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  • 1
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 50 (1996), S. 319-328 
    ISSN: 0006-3592
    Keywords: membrane fouling ; microfiltration ; sterile filtration ; quasi-elastic light scattering ; protein aggregation/adsorption ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The most troublesome problem encountered during the sterile filtration of protein solutions is membrane fouling. This article presents our study on sterile filtration of a model protein, recombinant human growth hormone (rhGH). Scanning electron microscopy (SEM) analysis shows that 0.22-μm membranes, when used to filter the mannitol-formulated protein solution under a 0.35-bar transmembrane pressure, were plugged to a great extent. When zinc ions were added to induce aggregates, the fouling tendency of rhGH solutions increased with increasing amount and size of the aggregates, indicating that the aggregates present before filtration might be responsible for membrane fouling. However, repeated filtration of the same solution using a fresh filter each time cannot reduce membrane fouling, and all filtrates contain the same trace amount of hGH particulates as the prefiltered solution. Particulate size was determined to be between 0.03 and 0.15 μm by dynamic light scattering. Also, in view of the fact that protein formulations significantly affected the tendency of fouling with the same preexisting aggregates, it is likely that fouling was more attributed to the aggregation taking place in the filter pores during filtration (secondary aggregation) than to the aggregates present before filtration. Adding a surfactant to or increasing the pH of the protein solution improves the filtration, whereas increasing ionic strength slows down the filtration. This result suggests that the balance of the protein's interaction and electrostatic repulsion plays an important role in the protein's fouling tendency. Many factors might change the microenvironment in the pores and disturb this balance. Those considerations and the aggregation tendency of rhGH in the filter pores will be discussed in detail separately. © 1996 John Wiley & Sons, Inc.
    Additional Material: 10 Ill.
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  • 2
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 54 (1997), S. 503-512 
    ISSN: 0006-3592
    Keywords: aggregation by air-liquid interface ; foaming ; rhDNase ; rhGH ; shear ; shear rate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of shear alone on the aggregation of recombinant human growth hormone (rhGH) and recombinant human deoxyribonuclease (rhDNase) has been found to be insignificant. This study focused on the synergetic effect of shear and gas-liquid interface on these two model proteins. Two shearing systems, the concentric-cylinder shear device (CCSD) and the rotor/stator homogenizer, were used to generate high shear (〉 106) in aqueous solutions in the presence of air. High shear in the presence of an air-liquid interface had no major effect on rhDNase but caused rhGH to form noncovalent aggregates. rhGH aggregation was induced by the air-liquid interface and was found to increase with increasing protein concentration and the air-liquid interfacial area. The aggregation was irreversible and exhibited a first-order kinetics with respect to the protein concentration and air-liquid interfacial area. Shear and shear rate enhanced the interaction because of its continuous generation of new air-liquid interfaces. In the presence of a surfactant, aggregation could be delayed or prevented depending upon the type and the concentration of the surfactant. The effect of air-liquid interface on proteins at low shear was examined using a nitrogen bubbling method. We found that foaming is very detrimental to rhGH even though the shear involved is low. The use of anti-foaming materials could prevent rhGH aggregation during bubbling. The superior stability exhibited by rhDNase may be linked to the higher surface tension and lower foaming tendency of its aqueous solution. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 503-512, 1997.
    Additional Material: 8 Ill.
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  • 3
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 60 (1998), S. 301-309 
    ISSN: 0006-3592
    Keywords: cyclone design and configuration ; receiving vessel ; spray drying ; system design ; production yield ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The objective of this work was to improve a bench-top spray dryer's efficiency in both production recovery and throughput for preparing protein aerosol powders. A Büchi mini-spray dryer was used to prepare the powders of recombinant humanized anti-IgE antibody. The resulting powder's physical properties such as particle size, residual moisture, and morphology, along with its recovery and production rate was the basis of this development work. Mass balance suggests that approximately 10-20% of powder was lost in the exhaust air, consisting primarily of particles less than 2 μm. Also, significant loss (20-30%) occurred in the cyclone. Attempts were made to improve product recovery in the receiving vessel using dual-cyclone configurations, different cyclone designs, cyclones with anti-static treatment, and different receiver designs. System modifications such as replacing the original bag-filter unit with a vacuum system effectively reduced drying air flow resistance, allowing the protein to be dried at a lower inlet air temperature and the production scale to be increased. We concluded that the modified spray-drying system is advantageous over the original bench-top spray dryer. This improvement will be beneficial to early-stage research and development involving high-valued protein powders. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 301-309, 1998.
    Additional Material: 8 Ill.
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  • 4
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    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.
    Additional Material: 9 Ill.
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  • 5
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 53 (1997), S. 560-566 
    ISSN: 0006-3592
    Keywords: aggregation ; Ca2+ ; fluid-bed ; microcalorimetry ; rhDNase ; spray coating ; Würster process ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: This article documents a feasibility study on coating fine powders with protein solutions using a Würster spray coater (GPCG-1 from Glatt Air Techniques, Ramsey, NJ). Spray coating was based on a fluid-bed process where fluidized microcarriers were coated inside the Würster column and dried in the fluidization chamber. Recombinant human deoxyribonuclease (rhDNase) was used as the model protein. Lactose powders of two different size ranges, 53-125 and 125-250 μm, were used as the model microcarrier. The amount of protein applied was varied to obtain coatings of varying thickness. The extent of rhDNase loading determined experimentally was found to be consistent with the theoretical value and was also confirmed visually by scanning electron microscopy. The coating showed a strong integrity after being subjected to mechanical force. However, the protein suffered serious aggregation during coating, most likely due to the thermal stress of the process. Aggregation was significantly reduced when rhDNase was formulated with calcium ions, consistent with the observation that Ca2+ thermally stabilized the protein (as determined by scanning microcalorimetry) in aqueous solution. Thus, our study demonstrates that spray coating, particularly when used in conjunction with rational stabilization strategies, is a feasible alternative to other methods of preparing dried pharmaceutical proteins. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 560-566, 1997.
    Additional Material: 6 Ill.
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