Cyclodextrin production by cyclodextrin glycosyltransferase from Bacillus circulans DF 9R

Cyclodextrins (CD) are cyclic oligosaccharides with multiple applications in the food, pharmaceutical, cosmetic, agricultural and chemical industries. In this work, the conditions used to produce CD with cyclodextrin glycosyltransferase from Bacillus circulans DF 9R were optimized using experimental designs. The developed method allowed the partial purification and concentration of the enzyme from the cultural broth and, subsequently, the CD production, using the same cassava starch as enzyme adsorbent and as substrate. Heat-treatment of raw starch at 70 degrees C for 15 min in the presence of adsorbed cyclodextrin glycosyltransferase allowed the starch liquefaction without enzyme inactivation. The optimum conditions for CD production were: 5% (w/v) cassava starch, 15 U of enzyme per gram of substrate, reaction temperature of 56 degrees C and pH 6.4. After 4h, the proportion of starch converted to CD reached 66% (w/w) and the weight ratio of alpha-CD:beta-CD:gamma-CD was 1.00:0.70:0.16.     

Intermolecular transglycosylating reaction of cyclodextrin glucanotransferase immobilized on capillary membrane

The intermolecular transglycosylating reaction of cyclodextrin glucanotransferase ([EC 2.4.1.19]; CGTase) immobilized on a capillary membrane was investigated using low molecular weight substrates such as cyclodextrin (CD), maltooligosaccharide (MOS), and a CD-MOS mixture. The immobilized CGTase catalyzed the conversion reaction of α-CD to β-CD and MOS or β-CD to α-CD and MOS within a short residence time. The conversion ratio increased as the amount of immobilized CGTase increased. The addition of glucose, maltose, and sucrose as acceptors in the substrate solution containing CD resulted in the acceleration of CD degradation compared with only CD substrate. Furthermore, the MOS substrate (degree of polymerization =2–6) was disproportionated with a conversion ratio exceeding 70% by the immobilized CGTase. These data demonstrate that immobilized CGTase can catalyze intermolecular transglycosylation between low molecular substrates in a few minutes by regulating the amount of immobilized enzyme and the residence time. This might contribute to our comprehension of CGTase-immobilized bioreactors for CD production as well as to the development of new glycosides through its excellent transglycosylation ability.     

Characterisation of cyclodextrin glucanotransferase fromBacillus circulans ATCC 21783 in terms of cyclodextrin production

Cyclodextrin glucanotransferase (CGTase, EC 2.4.1.19) fromBacillus circulans ATCC 21783 was purified by ultrafiltration and a consecutive starch adsorption. Total enzyme yield of 75.5% and purification factor of 13.7 were achieved. CGTase was most active at 65°C, possessed two clearly revealed pH-optima at 6.0 and 8.6 and retained from 75 to 100% of its initial activity in a wide range of pH, between 5.0 and 11.0. The cyclising activity was enhanced by 1 mM CaCl₂ or 4 mM CoCl₂. The enzyme was thermostable up to 70°C, and 64% of the original activity remained at 70°C after 30 min heat treatment. Up to 41% conversion into cyclodextrins was obtained from 40 g l^?1 starch without using any additives. This CGTase produced two types of cyclodextrins, beta and gamma, in a ratio 73:27 after 4 h reaction time at 65°C. This feature of the enzyme could be of interest for industrial cyclodextrin production.     

Lipase of <Emphasis Type="Italic">Aspergillus niger</Emphasis> NCIM 1207: A Potential Biocatalyst for Synthesis of Isoamyl Acetate

Commercial lipase preparations and mycelium bound lipase from Aspergillus niger NCIM 1207 were used for esterification of acetic acid with isoamyl alcohol to obtain isoamyl acetate. The esterification reaction was carried out at 30°C in n-hexane with shaking at 120 rpm. Initial reaction rates, conversion efficiency and isoamyl acetate concentration obtained using Novozyme 435 were the highest. Mycelium bound lipase of A. niger NCIM 1207 produced maximal isoamyl acetate formation at an alcohol/acid ratio of 1.6. Acetic acid at higher concentrations than required for the critical alcohol/acid ratio lower than 1.3 and higher than 1.6 resulted in decreased yields of isoamyl acetate probably owing to lowering of micro-aqueous environmental pH around the enzyme leading to inhibition of enzyme activity. Mycelium bound A. niger lipase produced 80 g/l of isoamyl acetate within 96 h even though extremely less amount of enzyme activity was used for esterification. The presence of sodium sulphate during esterification reaction at higher substrate concentration resulted in increased conversion efficiency when we used mycelium bound enzyme preparations of A. niger NCIM 1207. This could be due to removal of excess water released during esterification reaction by sodium sulphate. High ester concentration (286.5 g/l) and conversion (73.5%) were obtained within 24 h using Novozyme 435 under these conditions.     

Immobilization of cyclodextrin glucanotransferase on capillary membrane

A bioreactor system with the enzyme immobilized on a capillary membrane is a promising tool for the mass production of valuable substances, because of the good productive efficiency. To investigate the kinetics of immobilized cyclodextrin glucanotransferase ([EC 2.4.1.19]; CGTase) on a capillary membrane in a bioreactor system, the amount of immobilized CGTase and the operating conditions, such as pressure and the reaction temperature, were examined under a constant substrate concentration (1.0%) and a constant flow rate (0.12 m/s). When the CGTase was immobilized at a concentration of 0.04 to 0.62 mg per membrane area (cm²), the decrease in the immobilized amount of CGTase resulted in an increase in the cyclodextrin production rate (g of CD/h·m²; CPR) and the CPR correlated well with the flux of the CGTase-immobilized membrane. Although a higher reaction temperature caused an increase in the CPR within a short operating time of the bioreactor, repeated operation at 60°C led to a reduction in the CPR due to the denaturation of the immobilized CGTase. The percentage of cyclodextrin (CD) to total sugar obtained in the permeate was slightly more than 60% under most operating conditions, but immobilization of the excess amount of CGTase (0.42–0.62 mg/cm²) reduced the CD yield as well as the ratio of α-CD to β-CD, suggesting that it led to a CGTase side-reaction such as intermolecular transglycosylation. These data suggest that the conditions under which the bioreactor with 0.04–0.40 mg/cm² was operated; a reaction temperature of 50°C, a residence time of 1–2 min and adjustable pressure, could be employed to obtain a high CPR using a large scale CGTase-immobilized membrane bioreactor.     

Optimization of cyclodextrin production from sago starch

Cyclodextrin (CD) is synthesized by bacterial cyclodextrin glycosyltransferase (CGTase) and is widely used in food, pharmaceutical, cosmetic, and agricultural industries. In this study, Bacillus circulans CGTase was partially purified by ammonium sulfate precipitation at 50-70% saturation. The optimum pH and temperature for CD production from sago starch were found to be in the ranges of 4.5-5.0 and 55-60 degrees C, respectively. beta-CD was the predominant product, constituting 65% of all CD products. The beta-CD produced using partially purified and crude CGTase were compared and found to have no significant difference in yield and productivity. The appropriate proportion of CGTase to sago starch for beta-CD production was determined by response surface methodology. The most appropriate enzyme:substrate ratio was 50 U g sago starch(-1) CGTase and 60 g l(-1) sago starch.     

Conversion of 17α-methyltestosterone to methandrostenolone by the bacterium pimelobacter simplex VKPM Ac-1632 with the presence of cyclodextrins

Conditions of conversion of 17α-methyltestosterone to methandrostenolone with the presence of modified β-cyclodextrins (methylcyclodextrin, hydroxypropylcyclodextrin, and hydroxyethylcyclodextrin) in the steroid: cyclodextrin ratio 1: 1 were studied. The experimental solutions of modified β-cyclodextrins were prepared in deionized water with 5–7% methanol. Under the conditions found to be optimal, 1,2–dehydrogenation of 17α-methyltestosterone was carried out with 2–4 g/l Pimelobacter simplex VKPM Ac-1632 biomass. At the substrate concentration 5–20 g/l, the reaction occurred for 1–15 h without any by-products. The maximum rate of methandrostenolone accumulation was observed with hydroxypropylcyclodextrin. The methylcyclodextrin solution can be reused for complete 17α-methyltestosterone conversion at the concentration 5 g/l.     

Lipase catalyzed acetylation of 3,5,4′-trihydroxystilbene: optimization and kinetics study

The use of immobilized lipase from Candida antarctica (Novozym(?) 435) to catalyze acetylation of trans-3,5,4'-trihydroxystilbene was investigated in this study. Response surface methodology and 5-level-4-factor central composite rotatable design were adopted to evaluate the effects of synthesis variables, including reaction time (24-72 h), temperature (25-65 °C), substrate molar ratio (1:15-1:75), and enzyme amount (600-3,000 PLU) on the percentage molar conversion of trans-4'-O-acetyl-3,5-dihydroxystilbene. The results showed that reaction temperature and enzyme amount were the most important parameters on percentage molar conversion. Based on ridge max analysis, the optimum conditions for synthesis were: reaction time 60 h, reaction temperature 64 °C, substrate molar ratio 1:56 and enzyme amount 2,293 PLU. The molar conversion of actual experimental values was 95% under optimal conditions. The synthesis product was analyzed using HPLC, mass and NMR. The results revealed that the major product was trans-4'-O-acetyl-3,5-dihydroxystilbene. The reaction kinetics was found to follow the Ping-Pong mechanism; substrate inhibition was not found at high vinyl acetate concentration.     

Optimization of a heterogeneous reaction system for the production of optically active D-amino acids using thermostable D-hydantoinase

A thermostable D-hydantoinase from Bacillus stearothermophilus SD-1 was previously mass-produced by batch cultivation of the recombinant E. coli harboring the gene encoding the enzyme (Lee et al., 1997). In this work, we attempted to optimize the process for the production of N-carbamoyl-D-p-hydroxyphenylglycine, which is readily hydrolyzed to D-p-hydroxyphenylglycine under acidic conditions, from 5-(4-hydroxyphenyl)hydantoin using the mass-produced D-hydantoinase. In an effort to overcome the low solubility of the substrate, enzyme reaction was carried out in a heterogeneous system consisting of a high substrate concentration up to 300 g/L. In this reaction system, most of substrate is present in suspended particles. Optimal temperature and pH were determined to be 45 degrees C and 8.5, respectively, by taking into account the reaction rate and conversion yield. When the free enzyme was employed as a biocatalyst, enzyme loading higher than 300 unit/g-substrate was required to achieve maximum conversion. Use of whole cell enzyme resulted in maximum conversion even at lower enzyme loadings than the free enzyme, showing 96% conversion yield at 300 g/L substrate. The heterogeneous reaction system used in this work might be applied to the enzymatic production of other valuable compounds from a rarely water-soluble substrate.     

Addition of polar organic solvents can improve the product selectivity of cyclodextrin glycosyltransferase. Solvent effects on cgtase

Cyclodextrin glycosyltransferase (EC 2.4.1.19, CGTase) is an enzyme that produces cyclodextrins from starch via an intramolecular transglycosylation reaction. Addition of small amounts (10% v/v) of polar organic solvents can affect both the overall production yield and the type of cyclodextrin produced from a maltodextrin substrate under simulated industrial process conditions. Using CGTase from Thermoanaerobacter sp. all solvents produced an increase in cyclodextrin yield when compared with a control, the greatest increase being obtained with addition of ethanol (26%). In addition product selectivity was affected by the nature of the organic solvent used: beta-cyclodextrin was favoured in the absence of any solvent and on the addition of dimethylsulphoxide, t-butanol and dimethylformanide while alpha-cyclodextrin was favoured by addition of acetonitrile, ethanol and tetrahydrofuran. With CGTase from Bacillus circulans strain 251 relatively smaller increases in overall cyclodextrin production were achieved (between 5-10%). Addition of t-butanol to a B. circulans catalysed reaction however did produce the largest selectivity for beta-cyclodextrin of any solvent-enzyme combination (82%). The effect of solvent addition was shown not to be related to the product inhibition of CGTase, but may be related to reduced competition from the intermolecular transglycosylation reaction that causes degradation of cyclodextrin products. This rate of this reaction was shown to be dependent on the nature of the organic solvent used.     

Production of cyclodextrins using moderately heat-treated cornstarch

Cyclodextrins are very useful compounds for the food, cosmetic, pharmaceutic, and plastic industries. We developed a process for the production of cyclodextrins from moderately heat-treated cornstarch. This method had many merits. First, the cyclodextrins were not degraded by cyclodextrin glucanotransferase, because low molecular weight maltodextrins were hardly produced. Second, it was possible to remove the residual cornstarch by a simple method such as filtration or centrifugation. Third, the amount of cyclodextrin glucanotransferase used for cyclodextrin production was less than that using the traditional method. Fourth, the pretreating method was simple. And fifth, the residual starch could be used as substrate for the production of other compounds. Cyclodextrins were produced at optimum conditions: heating temperature was 65°C; heating time was 1 h; concentration of substrate was 7.5%; amount of enzyme loaded was 48 U g⁻¹ of substrate. Using these conditions, the results were as follows: the content of cyclodextrins, 50%; the conversion yield of substrate, 25%; the productivity per enzyme unit, 5.22 mg of cyclodextrins.     

酶法转化DL-ATC合成L-半胱氨酸的酶促反应条件研究

目的:考察酶源保存方式、酶促反应时间、底物pH值、底物浓度、酶浓度、金属离子等因素对酶活力的影响。方法:以假单胞菌(Pseudomonassp.)TS1138为供试菌株,采用酸式茚三酮法测定L-半胱氨酸含量,研究了酶法转化DL-ATC合成L-半胱氨酸的酶促反应条件。结果:TS1138菌株中L-半胱氨酸脱巯基酶具有较高的活性,而且Mg2 、Mn2 、Fe2 、Zn2 、Cu2 等5种金属离子对DL-ATC水解酶酶系有不同程度的抑制,其中Cu2 对该酶系的抑制作用很大。结论:确定了TS1138菌株酶法转化DL-ATC合成L-半胱氨酸的最适酶促反应条件,为酶促反应动力学的研究奠定了基础。     

Lipase-catalyzed acyl exchange of soybean phosphatidylcholine in n-Hexane: a critical evaluation of both acyl incorporation and product recovery

Lipase-catalyzed acidolysis was examined for the production of structured phospholipids in a hexane system. In a practical operation of the reaction system, the formation of lyso-phospholipids from hydrolysis is often a serious problem, as demonstrated from previous studies. A clear elucidation of the issue and optimization of the system are essential for the practical applications in reality. The effects of enzyme dosage, reaction temperature, solvent amount, reaction time, and substrate ratio were optimized in terms of the acyl incorporation, which led to the products, and lyso-phospholipids formed by hydrolysis, which led to the low yields. The biocatalyst used was the commercial immobilized lipase Lipozyme TL IM and substrates used were phosphatidylcholine (PC) from soybean and caprylic acid. A response surface design was used to evaluate the influence of selected parameters and their relationships on the incorporation of caprylic acid and the corresponding recovery of PC. Incorporation of fatty acids increased with increasing enzyme dosage, reaction temperature, solvent amount, reaction time, and substrate ratio. Enzyme dosage had the most significant effect on the incorporation, followed by reaction time, reaction temperature, solvent amount, and substrate ratio. However the parameters had also a negative influence on the PC recovery. Solvent amount had the most negative effect on recovery, followed by enzyme dosage, temperature, and reaction time. Individually substrate ratio had no significant effect on the PC recovery. Interactions were observed between different parameters. On the basis of the models, the reaction was optimized for the maximum incorporation and maximum PC recovery. With all of the considerations, the optimal conditions are recommended as enzyme dosage 29%, reaction time 50 h, temperature 54 degrees C, substrate ratio 15 mol/mol caprylic acid/PC, and 5 mL of hexane per 3 g substrate. No additional water is necessary. Under these conditions, an incorporation of caprylic acid up to 46% and recovery of PC up to 60% can be obtained from the prediction. The prediction was confirmed from the verification experiments.     

A comparative study of the regioselectivity of the β-galactosidases from Kluyveromyces lactis and Bacillus circulans in the enzymatic synthesis of N-Acetyl-lactosamine in aqueous media

The enzymatic synthesis of N-acetyl-lactosamine (LacNAc) was studied in aqueous media with high substrate concentrations using the transgalactosylation of N-acetyl-D-glucosamine (GlcNAc), starting from lactose as a galactosyl donor. The efficiency and regioselectivity of the β-galactosidases from Kluyveromyces lactis (KlβGal) and Bacillus circulans (BcβGal) were compared. The reaction was optimized by varying the experimental conditions (pH, catalytic activity concentration, and mass concentration ratio of the substrates), which enhanced the synthesis yields with both enzymes and especially with BcβGal. BcβGal catalyzed the formation of the maximal LacNAc concentration obtained (101 mM or 39 g L(-1), corresponding to a yield of 11% on the basis of GlcNAc conversion), after 5 h at pH 6.5 and for a substrate mass concentration ratio of 1. This enzyme also gave an optimal synthesis yield of about 17.5%. No change in regioselectivity was observed when using KlβGal, whereas the regioselectivity of BcβGal proved to be subject to variations, the 1-4 and 1-6 linkages being favored under kinetic and thermodynamic control conditions, respectively. Finally, it was demonstrated that the N-acetyl-allolactosamine synthesized during the GlcNAc transgalactosylation catalyzed by BcβGal was a thermodynamic product and did not result from a chemical and/or enzymatic isomerization of LacNAc.     

Effect of different substrates and their preliminary treatment on cyclodextrin production

Summary Various kinds of substrates were tested for cyclodextrin production with cyclodextrin glucanotransferase (CGTase) from Bacillus megaterium. The enzyme formed cyclodextrin from different kinds of starch, dextrins, amylose, and amylopectin. However, the highest degree of conversion was obtained from starch. Corn starch appeared to be the best substrate – the cyclodextrin yield was 50.9%. The effect of molecular mass and preliminary treatment of starch with α-amylase on the CD yield was investigated. It was proved that CGTase preferred native starch with high molecular mass and low dextrose equivalent. The preliminary treatment with α-amylase occurred to be inefficient and unnecessary since it did not lead to an increase in the CD yield. Some of the substrates were treated with pullulanase. The effect of debranching was highest in the case of corn starch: the cyclodextrin yield increased by 10%.     

Molecular imprinting of cyclodextrin glycosyltransferases from Paenibacillus sp. A11 and Bacillus macerans with gamma-cyclodextrin

Cyclodextrin glycosyltransferase catalyzes the formation of a mixture of cyclodextrins from starch by an intramolecular transglycosylation reaction. To manipulate the product specificity of the Paenibacillus sp. A11 and Bacillus macerans cyclodextrin glycosyltransferases towards the preferential formation of gamma-cyclodextrin (CD(8)), crosslinked imprinted proteins of both cyclodextrin glycosyltransferases were prepared by applying enzyme imprinting and immobilization methodologies. The crosslinked imprinted cyclodextrin glycosyltransferases obtained by imprinting with CD(8) showed pH and temperature optima similar to those of the native and immobilized cyclodextrin glycosyltransferases. However, the pH and temperature stability of the immobilized and crosslinked imprinted cyclodextrin glycosyltransferases were higher than those of the native cyclodextrin glycosyltransferases. When the catalytic activities of the native, immobilized and crosslinked imprinted cyclodextrin glycosyltransferases were compared, the efficiency of the crosslinked imprinted enzymes for CD(8) synthesis was increased 10-fold, whereas that for cyclodextrin hydrolysis was decreased. Comparison of the product ratios by high-performance anion exchange chromatography showed that the native cyclodextrin glycosyltransferases from Paenibacillus sp. A11 and Bacillus macerans produced CD(6) : CD(7) : CD(8) : > or = CD(9) ratios of 15 : 65 : 20 : 0 and 43 : 36 : 21 : 0 after 24 h of reaction at 40 degrees C with starch substrates. In contrast, the crosslinked imprinted cyclodextrin glycosyltransferases from Paenibacillus sp. A11 and Bacillus macerans produced cyclodextrin in ratios of 15 : 20 : 50 : 15 and 17 : 14 : 49 : 20, respectively. The size of the synthesis products formed by the crosslinked imprinted cyclodextrin glycosyltransferases was shifted towards CD(8) and > or = CD(9), and the overall cyclodextrin yield was increased by 12% compared to the native enzymes. The crosslinked imprinted cyclodextrin glycosyltransferases also showed higher stability in organic solvents, retaining 85% of their initial activity after five cycles of synthesis reactions.     

Enzymatic hydrolysis of hydrophobic triolein by lipase in a mono-phase reaction system containing cyclodextrin; Reaction characteristics

A hydrophobic substrate triolein was hydrolyzed by lipase in a mono-phase reaction system containing cyclodextrin(CD) as emulsifier. The triolein was transformed to an emulsion-like state in the CD containing reaction system in contrast to the oil-droplet like state without CD due to the formation of an inclusion complex between the lipids and CDs. The hydrolysis reaction increased substantially in the CD containing reaction system, and the optimum reaction conditions including the amount of lipase, β-CD concentration, and mixing ratio of triolein and β-CD, were determined. The performance of the enzyme reaction in a mono-phase reaction system was compared with that of a two-phase reaction system which used water immiscible hexane as the organic solvent. The role of a CD in the mono-phase reaction system was elucidated by comparing the degree of the inclusion complex formation with triolein and oleic acid, K_m and V_max values, and product inhibition by oleic acid in aqueous and CD containing reaction systems. The resulting enhanced reaction seems to be caused by two phenomena; the increased accessibility of lipase to triolein and reduced product inhibition by oleic acid through the formation of an inclusion complex.     

Inhibition of beta-lactamase of Bacillus licheniformis 749/C by compound PS-5, a new beta-lactam antibiotic.

By use of a new computer-assisted u.v.-spectrophotometric assay method, the kinetic parameters of the reaction catalysed by Bacillus licheniformis 749/C beta-lactamase were re-examined and the mode of inhibition of the enzyme by compound PS-5, a novel beta-lactam antibiotic, was studied with benzylpenicillin as substrate. (1) The fundamental assay conditions for the determination of Km and V were examined in detail with benzylpenicillin as substrate. In 0.1 M-sodium/potassium phosphate buffer, pH 6.8, at 30 degrees C, initial substrate concentrations of benzylpenicillin above 0.7 mM were very likely to lead to substrate inhibition. The Km value of the enzyme for benzylpenicillin at initial concentrations from 1.96 to 0.07 mM was calculated to be 97-108 microM. (2) The Km values of the enzyme for 6-aminopenicillanic acid, ampicillin and cephaloridine were found to be 25, 154-161 and 144-161 microM respectively. (3) Compound PS-5 was virtually unattacked by Bacillus licheniformis 749/C beta-lactamase. (4) The activity of the enzyme was diminished by compound PS-5, to extents depending on the duration of incubation and the concentration of the inhibitor. The rate of inactivation of the enzyme by compound PS-5 followed first-order kinetics. (5) In an Appendix, a new computer-assisted u.v.-spectrophotometric enzyme assay method, in which a single reaction progress curve of time-absorbance was analysed by the integrated Michaelis-Menten equation, was devised for the accurate and precise determination of the kinetic constants of beta-lactamase. For conversion of absorbance readings into molar substrate concentrations, the initial or final absorbance reading that was independent of the reaction time was used as the basis of calculation. In calculation of Km and V three systematic methods of data combination were employed for finer analysis of the reaction progress curve. A list of the computer program named YF6TAIM is obtainable from the author on request or as Supplementary Publication SUP 50100 (12 pages) from the British Library Lending Division, Boston Spa, Wetherby, West Yorkshire LS23 7BQ, U.K., on the terms indicated in Biochem. J. (1978) 169, 5.     

Purification, characterization, and kinetic mechanism of S-adenosyl-L-methionine:macrocin O-methyltransferase from Streptomyces fradiae

S-Adenosyl-L-methionine:macrocin O-methyltransferase catalyzes conversion of macrocin to tylosin, the terminal and main rate-limiting step of tylosin biosynthesis in Streptomyces fradiae. The O-methyltransferase was stabilized in vitro and purified to electrophoretic homogeneity. The purified enzyme had a molecular weight of 65,000 and consisted of two identical subunits of 32,000 with an isoelectric point of 4.5. The enzyme required Mg2+, Mn2+, or Co2+ for maximal activity and was catalytically optimal at pH 7.5-8.0 and 31 degrees C. The O-methyltransferase catalyzed the conversion of macrocin to tylosin at a stoichiometric ratio of 1:1. The enzyme also mediated conversion of lactenocin----desmycosin. The corresponding Vmax/Km ratios for the two analogous conversions were similar, and both enzymic conversions were susceptible to extensive competitive and noncompetitive inhibitions by macrolide metabolites. Steady-state kinetic studies for initial velocity, substrate analogue, and product inhibitions have allowed formulation of Ordered Bi Bi as the reaction mechanism for macrocin O-methyltransferase.     

Some kinetic properties of gamma-glutamyltransferase from rabbit liver

gamma-Glutamyltransferase ((5-glutamyl)-peptide: amino-acid 5-glutamyltransferase, EC 2.3.2.2) of rabbit liver (detergent form) was purified 1100-fold in order to study its kinetic properties. Kinetic studies were conducted from pH 6.0 to 12.0 in the absence and presence of the acceptor substrate glycylglycine using gamma-glutamyl-3-carboxy-4-nitroanilide as the donor. The existence of more than one binding site for both donor and acceptor is postulated on kinetic evidence such as donor substrate activation, donor substrate inhibition and acceptor substrate activation. Homotropic interaction is also observed, in the form of negative cooperativity, in donor substrate binding, in the absence of acceptor at pH less than 9.0 and positive cooperativity (n = 2), in the absence or presence of acceptor at pH greater than 9.0. Hydrolase reaction reaches a maximum of activity at pH 10 (pK 8.6). Transferase activity under conditions of maximal velocity is maximal at pH 9.0 (pK 7.1). The ratio of transferase activity/hydrolase activity is maximal at pH 7.0-7.5. At low donor substrate concentrations, maximal activity is attained at pH 7.5.