative yeast species exhibit a “Kluyver effect”: even under oxygen-limited growth conditions, certain disaccharides that support aerobic, respiratory growth are not fermented, even though the component monosaccharides are good fermentation substrates. This article investigates the applicability of this phenomenon for high-cell-density cultivation of yeasts. In glucose-grown batch cultures of Candida utilis CBS 621, the onset of oxygen limitation led to alcoholic fermentation and, consequently, a decrease of the biomass yield on sugar. In maltose-grown cultures, alcoholic fermentation did not occur and oxygen-limited growth resulted in high biomass concentrations (90 g dry weight L-1 from 200 g L-1 maltose monohydrate in a simple batch fermentation). It was subsequently investigated whether this principle could also be applied to Kluyveromyces species exhibiting a Kluyver effect for lactose. In oxygen-limited, glucose-grown chemostat cultures of K. wickerhamii CBS 2745, high ethanol concentrations and low biomass yields were observed. Conversely, ethanol was absent and biomass yields on sugar were high in oxygen-limited chemostat cultures grown on lactose. Batch cultures of K. wickerhamii grown on lactose exhibited the same growth characteristics as the maltose-grown C. utilis cultures: absence of ethanol formation and high biomass yields. Within the species K. marxianus, the occurrence of a Kluyver effect for lactose is known to be strain dependent. Thus, K. marxianus CBS 7894 could be grown to high biomass densities in lactose-grown batch cultures, whereas strain CBS 5795 produced ethanol after the onset of oxygen limitation and, consequently, yielded low amounts of biomass. Because the use of yeast strains exhibiting a Kluyver effect obviates the need for controlled substrate-feeding strategies to avoid oxygen limitation, such strains should be excellently suited for the production of biomass and growth-related products from low-cost disaccharide-containing feedstocks. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 659-666 
    ISSN: 0006-3592
    Keywords: suspension culture ; insect cells ; baculovirus ; multiplicity of infection ; time of infection ; model ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In vitro infection of insect cells with baculoviruses is increasingly considered a viable means for the production of biopesticides, recombinant veterinary vaccines, and other recombinant products. Batch fermentation processes traditionally employ intermediate to high multiplicities of infection necessitating two parallel scale-up processes - one for cells and one for virus. In this study, we consider the use of multiplicities of infection as low as 0.0001 plaque-forming units per cell, a virus level low enough to enable infection of even large reactors (e.g., 10 m3) directly from a frozen stock. Using low multiplicities in the Sf9/β-gal-AcNPV system, recombinant protein titers comparable with the maximum titer observed in high multiplicity infections were achieved. Cultures yielding the maximum titer were characterized by reaching a maximum cell density between 3 and 4 × 109 cell L-1. This optimal cell yield did not depend on the multiplicity of infection, supporting the existing view that batch cultures are limited by availability of substrate. Up to a certain cell density, product titer will increase almost linearly with availability of biocatalyst, that is, cells. Beyond this point any further cell formation comes at the expense of final product titer. Low multiplicity infections were found not to cause any significant dispersion of the protein production process. Hence, product stability is not a major issue of concern using low multiplicities of infection. The sensitivity to initial conditions and disturbances, however, remains an issue of concern for the commercial use of low multiplicity infections. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 700-708 
    ISSN: 0006-3592
    Keywords: alcohol dehydrogenase ; enzyme ; water sorption isoterm ; gas phase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The adsorption of water by alcohol dehydrogenase from baker's yeast (YADH) has been measured in a continuous-flow gas reactor at varying temperatures. Adsorption isotherms in the presence of gaseous organic substrates are compared to those from organic-free gas mixtures. Almost no effect of the hydrophobic molecule on total water adsorption was observed. A rarely mentioned multilayer isotherm model from the 1930s, the Huttig's isotherm, has been found to fit the experimental data with extremely good accuracy. The model enables the calculation of both the heat of adsorption of water to the enzyme and the total amount of water necessary for monolayer coverage. The heat of adsorption of water in the first layer is approximately -16 kcal/mol. This tight binding of water, which is much higher than the heat of condensation of pure water, helps to explain the kinetic properties of YADH-catalyzed reactions on vapor phase substrates. While the monolayer coverage is temperature independent, the enzyme demonstrates hysteresis when transitioning between adsorption and desorption. The hysteresis observed in water sorption studies may also explain previously reported properties of the enzyme. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 699-699 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
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  • 41
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    Biotechnology and Bioengineering 50 (1996), S. 24-35 
    ISSN: 0006-3592
    Keywords: biofilm ; interspecies competition ; spatial microbial distribution ; heterotrophs ; nitrifiers ; microslicing ; model simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Spatial microbial distributions of nitrifiers and heterotrophs in undefined mixed-population biofilms were experimentally investigated using a microslicer technique and correlated with nitrification efficiency of the biofilm system. The general stratification of different bacterial groups in the biofilm was simulated using a one-dimensional (1-D) mathematical biofilm accumulation model (BAM) and compared with the experimental results. Biofilms were cultured at three C : N ratios of feed solutions in a partially submerged rotating biological contactor (RBC). It was shown that the biofilms were vertically stratified (from biofilm surface to substratum). At C : N = 0, heterotrophs and nitrifiers coexisted in the outermost biofilm and heterotrophs dominated in the innermost biofilm. At C : N = 1.5, heterotrophs outcompeted nitrifiers for dissolved oxygen and space; thus, heterotrophs dominated in the outermost biofilm and nitrifiers were present only in the deeper biofilm. Nitrifiers and heterotrophs coexisted in the innermost biofilm. An increase in the influent C : N ratio resulted in stronger stratification of microbial species, as well as inhibition of nitrification. In batch experiments, NH4—N utilization rate (RNH4—N) was almost the same at each substrate C : N ratio even though NH4 oxidizers were predominantly present in the deeper biofilm. The biofilm performance could not be sufficiently explained by the obtained microbial spatial distribution, suggesting that one-dimensional description of microbial distribution was not good enough and three-dimensional measurements of microbial spatial distribution is necessary. Total bacterial densities increased by a factor of 3-17 with biofilm depth. The metabolically active cell fraction decreased from 35 ± 13% in the outermost biofilm to 15 ± 4% in the innermost biofilm, presumably due to substrate limitation. The model predicted more pronounced stratification of nitrifiers and heterotrophs than the observed results. This discrepancy could be attributed to the real biofilms that were structurally heterogeneous (e.g., water channels), which could not be described by the one-dimensional model. The results of this study clearly indicate the limitation of 1-D biofilm models to describe the extent of stratification of nitrifiers and heterotrophs and suggest a 3-D model is necessary. © 1996 John Wiley & Sons, Inc.
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  • 42
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    Biotechnology and Bioengineering 50 (1996), S. 65-72 
    ISSN: 0006-3592
    Keywords: somatic embryo ; plant cell culture ; image analysis ; pattern recognition ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Somatic embryogenesis is among the most promising means of large scale plant micropropagation. The development of somatic embryos is characterized by their morphological changes. Embryos in culture usually exhibit high heterogeneity and abnormality. As conventional microscopic observation is laborious and subjective, an objective and quantitative morphokinetic description is important for further advancement of this important process technology. We developed an image analysis system capable of measuring morphological and size features of embryos. Subtle environmental effects on embryo development, which are often masked by the subjectivity of microscopic observation, are now discernible by statistically comparing the distributions of these morphological and size features. This image analysis and pattern recognition system was applied to examine the kinetics of a fed-batch culture. © 1996 John Wiley & Sons, Inc.
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  • 43
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    Biotechnology and Bioengineering 50 (1996), S. 108-114 
    ISSN: 0006-3592
    Keywords: β-galactosidase ; overexpression ; runaway replication vectors ; translational fusions ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: To determine the utility of coupling runaway replication to the expression of cloned genes under the control of strong promoters, lacZ transcriptional fusions to the trp or tac promoter (Ptrp or Ptac) were constructed using plasmids in which the copy number is thermally regulated. Cells containing these plasmids were able to produce β-galactosidase to levels between 3700 and 46,000 Miller units when induced only by a temperature upshift. The addition of the appropriate chemical inducer, either IPTG (isopropyl-β-D-thiogalactopyranoside) or IAA (3-β-indoleacrylic acid), did not significantly enhance the thermal induction. The Ptac-controlled and Ptrp-controlled lacZ induction differed slightly in that the Ptac-controlled thermal induction exhibited a lag of approximately 1.5 h as compared to both chemical and thermal induction, whereas in the case of Ptrp-controlled induction, an increase in β-galactosidase expression above background occurred at approximately the same time regardless of the means of induction. The best vector, a Ptrp-controlled lacZ fusion carried on a runaway replication vector having a basal copy number of 10, was able to mediate the expression of β-galactosidase to approximately 40,000 Miller units of β-galactosidase comprising 25% of the total cell protein at 17 h postinduction under optimal conditions for protein yield. In these cells, lysis occurred as lacZ was maximally expressed. Under noninducing conditions, the plasmids were stable for at least 60 generations in the absence of antibiotic in batch culture. © 1996 John Wiley & Sons, Inc.
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  • 44
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    Biotechnology and Bioengineering 50 (1996), S. 136-144 
    ISSN: 0006-3592
    Keywords: sulfate-reducing bacteria ; biofilm ; immobilization ; gas-lift reactor ; carbon monoxide ; synthesis gas ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Biological sulfate reduction was studied in laboratory-scale gas-lift reactors. Synthesis gas (gas mixtures of H2/CO/CO2) was used as energy and carbon source. The required biomass retention was obtained by aggregation and immobilization on pumice particles. Special attention was paid to the effect of CO addition on the sulfate conversion rate, aggregation, and aggregate composition.Addition of 5% CO negatively affected the overall sulfate conversion rate; i.e., it dropped from 12-14 to 6-8 g SO2-4/L day. However, a further increase of CO to 10 and 20% did not further deteriorate the process. With external biomass recycling the sulfate conversion rate could be improved to 10 g SO2-4/L day. Therefore biomass retention clearly could be regarded as the rate-limiting step. Furthermore, CO affected the aggregate shape and diameter. Scanning electron microscopy (SEM) photographs showed that rough aggregates pregrown on H2/CO2 changed into smooth aggregates upon addition of CO. Addition of CO also changed the aggregate Sauter mean diameter (d32) from 1.7 mm at 5% CO to 2.1 mm at 20% CO. After addition of CO, a layered biomass structure developed. Acetobacterium sp. were mainly located at the outside of the aggregates, whereas Desulfovibrio sp. were located inside the aggregates. © 1996 John Wiley & Sons, Inc.
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  • 45
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    Biotechnology and Bioengineering 50 (1996), S. 197-202 
    ISSN: 0006-3592
    Keywords: poly-3-hydroxybutyrate (PHB) ; Alcaligenes latus ; high-cell-density fed-batch culture ; pH stat ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Alcaligenes latus, a growth-associated PHB producer, was cultivated by a pH-stat modal fed-batch culture technique to attain high PHB productivity. Both sucrose solution and inorganic medium were fed in conjunction with the supply of ammonia solution which serves as a nitrogen source and as a means of pH control. Compositions of the inorganic medium were formulated by elemental analysis of A. latus cell mass. The effect on inoculum size was examined to reduce culture time. High concentrations of cell (142 g/L) and PHB (68.4 g/L) were obtained in a short culture time (18 h) with an inoculum size of 13.7 g/L. The PHB content and the PHB productivity at the end of the fed-batch culture were 50% of dry cell weight and 4.0 g PHB/(L · h), respectively. © 1996 John Wiley & Sons, Inc.
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  • 46
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    Biotechnology and Bioengineering 50 (1996), S. 222-227 
    ISSN: 0006-3592
    Keywords: γ-poly(glutamate) ; γ-PGA ; Bacillus licheniformis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bacillus licheniformis ATCC 9945A was grown on Medium E in batch fermentations in which the pH was maintained at 5.5., 6.5, 7.4, and 8.25. The effects of pH on cell growth, carbon source utilization, and γ-polyglutamic acid (γ-PGA) production, molecular weight, and polymer stereochemistry were determined. The γ-PGA yield was highest (15 g/L, 96 h growth time) at pH 6.5. The increase in γ-PGA formation at pH 6.5 corresponded with a relatively high specific production rate at high γ-PGA concentration (0.09 h-1, ∼15 g/L γ-PGA). In contrast, the specific γ-PGA production rates at fermentor pH values of 5.5 and 7.4 decreased significantly for γ-PGA fermentor yields 〉∼5 g/L. Interestingly, alteration of the medium pH had little to no significant effects on the product quality as measured by stereochemical composition and molecular weight. While glutamate and glycerol utilization were similar as a function of pH, citrate consumption increased at pH 6.5, indicating that the formation of γ-PGA from citrate at pH 6.5 was of increased importance. The effect of aeration was evaluated by increasing the agitation speed (250 to 800 rpm) and aeration rate (0.5 to 2.0 L/min) at pH 6.5, the pH of maximal γ-PGA production. Increased aeration resulted in doubling of the cell dry weights (2 to 4 g/L), increasing γ-PGA yields (6.3 to 23 g/L by 48 h) and increasing in the maximum γ-PGA-specific production rate (0.09 to 0.11 h-1). Other effects of increased agitation included a rapid depletion of glutamate and citrate (by 50 h) and a decrease in product molecular weight. Despite the increase in agitation and aeration, oxygen limitation of the culture was not avoided, because the partial pressure decreased to 〈1.0% by 29 h. © 1996 John Wiley & Sons, Inc.
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  • 47
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    Biotechnology and Bioengineering 50 (1996), S. 238-247 
    ISSN: 0006-3592
    Keywords: hybridomas ; monoclonal antibody ; kinetic model ; instability ; nutrient and product effects ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An attempt has been made to mathematically describe and analyze monoclonal antibody (MAB) productivity of hybridoma cells, with particular emphasis on continuous cultures under unsteady-state conditions. A simple and unstructured general kinetic model that takes account of productivity loss during long-term cultivation, cell proliferation, and the effects of nutrients and toxic products is proposed. The model is verified with data of continuous culture from five different cell lines under a wide range of experimental conditions. Analysis of these results showed that for a reliable assessment of effects of different factors and for comparison of kinetic data on MAB production it is important to consider possible loss of MAB productivity, the time dependence of which can be modeled by an exponential function plus a constant term. Variations of nutrient concentration, particularly that of glucose, glutamine, and serum, can significantly alter MAB production under certain conditions. These effects can be described in terms of saturation kinetic and/or noncompetitive inhibition kinetics. © 1996 John Wiley & Sons, Inc.
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  • 48
    ISSN: 0006-3592
    Keywords: metabolic engineering ; CHO cell ; E2F-1 ; serum-free cell culture ; two-dimensional electrophoresis of proteins ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Engineering of the cell cycle can be an effective means for bypassing growth factor requirements of animal cells. Cloned human E2F-1 from Nalm 6 cells was subcloned into pRc/CMV and transfected into Chinese hamster ovary (CHO) cells. Ten stable transfectant clones isolated from cells cultured under neomycin-resistance selection pressure all expressed significantly higher amounts of E2F-1 than control cells as determined by Western analysis. Confocal immunofluorescent microscopy and Southern analysis of several clones also provided evidence for the expression of cloned E2F-1 in these cells. CHO K1:E2F-1 cells are able to proliferate on well-defined serum- and protein-free basal medium and exhibit an S-phase extended by 65% compared to CHO K1 cells mitogenically stimulated by basic fibroblast growth factor (bFGF). Two-dimensional electrophoresis of the intracellular proteins of E2F-1 clones shows an increase in 236 gene products compared to CHO K1 control cells, further verifying a functional regulatory role of cloned E2F-1 in CHO cells. Among these upregulated species is the cell cycle regulatory protein, cyclin A, which has already been shown to be regulated by E2F-1 in human fibroblasts. Overexpression of cloned E2F-1 in CHO cells is a potentially useful new strategy for bypassing serum requirements in mammalian cell culture. Furthermore, such cell cycle control stimulus-protein pattern response data can contribute to a clearer understanding of complex multigene networks involved in mammalian cell cycle regulation. © 1996 John Wiley & Sons, Inc.
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  • 49
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    Biotechnology and Bioengineering 50 (1996), S. 291-298 
    ISSN: 0006-3592
    Keywords: stoichiometric model ; medium design ; microbial transglutaminase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A stoichiometric model was developed for the application of medium design in microbial transglutaminase production by Streptoverticillium mobaraense. The model avoids dealing with all the metabolic reactions involved by simply lumping them into a single reaction. With the help of measurement results, an analysis of the nutrients' roles, and biochemical knowledge of the microorganism, all stoichiometric coefficients in the model were calculated. These coefficients were used for medium design. With this designed medium, microbial transglutaminase activity was increased fourfold, compared to that in the basal medium. © 1996 John Wiley & Sons, Inc.
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  • 50
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    Biotechnology and Bioengineering 50 (1996), S. 341-346 
    ISSN: 0006-3592
    Keywords: glycolate oxidase ; Aspergillus nidulans ; heterologous expression ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The biocatalytic production of glyoxylic acid from glycolic acid requires two enzymes: glycolate oxidase, which catalyzes the oxidation of glycolic acid by oxygen to produce glyoxylic acid and hydrogen peroxide, and catalase, which decomposes the byproduct hydrogen peroxide. As an alternative to isolation from the leaf peroxisomes of spinach, glycolate oxidase has now been cloned and expressed in transformants of Aspergillus nidulans T580 at levels ranging from 1.7 to 36 IU/g dry wt. cells. The glycolate oxidase of transformant strain T17 comprises ca. 1.9% of total cell protein and is expressed at near 100% activity. © 1996 John Wiley & Sons, Inc.
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  • 51
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    Biotechnology and Bioengineering 50 (1996), S. 365-373 
    ISSN: 0006-3592
    Keywords: hydrogel ; diffusion ; alginate ; agarose ; cell encapsulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Current membrane-based bioartificial organs consist of three basic components: (1) a synthetic membrane, (2) cells that secrete the product of interest, and (3) an encapsulated matrix material. Alginate and agarose have been widely used to encapsulate cells for artificial organ applications. It is important to understand the degree of transport resistance imparted by these matrices in cell encapsulation to determine if adequate nutrient and product fluxes can be obtained. For artificial organs in xenogeneic applications, it may also be important to determine the extent of immunoprotection offered by the matrix material. In this study, diffusion coefficients were measured for relevant solutes [ranging in size from oxygen to immunoglobulin G (IgG)] into and out of agarose and alginate gels. Alginate gels were produced by an extrusion/ionic crosslinking process using calcium while agarose gels were thermally gelled. The effect of varying crosslinking condition, polymer concentration, and direction of diffusion on transport was investigated. In general, 2-4% agarose gels offered little transport resistance for solutes up to 150 kD, while 1.5-3% alginate gels offered significant transport resistance for solutes in the molecular weight range 44-155 kD - lowering their diffusion rates from 10- to 100-fold as compared to their diffusion in water. Doubling the alginate concentration had a more significant effect on hindering diffusion of larger molecular weight species than did doubling the agarose concentration. Average pore diameters of approximately 170 and 147 Å for 1.5 and 3% alginate gels, respectively, and 480 and 360 Å for 2 and 4% agarose gels, respectively, were estimated using a semiempirical correlation based on diffusional transport of different-size solutes. The method developed for measuring diffusion in these gels is highly reproducible and useful for gels crosslinked in the cylindrical geometry, relevant for studying transport through matrices used in cell immobilization in the hollow fiber configuration. © 1996 John Wiley & Sons, Inc.
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  • 52
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    Biotechnology and Bioengineering 50 (1996), S. 382-391 
    ISSN: 0006-3592
    Keywords: liver ; artificial organs ; hepatic encephalopathy ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Despite recent advances in medical therapy, patients with fulminant hepatic failure (FHF) have a mortality rate approaching 90%. Many patients die because of failure to arrest the progression of cerebral edema. Liver transplantation has improved survival to 65% to 75%. However, there is a shortage of donors and approximately one half of the patients with FHF will die while awaiting liver transplantation. There is thus a need to develop an extracorporeal liver assist system to help keep these patients alive and neurologically intact until either an organ becomes available for transplantation or the native liver recovers from injury. Such a system could also be used during the period of functional recovery from massive liver resection or to assist patients with decompensated chronic liver disease. Over the years, various methods utilizing charcoal and resin hemoperfusion, dialysis, plasma exchange, and other methods of blood detoxification have been developed and tested, but none have gained wide acceptance. This was due to: (i) incomplete understanding of the pathophysiology of liver failure; (ii) lack of accurate methods of assessment, quantitation, and stratification of the degree of liver dysfunction; and (iii) inadequate numbers of prospective controlled clinical trials examining the effects of specific therapeutic modalities. Liver support systems utilizing liver tissue preparations were developed in the 1950s, but it was not until recently that advances in hepatocyte isolation and culture, better understanding of hepatocyte-matrix interactions, and improved hollow-fiber technology have resulted in the development of a new generation of liver assist devices. Some of these devices are currently being tested in the clinical setting. In a preliminary clinical study, we have used a porcine hepatocyte-based liver support system to treat patients with acute liver failure as well as patients with acute exacerbation of chronic liver disease. Patients in the first group, who were candidates for transplantation, were successfully bridged to a transplant with excellent survival. No obvious benefit from bioartifical liver treatments was seen in the second group. It is possible that, in this group, patients will have to be treated earlier and for longer periods of time. Prospective controlled trials will be initiated as soon as the current phase I study is concluded to determine the efficacy of this system in both patients populations. © 1996 John Wiley & Sons, Inc.
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  • 53
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    Biotechnology and Bioengineering 50 (1996), S. 609-616 
    ISSN: 0006-3592
    Keywords: enzyme inactivation ; substrate modulation ; product modulation ; penicillin acylase ; 6-aminopenicillanic acid ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Inactivation of immobilized penicillin acylase has been studied in the presence of substrate (penicillin G) and products (phenylacetic acid and 6-aminopenicillanic acid), under the hypothesis that substances which interact with the enzyme molecule during catalysis will have an effect on enzyme stability. The kinetics of immobilized penicillin acylase inactivation was a multistage process, decay constants being evaluated for the free-enzyme and enzyme complexes, from whose values modulation factors were determined for the effectors in each enzyme complex at each stage. 6-Aminopenicillanic acid and penicillin G stabilized the enzyme in the first stage of decay. Modulation factors in that stage were 0.96 for penicillin G and 0.98 for 6-aminopenicillanic acid. Phenylacetic acid increased the rate of inactivation in both stages, modulating factors being -2.31 and -2.23, respectively. Modulation factors influence enzyme performance in a reactor and are useful parameters for a proper evaluation. © 1996 John Wiley & Sons, Inc.
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  • 54
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    Biotechnology and Bioengineering 50 (1996), S. 636-642 
    ISSN: 0006-3592
    Keywords: genetic manipulation ; stationary-phase genes ; recombinant protein ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Genetic manipulation of the host strain, by which cell physiology could be modulated, was exploited to enhance recombinant protein production in Escherichia coli. The effects of an inactivated stationary-phase gene (rmf or katF) on recombinant protein production in strains with two different expression systems (the pH-inducible and the lac promoters) were investigated. An improvement of recombinant protein production in the katF mutant at low growth rates was observed for both expression systems. A fourfold and a 30% increase in the volumetric recombinant protein activity were observed for the pH-inducible and the lac promoter system, respectively. The effect of the rmf mutation, on the other hand, depends on the expression system. A twofold increase in the volumetric recombinant protein activity was found for the pH-inducible promoter system, but there was no improvement for the lac promoter system. Improvement in culture performance for slow-growing cultures may have an impact on the design strategy of the host/vector system used in fed-batch cultures, where the specific growth rate is usually slow. The information may also be useful for developing optimal host/vector gene expression systems for recombinant protein production. © 1996 John Wiley & Sons, Inc.
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  • 55
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    Biotechnology and Bioengineering 50 (1996), S. 643-654 
    ISSN: 0006-3592
    Keywords: specific energy dissipation rate ; fluidized-bed bioreactor ; biofilm thickness ; bed expansion ; stratification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: An innovative hydrodynamic parameter, specific energy dissipation rate (ω), is proposed and defined as the energy dissipation at the biofilm surface (by erosive effect of flowing water surrounding the bioparticle) per unit volume of fluidized-bed bioreactor per unit time. From the simulated results, ω is varied with operating flow rate and bed expansion characteristics. The biofilm thickness (δ) is found to be inversely proportional to ω. A small ω value benefits the growth of a thick biofilm. Thus, at different stages (e.g., during start-up and at different biofilm thicknesses) the model can be applied to predetermine a better operating scheme. The experimental results also show that the steady-state biofilm thickness measured in the upper and lower parts of the bioreactors is inversely proportional to ω values. Biofilm thickness and ω in the upper part of the bioreactors are respectively larger and smaller than those in the lower part. In addition, by referring to the published data, δ correlates well with ω, and thus the proposed model is well verified. © 1996 John Wiley & Sons, Inc.
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  • 56
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    Biotechnology and Bioengineering 50 (1996), S. 687-692 
    ISSN: 0006-3592
    Keywords: hydration state of support ; colyophilized enzyme ; lyophilization ; subtilisin-A ; enzymatic optical resolution ; organic solvent ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Subtilisin-A was colyophilized with various types of support materials, such as Amberlite IRC-50, Celite545, chitosan, DEAE-cellulose, DOWEX-1, zeolite, glass bead, and polystyrene. The colyophilized enzyme was used for the optical resolution of racemic 1-phenylethylamine with 2,2,2-trifluoroethylbutyrate in 3-methyl-3-pentanol. The enzyme activity in organic media changed dramatically according to the hydration state of the support materials before lyophilization. This effect was especially marked with supports of high water capacity (aquaphilicity), such as chitosan and DEAE-cellulose. By hydrating these supports of high aquaphilicity prior to lyophilization, subtilisin-A activity in organic media increased ca. 4-8 times, depending upon the supports used. This result suggests that the hydration state of aquaphilic support materials for colyophilization is critical to determining enzyme activity in organic solvents. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 58
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    Biotechnology and Bioengineering 50 (1996), S. 709-717 
    ISSN: 0006-3592
    Keywords: phenol biodegradation ; wastewater treatment ; oxygen consumption rate ; substrate inhibition ; active diffusion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The reaction kinetics for phenol biodegradation at low substrate concentrations can be estimated based on the analysis of changes in the dissolved oxygen concentration in the bulk liquid during biodegradation. The measured oxygen concentration changes with an interesting behavior as biodegradation proceeds. The oxygen concentration in the bulk liquid decreases rapidly in the early stages of degradation and subsequently decreases linearly and then rapidly recovers to the initial saturated level. Taking into account the oxygen transfer rate between gas and liquid phases and oxygen consumption rate by microbes, the change in the dissolved oxygen concentration can be simulated with an unsteady state mass balance equation and three kinetic models for the rate of phenol metabolism: a substrate-inhibited model; a zero-order model; and a combined model. In the combined model, it is assumed that, at phenol concentrations above 10 mg/L, the degradation rate is expressed by a substrate-inhibited model; whereas at concentrations below 10 mg/L the zero-order model is applied. It was found that the characteristics of the change in the dissolved oxygen concentration, especially the rapid increase at the end of degradation, can only be described by the combined kinetic model. This result suggests that conventional Haldane-type kinetics would be unsuitable for estimating the phenol consumption rate at low phenol concentrations, in particular, at concentrations less than 10 mg/L. © 1996 John Wiley & Sons, Inc.
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  • 59
    ISSN: 0006-3592
    Keywords: halogenated compounds ; basidiomycetes ; Bjerkander adusta ; flavors ; membrane inlet mass spectrometry (MIMS) ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Membrane inlet mass spectrometry has been used for the characterization of halogenated organic compounds produced by the fungus Bjerkandera adusta. Using this technique we obtained electron impact-, chemical ionization-, electron capture negative chemical ionization-mass spectra and tandem mass spectra directly from the growth medium. Through this direct analysis of the samples we identified novel bioconversion products and confirmed recently published data on the production of both chlorinated and brominated methoxybenzaldehyde metabolites. Growth profiles of the culture grown on a defined medium showed that the production of secondary metabolites starts after approximately 6 days and reaches maximal concentrations of 25-250 μM after 15-20 days. Although delayed, the production of secondary metabolites paralleled a depletion of glucose from the medium and stopped shortly after all glucose had been consumed. Experiments in which fluoro- and bromo-labeled 4-methoxybenzaldehydes were added to the medium at day 8 showed biotransformation of these compounds into chloro-3-fluoro-4-methoxy-benzaldehyde and chloro-3-bromo-4-methoxybenzaldehyde, respectively. No dichlorinated products were observed, suggesting that halogenation takes place only at the meta position on the 4-methoxybenzaldehydes. These experiments are the first to bring direct evidence of a halogenation mechanism, where the enzymatic attack takes place directly on the 4-methoxybenzaldehyde intermediates. © John Wiley & Sons, Inc.
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  • 60
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    Biotechnology and Bioengineering 51 (1996), S. 51-60 
    ISSN: 0006-3592
    Keywords: photobioreactor ; solar irradiance ; diffuse light ; cell density ; biomass productivity ; Monodus subterraneus ; Anabaena siamensis ; Spirulina platensis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A flat inclined modular photobioreactor (FIMP) for mass cultivation of photoautotrophic microorganisms is described. It consists of flat glass reactors connected in cascade facing the sun with the proper tilt angles to assure maximal exposure to direct beam radiation. The optimal cell density in reference to the length of the reactor light path was evaluated, and the effect of the tilt angle on utilization of both direct beam as well as diffuse sunlight was quantitatively assessed. The mixing mode and extent were also optimized in reference to productivity of biomass. The FIMP proved very successful in supporting continuous cultures of the tested species of photoautotrophs, addressing the major criteria involved in design optimization of photobioreactors: Made of fully transparent glass, inclined toward the sun and endowed with a high surface-to-volume ratio, it combines an optimal light path with a vigorous agitation system. The maximal exposure to the culture to solar irradiance as well as the substantial control of temperature facilitate, under these conditions, a particularly high, extremely light-limited optimal cell density. The integrated effects of these growth conditions resulted in record volumetric and areal output rates of Monodus subterraneus, Anabana siamensis, and Spirulina platensis. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 148-156 
    ISSN: 0006-3592
    Keywords: surfactant ; lipase ; Naproxen ; esterification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: In the enantioselective esterification of racemic Naproxen with trimethylsilyl methanol in isooctane by Candida cylindracea lipase, improvements in (S)-naproxen ester productivity and enzyme selectivity were demonstrated by adding bis(2-ethylhexyl) sodium sulfosuccinate (AOT) as the best surfactant. The effect of water content on the enhancement of enzyme activity was elucidated from the reduced adsorption of surfactant molecules on the lipase. A competitive inhibition by the alcohol and a noncompetitive inhibition by the surfactant to the enzyme were found from the kinetic analysis. By using a two-phase extraction, a complete separation of the surfactant from the organic solution was obtained. © 1996 John Wiley & Sons, Inc.
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  • 62
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    Biotechnology and Bioengineering 51 (1996), S. 157-162 
    ISSN: 0006-3592
    Keywords: calcium-alginate capsules ; microencapsulation ; invertase ; recombinant Saccharomyces cerevisiae ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: As a means of integrating cell growth and immobilization, recombinant Saccharomyces cerevisiae cells with invertase activity were immobilized in liquid-core alginate capsules and cultured to a high density. S. cerevisiae cells of SEY 2102 (MAT α ura3-52 leu2-3, 112 his4-519) harboring plasmid pRB58 with the SUC2 gene coding for invertase were grown to 83 g/L of liquid-core volume inside the capsule on a dry weight basis. The cloned invertase was expressed well in the immobilized cells with slightly higher activity than the free cells in a batch culture. Invertase in the immobilized cells showed slightly more improved thermal stability than in the free cells. Storage in a Na-acetate buffer at 4°C and 10°C for 1 month resulted in 7% and 8% loss in activity, respectively. The sucrose hydrolysis reaction was stably maintained for 25 repeated batches for 7 days at 30°C. Continuous hydrolysis of 0.3 M sucrose was carried out in a packed bed reactor with a conversion of more than 90% at a maximum productivity of 55.5 g glucose/L per hour for 7 days. In a continuous stirred tank reactor, the maximum productivity of 80.8 g glucose/L per hour was achieved at a conversion of 59.1% using 1.0 M sucrose solution, and 0.5 M sucrose solution was hydrolyzed for 1 week with a 95% conversion at a productivity of 48.8 g/L per hour. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 177-189 
    ISSN: 0006-3592
    Keywords: Corynebacterium ; intracellular flux ; metabolism network ; growth phase ; mixture of carbon sources ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The distribution of carbon in the metabolic network of a bacterial cell was estimated by a mass-balance-based intracellular flux computation method. It was applied to the growth phase of Corynebacterium melassecola, a glutamic acid producing bacterium, using experimental production yields of biomass, lactate and acetate measured during batch cultures on glucose, fructose, and various mixtures of both sugars. This flux computation method identifies the direction of the 86 reactions that ensure proper metabolic function during the growth phase of C. melassecola. Flux ratios allow comparison of calculated and relevant experimental yields. The results highlight the key influence of the biomass production yield YX-O2 on the overall distribution of carbon; the proportion of carbon drained in the pentose-P pathway fell from a value in the range of 54% to 47% on media containing glucose (YX-O2 = 1.75 to 1.56 g X/g O2) to 37% on fructose medium (YX-O2 = 1.36 g X/g O2). The highest maintenance requirement was calculated on fructose medium (Jm = 290 mol ATP/100 mol fructose) which must be connected to a lower efficiency of cell multiplication observed on this substrate. Another important result was that the significant decreases in experimental values of production yields and rates observed on fructose medium which were related to the operation of the FBPase. In particular, it was estimated that, as long as the proportion of glucose in the carbon source remains above 22% (78% fructose), the operation of the FBPase is not necessary and the bacteria exhibit behavior similar to that observed on glucose alone; this result is consistent with experimental observations. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 206-214 
    ISSN: 0006-3592
    Keywords: animal cells ; biomass activity ; oxygen solubility ; software sensor ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A software sensor was developed to determine the volumetric biomass activity of animal cell cultivations on-line. It was based on the on-line estimation of the ATP-production rate from the oxygen uptake and the lactic-acid production rate. The sensor was verified for a batch culture of Vero cells, and a batch and a continuous culture of hybridoma cells. For the hybridoma cells, the sensor showed a good correlation with the biomass concentration. However, this was not the case for the Vero cells. As soon as glutamine was exhausted, the biomass activity stabilized, whereas the amount of biomass almost doubled. Because the sensor developed responds to nutrient limitations much faster than becomes visible through cell density measurements, and because the volumetric biomass activity can be related to the volumetric consumption rates and production rates of important metabolites, it shows excellent possibilities for control purposes. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 327-341 
    ISSN: 0006-3592
    Keywords: Candida rugosa ; immobilization ; olive oil hydrolysis ; phenylglycidate ; glutaraldehyde ; adipic dihydrazide ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The aim of this study was to evaluate the immobilization of lipase from Candida rugosa on a nylon support by methods used to attach biomolecules to solid supports through their carbohydrate moieties. The carbohydrate groups were converted to dialdehydes by treatment with sodium periodate. The length of exposure and the periodate amount were optimized to the point where almost total activity retention was obtained. Tests of the immobilized enzyme showed the expressed activity to be significantly higher than the activity obtained with the unimmobilized enzyme. The use of reverse micelles as a way of delivering water to the enzyme was tested and found to give significantly higher activities. The immobilized enzyme activity was also tested with other substrates, one of which was a chiral ester. The immobilized enzyme was found to have high stereoselective efficiency and activity toward racemic methyl methoxyphenyl glycidate, a chiral intermediate used in the manufacture of the drug diltiazem. © 1996 John Wiley & Sons, Inc.
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  • 66
    ISSN: 0006-3592
    Keywords: trichloroethylene ; methane monooxygenase ; Methylosinus trichosporium ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: By complementing cell-free extracts of Pseudomonas putida F1/pSMMO20 with purified soluble methane monooxygenase (sMMO) components of Methylosinus trichosporium OB3b, the low cloned-gene sMMO activity in the recombinant strain was found to be due to incomplete activity of the hydroxylase component. To address this incomplete activity, additional sMMO-expressing strains were formed by transferring mmo-containing pSMMO20 and pSMMO50 into various bacterial species including pseudomonads and α-2 subdivision strains such as methanotrophs, methylotrophs, Agrobacterium tumefaciens A114, and Rhizobium meliloti 102F34 (11 new strains screened); sMMO activity was detected in the last two strains. To increase plasmid segregational stability, the hok/sok locus originally from Escherichia coli plasmid R1 was inserted downstream of the mmo locus of pSMMO20 (resulting in pSMMO40) and found to enhance plasmid stability in P. putida F1 and R. meliloti 102F34 (first report of hok/sok in Rhizobium). To further increase sMMO activity, a modified Whittenbury minimal medium was selected from various minimal and complex media based on trichloroethylene (TCE) degradation and growth rates and was improved by removing the sMMO-inhibiting metal ions [Cu(II), Ni(II), and Zn(II)] and chloramphenicol from the medium and by supplementing with an iron source (3.6 μM of ferrous ammonium sulfate). Using chemostat-grown P. putida F1/pSMMO40, it was found that sMMO activity was higher for cells grown at higher dilution rates. These optimization efforts resulted in a twofold increase in the extent of TCE degradation and more consistent sMMO activity. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 360-370 
    ISSN: 0006-3592
    Keywords: induction ; Escherichia coli ; biofilms ; immobilization ; protein synthesis in starved bacteria ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Activation and regeneration of whole cell biocatalytic activity via initial and subsequent induction of the lacZ gene was investigated in starved Escherichia coli using a novel synthetic biofilm. Stationary-phase bacteria were entrapped in 10-80 μm thick multi-layer films, where a copolymer of acrylic and vinyl acetate was the immobilization matrix. The E. coli were placed in a defined starvation medium containing essentially no nitrogen or carbon source and induced initially using lactose or isopropylthiogalactoside (IPTG). Subsequent inductions were performed with IPTG. Comparison studies with suspended bacteria showed that when IPTG was the initial inducing agent, induction kinetics are linear for both immobilized and suspended cells. After induction with lactose, however, a lag time is noted for suspended cells, but not for E. coli in the biofilm. Biocatalytic activity was successfully regenerated by re-inducing starved suspended cells 1-3 days after an initial induction with lactose. This regeneration was demonstrated in the synthesis of additional active β-galactosidase. However, immobilized cells could be re-induced for at least 17 days after the initial induction, and viability in the synthetic biofilms remained greater than 90%, demonstrating that periodic induction is a valuable method for extending the life of whole cell biocatalysts. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 422-433 
    ISSN: 0006-3592
    Keywords: tissue plasminogen activator ; multicell spheroids ; microcarrier ; Bowes melanoma cells ; cell cycle ; cellular protein ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Bowes melanoma cells synthesize more tissue plasminogen activator (tPA) in monolayer cultures than in multicell spheroids. Cellular production of tPA in these cells was measured during a cultivation period of 800 h. Without changing the cell culture assay, we were able to obtain monolayers, multilayers, and multicell spheroids (cell aggregates) by stirring microcarrier beads in 500-mL spinner flasks operated at 50 rpm. Thus, the medium conditions in the liquid were similar for cells in monolayers and in multicell spheroids. Probes for measurements of intracellular and extracellular parameters were taken from the same culture at distinct times; therefore, their variations during cultivation can directly be compared. Because cells were cultured in an unregulated (with regard to pH, glucose, etc.) spinner flask, their concentration was kept below 106 cells/mL, thus avoiding too fast and too severe depletion of oxygen and other medium factors. Nevertheless, the tPA productivity decreased from 8 ng/h/106 cells (monolayer) to 4 ng/h/106 cells (multicell spheroids with microcarrier nucleus, 800 μm diameter), matching the decrease of total cellular protein. Due to medium depletion, the cell cycle distribution changed from 45% to 68% G1 cells in a characteristic way during growth of multicell spheroids. This is accompanied by changes in amino acids, glucose, lactate, and pH, which may account for the reduction of tPA productivity. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 45-51 
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; δ sequences cloned genes ; integration ; stability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The chromosomal δ sequences of the yeast Saccharomyces cerevisiae were employed as recombination sites to integrate the bacterial neor gene and the yeast SUC2 gene into the yeast genome. A dominate selection method employing the aminoglycoside antibiotic G418 was used. Transformation efficiencies and growth behaviors of the transformants were studied. Transformants were obtained with more than 40 integrations; the majority of insertions were tandem with a maximum of three different insertion sites utilized at one time. After 70-100 generations of growth in nonselective medium, the high copy number SUC2-neor integrants were found to be unstable; only minor instability was observed for the neor and low copy number SUC2-neor integrants. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 78-86 
    ISSN: 0006-3592
    Keywords: crossflow microfiltration ; hydrodynamics ; fouling ; bioreactor ; Lactobacillus helveticus ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A filtration rig equipped with a tubular alumina membrane was used to study the performance of crossflow microfiltration of Lactobacillus helveticus. Experiments were performed at constant permeation flux. High cell concentrations and fast transient conditions to the stationary J adversely affected permeability. Membrane fouling was due to a fast irreversible layer formation and to a reversible cell cake. This microbial deposit characteristics were dependent on the ratio permeation flux/wall shear stress, J/τw. Fouling was faster and more severe when J/τw was greater than a critical value of 1.15 L-1 · h-1 · m-2 · Pa-1. The disordered structure of this cell cake seemed to lead to a macromolecule deposit between the cells which adversely affected the membrane permeability. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 49 (1996), S. 101-105 
    ISSN: 0006-3592
    Keywords: Xanthomonas maltophilia ; benzoic acid ; Vitreoscilla hemoglobin gene ; genetic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Xanthomonas maltophilia was transformed with the gene encoding Vitreoscilla (bacterial) hemoglobin, vgb, and the growth of the engineered strain was compared with that of the untransformed strain using benzoic acid as the sole carbon source. In general, growth of the engineered strain was greater than that of the untransformed strain; this was true for experiments using both overnight cultures and log phase cells as inocula, but particularly for the latter. In both cases the engineered strain was also more efficient than the untransformed strain in converting benzoic acid into biomass. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 91-97 
    ISSN: 0006-3592
    Keywords: waste-gas treatment ; trickle-bed reactor ; fungi ; biofilm ; toluene ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Removal of organic compounds like toluene from waste gases with a trickle-bed reactor can result in clogging of the reactor due to the formation of an excessive amount of biomass. We therefore limited the amount of nutrients available for growth, to prevent clogging of the reactor. As a consequence of this nutrient limitation a lower removal rate was observed. However, when a fungal culture was used to inoculate the reactor, the toluene removal rate under nutrient limiting conditions was higher. Over a period of 375 days, an average removal rate of 27 g C/(m3 h) was obtained with the reactor inoculated with the fungal culture. From the carbon balance over the reactor and the nitrogen availability it was concluded that, under these nutrient-limited conditions, large amounts of carbohydrates are probably formed. We also studied the application of a NaOH wash to remove excess biomass, as a method to prevent clogging. Under these conditions an average toluene removal rate of 35 g C/(m3 h) was obtained. After about 50 days there was no net increase in the biomass content of the reactor. The amount of biomass which was formed in the reactor equaled the amount removed by the NaOH wash. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 115-124 
    ISSN: 0006-3592
    Keywords: anaerobic degradation ; granulation ; plug-flow ; sludge, thermophilic ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The characteristics and development of thermophilic anaerobic sludge in upflow staged sludge bed (USSB) reactors were studied. The compartmentalized reactors were inoculated with partially crushed mesophilic granular sludge and then fed with either a mixture of volatile fatty acids (VFA) or a mixture of sucrose and VFA. The staged degradation of the soluble substrate in the various compartments led to a clear segregation of specific types of biomass along the height of the reactor, particularly in reactors fed with the sucrose-VFA mixture. Both the biological as well as the physical properties of the cultivated sludge were affected by the fraction of nonacidified substrate. The sludge in the first compartment of the reactor treating the sucrose-VFA mixture was whitish and fluffy, most likely resulting from the development of acidifying bacteria. Sludge granules which developed in the top part of this reactor possessed the highest acetogenic and methanogenic activity and the highest granule strength as well. The experiments also revealed that the conversion of the sucrose-VFA mixture into methane gradually deteriorated at prolonged operation at high organic loading rates (50 to 100 g COD · L-1 · day-1). Stable long-term performance of a reactor can only be achieved by preserving the sludge segregation along the height of the reactor. In the reactor fed solely with the VFA mixture little formation of granular sludge occurred. In this reactor, large differences in sludge characteristics were also observed along the reactor height. Li+-tracer experiments indicated that the hydraulic regime in the USSB reactor is best characterized by a series of at least five completely mixed reactors. The formation of granular sludge was found to influence the liquid flow pattern. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 151-168 
    ISSN: 0006-3592
    Keywords: avidin ; liposomes ; aggregation kinetics ; biotin ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The aggregation of biotin-modified phospholipid vesicles (liposomes) induced by binding the protein avidin in solution is analyzed experimentally and theoretically. Avidin has four binding sites that can recognize biotin specifically, and is able to cross-link the liposomes to form large aggregates. The aggregation kinetics were followed using quasi-elastic light scattering (QLS) to measure the mean particle size, and by measuring the solution turbidity. The rate and extent of aggregation were determined as a function of vesicle concentration, protein concentration, and the biotin density on the surface of the liposomes. A model based on Smoluchowski kinetics, fractal concepts, and Rayleigh and Mie light scattering theory was developed to analyze the experimental observations. Small aggregates (〈7800 Å diameter) may be treated as globular; however, the fractal nature of larger particles must be taken into account. Parameters in the model are taken from molecular simulations, or fit to the experimental observations. The aggregation kinetics are primarily determined by the biotin density on the liposome surface, the stoichiometric ratio of avidin molecules to liposomes, and the liposome concentration. Good agreement is found between the model and the experimental results. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 51 (1996), S. 713-719 
    ISSN: 0006-3592
    Keywords: biofilm detachment ; fluidized bed biological reactor ; dimensional analysis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Dimensional analysis was applied for the description of biofilm detachment in liquid fluidized bed biological reactors. This technique allowed the identification of the significant parameters influencing detachment mechanisms and suggested suitable experiments for the characterization of involved phenomena. The influence of the significant variables was established on a lab-scale reactor and an empirical model was proposed to correlate experimental results. The detachment rate was strongly dependent on liquid velocity, while the influence of other parameters, such as solid hold-up and liquid shear stress, was found to be less important.
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    Biotechnology and Bioengineering 51 (1996) 
    ISSN: 0006-3592
    Keywords: Chemistry ; Biochemistry and Biotechnology
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  • 77
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    Biotechnology and Bioengineering 51 (1996), S. 725-729 
    ISSN: 0006-3592
    Keywords: bioreactor control ; fed batch ; high antibody ; high density ; medium design ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A simple feeding strategy was developed and successfully employed for nutritional control in a 2-L fed-batch culture of hybridoma cells. A previously developed stoichiometric model for animal cell growth was used to design a supplemental medium for feeding. Undialyzed fetal bovine serum and trace metals (Fe2+, SeO32-, Li+, Zn2+, and Cu2+) were fed to the cells periodically in addition to the automatic feeding of other nutrients in the supplemental medium. In this study, the maximum viable cell density was increased from 6.3 × 106 to 1.7 × 107 cells/mL, and the culture span was extended from 340 to 550 hours. The final monoclonal antibody titer achieved was 2400 mg/L. The specific production rates for ammonia and lactate were further reduced from 0.0045 and 0.0048 in our previous fed-batch experiments to 0.0028 and 0.0036 mmol/109 cell h, respectively. Only 3.4% of the total glucose consumption was converted into lactate, compared to 67% in a conventional batch culture.
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    Biotechnology and Bioengineering 50 (1996), S. 465-478 
    ISSN: 0006-3592
    Keywords: hematopoietic stem cells ; quiescence ; self-renewal ; multilineage potential ; single cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We have developed methods for detailed characterization of the proliferation kinetics and lineage potential of single human hematopoietic progenitor cells in an in vitro culture system. Fetal bone marrow CD34hi/lin- cells were cultured at one cell per well in the presence of c-kit ligand (KL), interleukin (IL)-3, IL-6, and leukemia inhibitory factor (LIF) on a murine stroma cell monolayer. Individual wells were scored for growth between 1 and 10 weeks of culture and analyzed by flow cytometry for lineage composition. A wide variation in time (1 to 8 weeks) was observed before initial cell division, even in the presence of cytokines promoting cell division in primitive progenitors. Eleven percent of the plated cells eventually produced a confluent culture well of approximately 20,000 progeny. Confluent wells were harvested and individually analyzed by flow cytometry for cell surface phenotype. Forty-eight percent of confluent wells contained primitive progenitors (CD34+lin-), 16% contained B-lymphoid cells (CD19+ or CD10+), and 100% contained cells committed to the myelo-erythroid lineage (CD33+). CD34+/lin- cells from confluent wells were replated at one cell per well in secondary culture and the analysis repeated. One of 216 original single cells plated produced populations of B-lymphoid cells, myeloid cells, and primitive progenitors (CD34+/lin-) which persisted through two expansion cycles. We estimate that more than 36 million cells can be produced from a single cell under these culture conditions. A very small percentage of the CD34hi/lin- population (about 1%) was responsible for the majority of subsequent cell production. Our estimate of stem cell content in fetal bone marrow, defined by self-renewal as well as both B-lymphoid and myeloid differentiation from one cell, is approximately 1/13,000. This assay system provides direct in vitro measurements of the expected characteristics of hematopoietic stem cells (high proliferation potential, multilineage potential, self-renewal, and quiescence), and is therefore well suited to assessment of stem cell activity within various cell populations. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 50 (1996), S. 479-492 
    ISSN: 0006-3592
    Keywords: stem cell ; bioreactor ; stromal layer ; Graetz number ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Tissue function is comprised of a complex interplay between biological and physicochemical rate processes. The design of bioreactors for tissue engineering must account for these processes simultaneously in order to obtain a bioreactor that provides a uniform environment for tissue growth and development. In the present study we consider the effects of fluid flow and mass transfer on the growth of a tissue in a parallel-plate bioreactor configuration. The parenchymal cells grow on a preformed stromal (feeder) layer that secretes a growth factor that stimulates parenchymal stem cell replication and differentiation. The biological dynamics are described by a unilineage model that describes the replication and differentiation of the tissue stem cell. The physicochemical rates are described by the Navier-Stokes and convective-diffusion equations. The model equations are solved by a finite element method. Two dimensionless groups govern the behavior of the solution. One is the Graetz number (Gz) that describes the relative rates of convection and diffusion, and the other a new dimensionless ratio (designated by P) that describes the interplay of the growth factor production, diffusion, and stimulation. Four geometries (slab, gondola, diamond, and radial shapes) for the parallel-plate bioreactor are analyzed. The uniformity of cell growth is measured by a two-dimensional coefficient of variance. The concentration distribution of the stroma-derived growth factor was computed first based on fluid flow and bioreactor geometry. Then the concomitant cell density distribution was obtained by integrating the calculated growth factor concentration with the parenchymal cell growth and unilineage differentiation process. The spatiotemporal cell growth patterns in four different bioreactor configurations were investigated under a variety of combinations of Gz (10-1, 100, and 101) and P(10-2, 10-1, 100, 101, and 102). The results indicate high cell density and uniformity can be achieved for parameter values of P = 0.01, …, 0.1 and Gz = 0.1, …, 1.0. Among the four geometries investigated the radial-flow-type bioreactor provides the most uniform environment in which parenchymal cells can grow and differentiate ex vivo due to the absence of walls that are parallel to the flow paths creating slow flowing regions. © 1996 John Wiley & Sons, Inc.
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  • 80
    ISSN: 0006-3592
    Keywords: perfusion chamber ; bone marrow stroma ; mononuclear cell cultures ; hematopoietic cultures ; cell retention ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Perfusion and static cultures of peripheral blood (PB) mononuclear cells (MNCs), obtained from patients following stem cell mobilization, were supplemented with interleukin-3 (IL-3), IL-6, granulocyte colony-stimulating factor (G-CSF), and stem cell factor (SCF) and compared with and without a preformed irradiated allogeneic bone marrow stromal layer. Perfusion cultures without a stromal layer effectively retained nonadherent cells through the use of a novel “grooved” perfusion chamber, which was designed with minimal mass transfer barriers in order to achieve a well-defined culture environment. The grooved chamber allowed easy and efficient culture inoculation and cell recovery. Average maximum expansion of CFU-GM (colony-forming unit granulocyte-macrophage) cells was observed on day 10 for all cultures. Perfusion cultures had a maximum CFU-GM expansion of 17- and 19-fold with and without a stromal layer, respectively. In contrast, static cultures had a maximum CFU-GM expansion of 18- and 13-fold with and without a stromal layer, respectively. Average long-term-culture initiating cell (LTC-IC) numbers on day 15 were 34% and 64% of input in stroma-containing and stroma-free perfusion cultures and 12% and 11% of input in stroma-containing and stroma-free static cultures, respectively. Thus, perfusion enhanced CFU-GM expansion and LTC-IC maintenance more for the stroma-free cultures than for stroma-containing cultures. This was surprising because analysis of medium supernatants indicated that the stroma-containing cultures were metabolically more active than the stroma-free cultures. In view of their equivalent, if not superior, performance compared to stroma-containing cultures, stroma-free perfusion cultures may offer significant advantages for potential clinical applications. © 1996 John Wiley & Sons, Inc.
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  • 81
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    Biotechnology and Bioengineering 50 (1996), S. 521-528 
    ISSN: 0006-3592
    Keywords: HIV ; cytotoxic T lymphocytes (CTL) ; serum ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The ex vivo expansion of antigen-specific cytotoxic T lymphocyte (CTL) lines is being developed for immunotherapy of viral infections and cancer and is critically dependent on the precise cell expansion and stimulation conditions. In this article, we investigate medium requirements for the development of HIV-specific CTL in cell lines generated from the peripheral blood of seven asymptomatic HIV-infected individuals. We find that HIV-specific CTL do not readily develop in the serum-free medium AIM V but do develop if the medium is supplemented with 1% plasma or serum. T cell lines with antigen-specific cytolytic activity express more cell-surface CD57 than do cell lines grown in the absence of serum or plasma. Three sources of serum (human autologous, human AB, or fetal calf) are comparable. Human plasma is somewhat less effective than serum from an identical source. © 1996 John Wiley & Sons, Inc.
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  • 82
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    Biotechnology and Bioengineering 50 (1996), S. 548-554 
    ISSN: 0006-3592
    Keywords: fluorescence ; transfection ; liposome ; flow cytometry ; plasmid ; cell cycle ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cationic liposomes are potentially important gene transfer vehicles, capable of conjugating with anionic DNA by condensation. Flow cytometry was used to examine quantitatively the incorporation of DNA-liposome complex into murine capillary lung endothelial cells. The plasmid DNA, a pSV-β-galactosidase vector, was covalently labeled with ethidium monoazide by photoactivation. The cationic liposome consisted of egg phosphatidylcholine (90%), cholesterol (5%), and stearylamine (5%). The number of plasmid molecules contained within each cell as a function of exposure time was estimated from fluorescence intensity. Fluorescently labeled plasmid is detectable after 10 min and increases with continued exposure, but at a decreasing rate, up to 2160 min. After 2160 min each cell, on average, contains approximately 10,000 plasmid molecules. Following transfection, a single cell unimodal population was detected by flow cytometry, suggesting that all cells participate in transfection equally. Furthermore, cell cycle analysis indicates that the entry of DNA-liposome complex is independent of cell cycle. © 1996 John Wiley & Sons, Inc.
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  • 83
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    Biotechnology and Bioengineering 50 (1996), S. 580-586 
    ISSN: 0006-3592
    Keywords: tissue engineering ; N1E-115 neuroblastoma cells ; electrophysiological differentiation ; retinoid cytotoxicity ; teratogenesis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The cytotoxic effects of retinoids on neuroblastoma cells at various times during electrophysiological differentiation were evaluated. We used N1E-115, a clone of the murine neuroblastoma C1300 derived from the neural crest, and three retinoids: vitamin A (retinol), all-trans retinoic acid (tretinoin), and 13-cis-retinoic acid (isotretinoin). Differentiating N1E-115 cells exposed to retinoids at an isotretinoin EC50 of 16 μM exhibited the greatest vulnerability in terms of cell death during a period (8 to 10 days) that was previously found to be the most sensitive for induction of gross malformations in rodents. This finding suggested possible similarities between the in vivo and in vitro retinoid mechanism(s) of action. The greatest period of vulnerability to retinoid cytotoxicity was also found to coincide with the rapid resting membrane potential (Vm) development period, suggesting a linkage between neuronal Vm and/or electrical excitability development and vulnerability to retinoid cytotoxicity. © 1996 John Wiley & Sons, Inc.
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  • 84
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    Biotechnology and Bioengineering 50 (1996), S. 145-150 
    ISSN: 0006-3592
    Keywords: high-pressure homogenization ; cell disruption ; cell size distribution ; simulation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Measurements of size distributions are provided for the breakage of commercial packed bakers' yeast cells as a function of operating pressure and number of passes through a Manton Gaulin high-pressure homogenizer. A two parameter model was developed, based upon the use of a Boltzmann function, to simulate the changes in size distribution that accompany the cell breakage process. The effects of operating pressure and number of passes are incorporated in the model and the result is used to simulate the particle size distribution of the cell homogenate. The results show that there is little breakage below a threshold pressure of 115 bar and above which breakage is critically dependent upon the pressure and number of passes through the homogenizer. The analysis provides a means of studying the efficiency of centrifugation that may follow cell disruption and provides the basis for further studies of size distribution changes accompanying cell disruption. © 1996 John Wiley & Sons, Inc.
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  • 85
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    Keywords: specific secretion rate ; animal cell culture ; hybridoma ; osmotic stress ; variance of specific secretion rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The specific secretion rate (q, μg protein secreted/viable cell-h) and its variance are very useful to compare the capability of cell lines for protein secretion. An assessment of specific secretion rate variability is also beneficial and important when the specific secretion rate is to be used as an on-line process parameter to monitor culture production behavior or for in-process decisionmaking. Experimental errors in mammalian cell culture (e.g., protein concentration measurement and cell counting) and estimation error in the method of calculating q contribute to the total variance of the specific secretion rate. Although the variance of q is essential for comparing the differences between cell lines and the response of the same cell line to different nutrient or environmental conditions, few methods for calculating the variance of the specific secretion rate have been reported. As a model system, we have used the weighted jackknife method and the delta method to calculate the variance in the specific secretion rate of a murine monoclonal antibody (qmAb) determined by a differential method. These methods were applied to calculate qmAb and its standard deviation to determine the change in qmAb kinetics during batch culture of the 9.2.27 hybridoma in response to growth in hyperosmotic media or osmotic stress. Without osmotic stress, during exponential growth in DMEM + 5% FBS spinner culture, the estimate of qmAb decreases at least threefold. Results indicate that the 9.2.27 hybridoma responds to hyperosmotic media (400 mOsm, 470 mOsm) by significantly reducing the degree of qmAb decrease in the exponential phase, thus maintaining a higher qmAb through the stationary phase. The trend of qmAb during the batch cultures studied is further confirmed by t-test. Osmotic stress is statistically shown to be able to alter significantly the hybridoma-specific mAb secretion kinetics during batch culture. Determination of the variance of specific secretion rate using the weighted jackknife method offers a powerful approach for establishing the confidence limits of specific protein secretion rate between cell cultures in different nutritional or osmotic environments. © 1996 John Wiley & Sons, Inc.
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  • 86
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    Biotechnology and Bioengineering 51 (1996), S. 659-672 
    ISSN: 0006-3592
    Keywords: methanotroph ; microbial filter ; attachment/detachment ; trichloroethylene degradation ; Methylosinus trichosporium OB3b ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We are investigating a methanotrophic filter strategy for the in situ bioremediation of low levels of chlorinated aliphatic, volatile organic chemicals (VOCs). It is based on the use of pregrown, resting cells, instead of growth-nutrient stimulations. The economic feasibility of such a filter is dependent on its operational longevity at ground-water temperatures. The latter, in turn, is dependent on several key parameters, such as the bacterial attachment densities reached during the injection of the microbial suspension and the subsequent detachment-removal of cells from the filter over time. Scaled attachment/detachment experiments were carried out using a representative quartzitic sand in glass 1-cm × 10-cm columns to simulate a filter. A rosette-dominated form of Methylosinus trichosporium OB3b was isolated and used in these and the subsequent catalytic longevity experiments. Its initial attachment, employing Higgins' medium phosphate buffer, pH 7.0 (HPB), was 7.0 to 8.0 × 108 bacteria/g of dry sand. This was elevated to ∼1.5 × 109 cells/g by including 1.0 mM MgCl2, 100 μM FeSO4, and 0.025% agar in the cell-suspension loading buffer. These loading additives also increased the time required to reach 50% cell detachment with HPB alone from 5 days to ∼45 days. The functional longevity of a column biofilter, formed with resting-state rosette-enriched cells in the presence of the aforementioned additives, was determined at 21°C by challenging it with weekly 12 h, ∼250 ppb pulses of trichloroethylene (TCE). The column results indicate that for our attached-cell filter to biodegrade TCE levels of several hundred ppb sufficiently, to 〈5 ppb, it will likely need replenishment at ∼8 week intervals, due to the instability of the endogenous whole-cell soluble methane monooxygenase specific activity beyond that time period. This study represents the first time that anyone has shown that a rosette-enriched substrain can be isolated from a well-known methanotrophic strain and then stably cultured and utilized advantageously for a specific application - namely its improved attachment-slowed detachment characteristics in a microbial filter.
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  • 87
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    Biotechnology and Bioengineering 51 (1996), S. 697-702 
    ISSN: 0006-3592
    Keywords: E. coli ; alginate immobilization ; oxygen transport ; mass transfer ; acetate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of reduced oxygen supply on the production of a recombinant protein (plasmid-encoded β-galactosidase) was investigated in Escherichia coli. A novel modified bubble tank reactor was used to provide a direct comparison between immobilized and suspended cells in identical environments except for the immobilization matrix. Decreased oxygen supply led to increased β-galactosidase synthesis by both immobilized and suspended cells. Immobilized cells produced similar amounts of β-galactosidase as the suspended cells. Lactose consumption and acetate production, on a per cell basis, were significantly higher in immobilized cells, suggesting that immobilized cells utilized fermentative metabolism. However, a transport analysis of the immobilized cell system showed that immobilized cells were not subject to either external or internal mass transfer gradients.
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  • 88
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    Biotechnology and Bioengineering 51 (1996), S. 703-712 
    ISSN: 0006-3592
    Keywords: Saccharomyces cerevisiae ; Ty3 retrotransposon ; cloned gene integration ; stability ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The Ty3 retrotransposon of Saccharomyces cerevisiae was employed for the site-specific integration of heterologous genes into the yeast genome. A GAL-regulated promoter allowed induction of the retrotransposition process, and a bacterial neor gene inserted in the Ty3 element was used as a selectable model heterologous gene. The frequency of transposition of this neor-marked element was found to be comparable to that of an unmarked element. Three amplification systems were constructed; the systems varied with respect to the location and number of the GAL-regulated helper and neor-marked Ty3 elements. For all three systems, neor integrations were readily selected with a maximum of two insertions obtained per round of amplification. A sequential amplification strategy was effective for further increasing the number of integrated cloned genes, and families of strains varying by only one neor insertion were easily obtained. Resistance to the antibiotic G418 correlated well with the number of integrated neor genes, and Northern blots verified the relationship between cloned gene number (up to four) and neor expression. Structural stability of the integrated genes was also demonstrated. By controlling the number of rounds of amplification and the level of G418 selection, precise numbers of integrated heterologous genes could be obtained. Because the amplification process can be repeated using different cloned genes inserted in the Ty3 element, these results demonstrate the potential of retrotransposition for the regulated integration of a series of different genes at nondeleterious chromosomal locations.
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  • 89
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    Biotechnology and Bioengineering 51 (1996), S. 720-724 
    ISSN: 0006-3592
    Keywords: hybrid protein ; dielectric permeability ; electroconductivity ; electro-optical properties ; Escherichia coli ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel method for monitoring the cell culture process has been developed. The method is based on the measurements of electro-optical characteristics of cell suspension, calculation of cell structure parameters, and the relationship between accumulation of proteins and change of these parameters' employment. Application of the method for the monitoring of a culture process of a recombinant strain is considered. The process of growth of recombinant strains cannot be sufficiently predicted and the direct measurement of cell culture parameters is unlikely to be the most efficient way of solving the problem.Escherichia coli plasmid-free and recombinant strains synthesizing the fusion protein consisting of tumor necrosis factor-α (TNF) and thymosin-α1 (T) were studied. It was found that cytoplasmic electroconductivity of the strains investigated increased during the culture process. The accumulation of insoluble recombinant pThy-315-encoded hybrid protein TNF(SINGLEBOND)T in cells resulted in a decrease of the membrane dielectric permeability. To determine variations of membrane dielectric permeability the amount of insoluble recombinant protein TNF(SINGLEBOND)T in the bacterial cells should be calculated.
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  • 90
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    Biotechnology and Bioengineering 51 (1996), S. 673-678 
    ISSN: 0006-3592
    Keywords: image analysis ; Saccharomyces cerevisiae floc ; floc counting ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A standardized image analysis method has been developed permitting determination of the number of yeast flocs and their size distribution. The method includes image grabbing, image enhancement, automatic determination of the appropriate threshold, curve fitting of the areahistogram, determination of the mean single floc area and its standard deviation, and floc counting. The extension of the method to other applications is immediate and straightforward. Two Saccharomyces cerevisiae floc Populations (with ages of 48 and 72 h) were analyzed. The results showed a variation around the mean of 9%-12% for the single floc mean area, 6%-7% for the number of single flocs, and 5%-6% for the total number of flocs. Aggregates of two flocs (doublets) and three flocs (triplets) were enumerated. The correctness of the method was checked by analyzing the parameters of interest as a function of the threshold. The constant correlation between the parameters and the threshold showed the validity and consistency of the method. © 1996 John Wiley & Sons, Inc.
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  • 91
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    Biotechnology and Bioengineering 52 (1996), S. 15-23 
    ISSN: 0006-3592
    Keywords: tissue engineering ; gene therapy ; artificial skin ; wound-healing growth factors ; growth factor delivery ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Skin substitutes, containing cultured keratinocytes of the epidermis (autologous or allogeneic cells), have been used in the treatment of severe burns and other defects of the skin such as chronic ulcers. Our goal is to enhance the functions of the cells used in these skin substitutes by genetic modification. We propose to develop a genetically modified skin graft which would function as a cell-based vehicle for the local synthesis and delivery of wound-healing growth factors. Using retroviral-mediated gene transfer, we have introduced stable copies of the genes encoding platelet-derived growth factor (PDGF-A) or insulin-like growth factor-1 (IGF-1) into cultured human diploid keratinocytes. After stable integration of these genes, the cells secreted significant levels of these growth factors, 744 ng and 502 ng/107 cells/24 h for PDGF-A and IGF-1, respectively. The modified cells were grown to confluence, detached as a multicell-layered epithelial sheet, and transplanted to athymic mice.Seven days after transplantation, grafts secreting PDGF-A or IGF-1 differentiated into a stratified epithelium comparable to unmodified cells. Most importantly, the newly synthesized connective tissue layer subjacent to the PDGF-A-modified grafts was significantly thicker and showed an increase in cellularity, vascularity, type I collagen, and fibronectin deposition when compared to control grafts of unmodified cells or grafts expressing IGF-1.These results demonstrated that the function of the cells of a skin substitute can be enhanced by genetic modification and show that PDGF-A secretion from these cells can mediate changes to the cellular, vascular, and extracellular matrix composition of the adjacent dermal tissue. Moreover, these results suggest that a cell-based method for growth factor synthesis and delivery may be a useful approach to promoting tissue repair. © 1996 John Wiley & Sons, Inc.
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  • 92
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    Biotechnology and Bioengineering 52 (1996), S. 24-33 
    ISSN: 0006-3592
    Keywords: unilineage model ; tissue function ex vivo ; hematopoiesis ; stem cell expansion ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Stem cell models are used to describe the function of several tissues. We present unilineage kinetic description of stem cell models and their application to the analysis of ex vivo hematopoietic cell expansion data. This model has the capability to simulate the total cell number and the number of cells at each stage of differentiation over time as a function of the stem cell self-renewal probability, the growth rate of each subpopulation, and the mature cell death rate. The model predicts experimental observations in perfusion-based hematopoietic bioreactor systems. To obtain net cell expansion ex vivo, the model simulations show that the stem cell self-renewal probability must exceed one-half, thus resulting in net expansion of the stem cell population. Experimental data on long-term culture-initiating cells (LTC-IC) confirm this prediction and the probability of self-renewal is estimated to be 0.62 to 0.73. This self-renewal probability, along with the death rate, define a relationship in which the apparent overall growth rate is less than the compartmental growth rate. Finally, the model predicts that cells beyond the stem cell stage of differentiation must self-renew to achieve the level of expansion within the time frame observed in experimental systems. © 1996 John Wiley & Sons, Inc.
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  • 93
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    Biotechnology and Bioengineering 52 (1996), S. 34-44 
    ISSN: 0006-3592
    Keywords: hepatocyte spheroid ; porcine hepatocyte ; hollow fiber ; bioartificial liver ; collagen ; bioreactor ; ureagenesis ; albumin synthesis ; glucuronidation ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A xenogeneic hollow fiber bioreactor utilizing collagen-entrapped dispersed hepatocytes has been developed as an extracorporeal bioartificial liver (BAL) for potential treatment of acute human fulminant hepatitis. Prolonged viability, enhanced liver-specific functions, and differentiated state have been observed in primary porcine hepatocytes cultivated as spheroids compared to dispersed hepatocytes plated on a monolayer. Entrapment of spheroids into the BAL can potentially improve performance over the existing device. Therefore, studies were conducted to evaluate the feasibility of utilizing spheroids as the functionally active component of our hybrid device. Confocal microscopy indicated high viability of spheroids entrapped into cylindrical collagen gel. Entrapment of spheroids alone into collagen gel showed reduced ability to contract collagen gel. By mixing spheroids with dispersed cells, the extent of collagen gel contraction was increased. Hepatocyte spheroids collagen-entrapped into BAL devices were maintained for over 9 days. Assessment of albumin synthesis and ureagenesis within a spheroid-entrapment BAL indicated higher or at least as high activity on a per-cell basis compared to a dispersed hepatocyte-entrapment BAL device. Clearance of 4-methylumbelliferone to its glucuronide was detected throughout the culture period as a marker of phase II conjugation activity. A spheroid-entrapment bioartificial liver warrants further studies for potential human therapy. © 1996 John Wiley & Sons, Inc.
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  • 94
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    Biotechnology and Bioengineering 52 (1996), S. 45-60 
    ISSN: 0006-3592
    Keywords: In vitro toxicology ; physiologically based pharmacokinetic models ; cell culture analog ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The overall goal of this project is the development of a new methodology for translating advances in molecular level understanding of toxicological responses into a predictive tool for dose response in whole animals and humans exposed to single compounds or mixtures of compounds. The methodology incorporates a mechanistic cellular level model into a PBPK (physiologically based pharmacokinetic) model which simultaneously guides the development of an in vitro cell culture analog (CCA) to the PBPK. Where the PBPK specifies an organ, (e.g., liver) the in vitro or CCA system contains a compartment with the appropriate cell or cell population (e.g., hepatocytes for the liver). The CCA has significant advantages over other in vitro systems and PBPK systems used independently for evaluating metabolic responses to drugs or potentially toxic chemicals where the exchange of metabolites between organs is likely to be important. The CCA system is superior to a PBPK because an a priori description of complete metabolism is not required and secondary, unexpected interactions can be detected. The CCA system, unlike other in vitro systems, gives a dynamic response that realistically simulates in vivo interactions between organs. Furthermore, the CCA allows dosing on the same basis as animal tests (e.g., milligrams per kilogram of body mass equivalent). Because the construction of a CCA is guided by a PBPK, this approach allows extrapolation to low doses and across species, including extrapolation to humans. We have constructed a prototype system and have conducted proof-of-concept experiments using naphthalene as a test chemical. These experiments clearly demonstrate the ability to generate a reactive metabolite in one compartment and detect its effects (on LDH release and glutathione depletion) in a second compartment. However, this prototype device would be expensive to replicate and requires nearly constant supervision from a trained investigator. For this concept to replace animals an inexpensive, self-regulating device is needed. An initial design to accomplish this goal is described as well as the corresponding model using naphthalene as a test compound. © 1996 John Wiley & Sons, Inc.
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    Biotechnology and Bioengineering 52 (1996), S. 61-80 
    ISSN: 0006-3592
    Keywords: growth factors ; receptors ; trafficking ; mammalian cells ; cell engineering ; cytokine ligands ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Peptide growth factors and other receptor-binding cytokine ligands are of interest in contemporary molecular health care approaches in applications such as wound healing, tissue regeneration, and gene therapy. Development of effective technologies based on operation of these regulatory molecules requires an ability to deliver the ligands to target cells in a reliable and well-characterizable manner. Quantitative information concerning the fate of peptide ligands within tissues is necessary for adequate interpretation of experimental observations at the tissue level and for truly rational engineering design of ligand-based therapies. To address this need, we are undertaking efforts to elucidate effects of key molecular and cellular parameters on temporal and spatial distribution of cytokines in cell population and cell/matrix systems. In this article we summarize some of our recent findings on dynamics of growth factor depletion by cellular endocytic trafficking, growth factor transport through cellular matrices, and growth factor production and release by autocrine cell systems. © 1996 John Wiley & Sons, Inc.
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  • 96
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    Biotechnology and Bioengineering 52 (1996), S. 81-88 
    ISSN: 0006-3592
    Keywords: platelet adhesion ; polyurethane ; thrombosis ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The surface and blood compatibility characteristics of Pellethane polyurethane blended with 1% or 5% (w/w) polytetramethylene oxide (PTMO) were evaluated. Analysis by X-ray photoelectron spectroscopy indicated that blending of PTMO caused an increased amount of amide wax, a processing agent present in Pellethane, to be expressed on the surface of the blended films in vacuo. Dynamic contact angle measurements in water, however, showed that PTMO was preferentially expressed on the blend film surfaces in water. The two lower molecular weight species, PTMO and amide wax, were thus capable of reorienting, depending on the environmental conditions. An in vitro assay of platelet adherence and thrombosis showed that polyurethane blended with 5% PTMO had about two-thirds fewer adherent platelets compared to unblended polyurethane and that a blend containing 1% PTMO was intermediate in platelet adherence. Measurements of albumin adsorption from binary solution with fibrinogen indicated that PTMO blends did not preferentially adsorb albumin compared to unblended polyurethane. © 1996 John Wiley & Sons, Inc.
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  • 97
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    Biotechnology and Bioengineering 52 (1996), S. 89-95 
    ISSN: 0006-3592
    Keywords: poly(organo phosphazenes) ; nanoparticles ; poly(ethylene oxide) ; biodegradable materials ; surface modification ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The use of biodegradable derivatives of poly(organo phosphazenes) for the preparation of nanoparticles and their surface modification with the novel poly(ethylene oxide) derivative of poly(organo phosphazene) has been assessed using a range of in vitro characterization methods. The nanoparticles were produced by the precipitation solvent evaporation method from the derivative co-substituted with phenylalanine and glycine ethyl ester side groups. A reduction in particle size to less than 200 nm was achieved by an increase in pH of the preparation medium. The formation (and colloidal stability) of these nanoparticles seems to be controlled by two opposite effects: attractive hydrophobic interactions between phenylalanine ester groups and electrostatic repulsions arising from the carboxyl groups formed due to (partial) hydrolysis of the ester bond(s) at the high pH of the preparation medium. The poly[(glycine ethyl ester)phosphazene] derivative containing 5000-Da poly(ethylene oxide) as 5% of the side groups was used for the surface modification of nanoparticles. Adsorbed onto the particles, the polymer produced a thick coating layer of approximately 35 nm. The coated nanoparticles exhibited reduced surface negative potential and improved colloidal stability toward electrolyte-induced flocculation, relative to the uncoated system. However, the steric stabilization provided was less effective than that of a Poloxamine 908 coating. This difference in effectiveness of the steric stabilization might indicate that, although both the stabilizing polymers possess a 5000-Da poly(ethylene oxide) moiety, there is a difference in the arrangements of these poly(ethylene oxide) chains at the particle surface. © 1996 John Wiley & Sons, Inc.
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  • 98
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    Biotechnology and Bioengineering 52 (1996), S. 102-108 
    ISSN: 0006-3592
    Keywords: polyphosphazenes ; biodegradation ; drug delivery ; mitomycin C ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article describes the synthesis of biodegradable polyphosphazenes. The rate of degradation can be varied in a controllable manner by the introduction of hydrolysis-sensitive amino acid ester side groups or by blending of polymers. Biodegradable polyphosphazenes can be used for the preparation of drug-containing implants and this is illustrated for devices containing the cytostatic agent mitomycin C. This article reviews data about the degradation characteristics of poly[(amino acid ester)phosphazene] derivatives that have been discussed previously. Some new data about MMC-containing poly[(organo)phosphazene] devices are discussed as well. © 1996 John Wiley & Sons, Inc.
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    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 52 (1996), S. 96-101 
    ISSN: 0006-3592
    Keywords: oral drug delivery ; polyanhydrides ; dicumarol ; polymer ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The current study focuses on the development of bioadhesive oral delivery systems based on bioerodible polyanhydrides. The polymers were studied and characterized using a novel tensiometer based on a very sensitive electrobalance. The system was designed to mimic in vivo interactions, thus all experiments were conducted with freshly excised tissue immersed in physiological saline at 37°C. Poly(fumaric-co-sebacic) [P(FA:SA)] was found to be the most bioadhesive polymer from a series of different thermoplastic materials evaluated. Correlation with in vivo performance was investigated by determining gastrointestinal (GI) residence time of barium-loaded microspheres. Residence times of 24 to 36 h provided a strong indication that these microspheres were good candidates for bioadhesive drug delivery systems. To evaluate the effect of these materials on bioavailability, the anticoagulant drug, dicumarol, was encapsulated. Systemic blood levels demonstrated increased bioavailability for the encapsulated dicumarol formulation as compared with unencapsulated drug. © 1996 John Wiley & Sons, Inc.
    Additional Material: 4 Ill.
    Type of Medium: Electronic Resource
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    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 52 (1996), S. 109-121 
    ISSN: 0006-3592
    Keywords: inverse metabolic engineering ; hemoglobin ; cell cycle ; CHO cell culture ; culture fluorescence ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The classical method of metabolic engineering, identifying a rate-determining step in a pathway and alleviating the bottleneck by enzyme overexpression, has motivated much research but has enjoyed only limited practical success. Intervention of other limiting steps, of counterbalancing regulation, and of unknown coupled pathways often confounds this direct approach. Here the concept of inverse metabolic engineering is codified and its application is illustrated with several examples. Inverse metabolic engineering means the elucidation of a metabolic engineering strategy by: first, identifying, constructing, or calculating a desired phenotype; second, determining the genetic or the particular environmental factors conferring that phenotype; and third, endowing that phenotype on another strain or organism by directed genetic or environmental manipulation. This paradigm has been successfully applied in several contexts, including elimination of growth factor requirements in mammalian cell culture and increasing the energetic efficiency of microaerobic bacterial respiration. © 1996 John Wiley & Sons, Inc.
    Additional Material: 11 Ill.
    Type of Medium: Electronic Resource
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