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  • 1
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Analytical chemistry 67 (1995), S. 2957-2965 
    ISSN: 1520-6882
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Analytical chemistry 66 (1994), S. 4034-4042 
    ISSN: 1520-6882
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology
    Type of Medium: Electronic Resource
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  • 3
    Electronic Resource
    Electronic Resource
    s.l. : American Chemical Society
    Analytical chemistry 61 (1989), S. 1602-1612 
    ISSN: 1520-6882
    Source: ACS Legacy Archives
    Topics: Chemistry and Pharmacology
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  • 4
    ISSN: 0006-3592
    Keywords: isoelectric membranes ; immobilized reactors ; urease ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A novel type of immobilized enzyme reactor operating under an electric field is here reported: a multicompartment immobilized enzyme reactor (MIER). In this experimental set-up, the enzyme and zwitterionic buffering ions are trapped in between two isoelectric membranes, having isoelectric point (pl) values so far apart as to trap the enzyme by an isoelectric mechanism, while allowing operation at pH optima, even when the latter pH value is quite removed from the enzyme pl. As an example, urease (pl 4.9) is trapped between a pl 4.0 and a pl 8.0 membranes, thus permitting operation (via suitable amphoteric ions buffering at pH 7.5) at the pH of optimum of activity (pH 7.5). The charged product (ammonium ions) quickly leaves the enzyme chamber under the influence of the electric field, thus allowing sustained activity for much longer time periods than in conventional reactors. As an example, while in a batch reactor 90% of original enzyme activity is lost in 200 min, only 2% activity is lost in the same period in the MIER reactor. As an additional bonus, the MIER reactor allows conversion rates of ∼95% in a wide range of substrate concentrations, whereas batch-type reactors rarely achieve better than 50% conversion under comparable experimental conditions. © 1997 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 60 (1998), S. 454-461 
    ISSN: 0006-3592
    Keywords: isoelectric membranes ; immobilized reactors ; penicillin G acylase ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Penicillin G acylase (PGA) is exploited for producing pure D-phenylglycine from a racemate mixture, via an acylation reaction onto a cosubstrate, the ester methyl-4-hydroxyphenyl acetate. The reaction, when carried in a batch, is severely hampered by the reverse process, by which the product, 4-hydroxyphenylacetyl-(L)phenyl glycine, upon consumption of L-phenylglycine, is converted by the enzyme back into free substrate and 4-hydroxyphenyl acetic acid via lysis of the amido bond. To prevent this noxious reaction, a multicompartment electrolyzer with isoelectric membranes (MIER) is used as enzyme reactor, operating in an electric field. PGA is trapped between pI 5.5 and pI 10.5 membranes, together with an amphoteric, isoelectric buffer (lysine). As the 4-hydroxyphenylacetyl-(L)phenyl glycine product is formed, it vacates the reaction chamber by electrophoretic transport and is collected close to the anode, in a chamber delimited by pI 2.5 and 4.0 membranes. The same fate occurs to the free acid 4-hydroxyphenyl acetic acid, formed upon spontaneous (and enzyme-driven) hydrolysis of the methyl ester in the reaction chamber. These combined processes leave behind, in the enzyme reaction chamber, the desired product, pure D-phenylglycine. The advantages of the MIER reactor over batch operations: the consumption of the L-form in the racemate is driven to completion and the enzyme is kept in a highly stable form, maintaining 100% activity after one day of operation, during which time the PGA enzyme, in the batch reactor, has already lost 〉75% catalytic activity. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 454-461, 1998.
    Additional Material: 8 Ill.
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  • 6
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Electrophoresis 2 (1981), S. 220-228 
    ISSN: 0173-0835
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Chemistry and Pharmacology
    Notes: The temperature at which polyacrylamide gels are polymerized strongly affects the structure and physical properties of this matrix. The suggested temperature of 0-4 °C has been found to produce highly turbid, highly porous and unelastic gels. At temperature of 25 °C of higher, the gels became progressively transparent, less porous and more elastic. This phenomenon is strongly pronounced in N,N′-methylenebisacrylamide (Bis) gels and progressively decreases for N,N′-(1,2-dihydroxyethylene)bisacrylamide (DHEBA) and N,N′-bisacrylylcystamine (BAC) gels. It has been attributed to the formation of hydrogen bonds among cross-linker molecules, which are presumably stabilized by low temperature and progressively broken at higher temperatures. The most extensively H-bonded compounds seem to be Bis molecules, since they can form four H-bonds/molecule, followed by DHEBA (in which inter-molecular H-bonds have to compete with intra-molecular H-bonds) and finally by BAC, which is sparingly H-bonded at 2 °C, and fully uncomplexed at 30°C. It is suggested that polymerization at 0-4°C should be abandoned, since it leads to unhomogeneous and unreproducible pore size matrices. Since H-bonds in Bis molecules are fully disrupted only at 60°C (a temperature unsuitable for gel polymerization, since it produces short chains and unelastic matrices), it is also suggested that the use of Bis should be discontinued in favour of better cross-links, such as DHEBA. In all cases, best polymerization conditions are obtained at 25-30°C. For all three cross-linkers, homogeneous gels are obtained in presence of 8 M urea or in pure formamide as solvent, since both agents fully disrupt H-bonds.
    Additional Material: 11 Ill.
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  • 7
    ISSN: 0173-0835
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Chemistry and Pharmacology
    Notes: Urine analysis by two-dimensional gel electrophoresis with isoelectric focusing in immobilized pH gradients in the first dimension allows the loading of high sample volumes and/or of large amounts of salts. When applied to urinary protein analysis, it makes it possible to apply up to 1 mL of dialyzed, unconcentrated sample or up to 350 μL of unprocessed urine.
    Additional Material: 2 Ill.
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  • 8
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Electrophoresis 8 (1987), S. 538-540 
    ISSN: 0173-0835
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Chemistry and Pharmacology
    Notes: By taking advantage of the insensitivity of immobilized pH gradients to high protein and salt loads, microheterogeneity and polymorphism of α1-acid glycoprotein could be demonstrated on whole serum by conventional Coomassie Brilliant Blue G-250 staining. Different running conditions were compared for optimal resolution.
    Additional Material: 2 Ill.
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  • 9
    Electronic Resource
    Electronic Resource
    Weinheim : Wiley-Blackwell
    Electrophoresis 6 (1985), S. 53-56 
    ISSN: 0173-0835
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Chemistry and Pharmacology
    Notes: Examples of increased resolution obtained with non-linear pH gradients are presented. Discussed in detail is the “ideal” pH course in the range 4-10, based on the statistical distribution of isoelectric points of protein from data in the literature.
    Additional Material: 3 Ill.
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  • 10
    ISSN: 0173-0835
    Keywords: Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Chemistry and Pharmacology
    Notes: The separation of enantiomeric forms of dansylated amino acids by isoelectric focusing in immobilized pH gradients (IPG) is demonstrated for the first time. Separations occur in a pH 3.0-4.0 IPG interval, in presence of 7murea, 10% methanol and 60 mM β-cyclodextrin (CD) as chiral discriminator. It is found that the inclusion complex formed between the D-form and CD has a lower pI than the uncomplexed form (ΔpI = 0.05 for DL-Phe and ΔpI = 0.025 for DL-Trp); from this, it is calculated that the pK of the tertiary amino group in the dansyl moiety is lowered by 0.1 pH unit in the former case (D-Phe) and by 0.05 in the case of D-Trp (both values referring to 60 mM CD gels). For some racemates (e.g., DL-Phe) the separation mechanism is still operative with CD concentrations as low as 20 mM. In our system 60 mM CD appears to be the solubility limit of CD. As the complex is stable in the electric field for at least 15 h, this separation mechanism could be exploited for purifying large quantities of pure D and L forms racemates in multicompartment electrolyzers with isoelectric Immobiline membranes.
    Additional Material: 3 Ill.
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