Production of immobilized penicillin acylase using aqueous polymer systems for enzyme purification and in situ immobilization

A novel approach for the isolation and purification of penicillin acylase (PA), which couples aqueous two-phase partitioning and enzyme immobilization has been investigated.A PA yield of 90% was achieved by treating E. coli cells with 4% butyl acetate, freeze-thawing step, and pressure homogenization. PA purification (93% recovery) was achieved by (1) removing cell debris via precipitation with polyethylene glycol (PEG 2000); (2) aqueous two-phase partitioning using a PEG 2000 + phosphate system (87% recovery).An in situ enzyme immobilization approach, using oxirane acrylic or aldehyde-agarose beads dispersed in the PEG-rich phase, was explored for the conversion of penicillin G to 6-aminopenicillanic acid. An appropriate immobilization reaction time was found. The catalytic performance of the enzyme, when immobilized, was found not to be affected by recycling of the phase-forming components.     

A single step purification process for cyclodextrin glucanotransferase from a Bacillus sp. isolated from soil

Cyclodextrin glucanotransferase (CGTase) is a commercially important enzyme which catalyses the formation of cyclodextrins (CDs) from starch. A CGTase producing bacterium was isolated from soil which gave a fairly high enzyme activity of 7.5 U mL(-1) after 24 h of growth which was further increased to 22 U mL(-1) by proper media design. The enzyme was purified to homogeneity by a novel single affinity precipitation step which resulted in a very high recovery of more than 90%. The molecular weight, as determined by SDS-PAGE, was found to be 68 kDa. The pH optimum was found to be 6.6 while a temperature optimum of 65 degrees C was observed. The enzyme exhibited a fairly high degree of functional stability with little loss of activity, even after 8 h of incubation at 65 degrees C. Ca++ had little effect on the activity of the enzyme while urea at 10 mM concentration increased the activity of the enzyme by more than 200%, suggesting that it is a unique enzyme.     

Biochemical properties of inulosucrase from Leuconostoc citreum CW28 used for inulin synthesis

Biochemical properties of inulosucrase from Leuconostoc citreum CW28, a potential biocatalyst for inulin synthesis, were determined in order to select optimal reaction conditions. The hydrolysis reaction was about 3.5 times more efficient than the transferase reaction. It was found that high sucrose concentrations (≈250 g L^-1) were required for maximum fructose transferase yields. High molecular weight inulin distributions were obtained with cell associated inulosucrase, while lower size products were associated to the activity of the free enzyme in solution. When using whole cells, mannitol was found as a by-product of the reaction resulting from the reduction of fructose released by sucrose hydrolysis. A 30 L pilot plant synthesis with 250 g L^-1 of sucrose was carried out using the cell associated inulosucrase resulting in 76% of the substrate being transformed to inulin.     

人鼠嵌合单克隆抗体c30.6的纯化

采用介体电泳技术对CHO细胞培养液中的人鼠嵌合单克隆抗体c30.6进行纯化,第一步在pH8.6条件下进行,抗体带正电荷而培养液中的大部分杂质带负电荷,抗体和杂质的在电场作用下向两电极运动,结果被分离在分离膜的两侧,SDS－PAGE显示抗体纯度达95％,且剩余杂质的分子量均小于抗体的分子量。第二步是在pH6.0条件下进行,此时抗体和杂质都带正电荷,它们在电场作用下向同一方向运动,但分离膜只允许分子量较小的杂质通过,抗体得以进一步纯化,抗体的回收率为80％,而且生物活性未受影响。     

Cross-linked enzyme aggregates of recombinant Candida antarctica lipase B for the efficient synthesis of olvanil,a nonpungent capsaicin analogue

Despite the proven therapeutic role of capsaicin in human health, its usage is still hampered by its high pungency. In this sense, nonpungent capsaicin analogues as olvanil are a feasible alternative to the unpleasant sensations produced by capsaicin while maintaining a similar pharmacological profile. Olvanil can be obtained by a lipase-catalyzed chemoenzymatic process. In the present work, recombinant Candida antarctica lipase B (CALB) was expressed in Pichia pastoris and subsequently immobilized by cross-linked enzyme aggregate (CLEA) methodology for the synthesis of olvanil. The CALB-CLEAs were obtained directly from the fermentation broth of P. pastoris without any purification step in order to assess the role of the contaminant proteins of the crude extract as co-feeders. The CALB-CLEAs were also bioimprinted to enhance the catalytic performance in olvanil synthesis. When CALB was precipitated with isopropanol, the obtained CALB-CLEAs exhibited the highest activity in the synthesis of olvanil, regardless of the glutaraldehyde concentration. The maximum product synthesis was found at 72 hr obtaining 6.8 g L⁻¹ of olvanil with a reaction yield of 16%. When CALB was bioimprinted with olvanil, the synthesis was enhanced 1.3 times, reaching 10.7 g L⁻¹ of olvanil at 72 hr of reaction with a reaction yield of 25%. Scanning electron microscopy images indicated different morphologies of the CLEAs depending on the precipitating agent and the template used for bioimprinting. Recombinant CALB-CLEAs obtained directly from the fermentation broth are a suitable alternative to commercial enzymatic preparations for the synthesis of olvanil in organic medium.     

Comparison of covalent immobilization of amylase on polystyrene pellets with pentaethylenehexamine and pentaethylene glycol spacers

α-Amylase from Aspergillus oryzae was covalently immobilized onto polystyrene pellets with pentaethylenehexamine (PS-PEHA-Ald) and pentaethylene glycol (PS-PG-Ald) carrying a terminal aldehyde group. Optimum immobilization occured at pH 8.0 and 25 °C, and at pH 7.0 and 35 °C for PS-PEHA-Ald and PS-PG-Ald, respectively. PS-PEHA-Ald immobilized enzyme retained approximately 75% of the initial activity over 45 days of storage, 70% of the initial activity after nine runs of recycling and displayed the better resistance to detrimental metal ions. PS-PG-Ald immobilized enzyme retained approximately 50% of the initial activity in 8h at 70 °C. The catalytic efficiencies of PS-PEHA-Ald immobilized and PS-PG-Ald immobilized amylase were 1.42 and 1.29 times higher than that of native enzyme. The activation energy of the reaction mediated by the amylase was reduced by 58.1% and 57.3% when PS-PEHA-Ald and PS-PG-Ald used as support respectively.     

Partial purification and characterization of extracellular cellulase from a strain ofTrichoderma viride isolated from forest soil

Partial purification of extracellular cellulase ofTrichoderma viride isolated from forest soil was done by ammonium sulfate precipitation of culture supernatant, centrifugation at higher speed, solubilization of protein in sodium acetate buffer and dialysis. The specific activity of cellulase in the culture supernatant, was 136 nkat/mg which was increased by 172% after the completion of final step (234 nkat/mg). The recovery of enzyme was 70%. The enzyme was characterized by demonstration of optimum activity at 55°C and pH 5.0 with 1% carboxymethyl cellulose as substrate.     

Affinity precipitation and macroaffinity ligand facilitated three-phase partitioning for refolding and simultaneous purification of urea-denatured pectinase

Protein refolding is an integral step in the recovery of protein activity from inclusion bodies. It is shown that affinity precipitation and macroaffinity ligand facilitated three-phase partitioning (MLFTPP) led to refolding of urea-denatured pectinase present in a commercial preparation, with simultaneous purification. Affinity precipitation consists of precipitation of the desired enzyme by complexing it with a suitable stimulus-sensitive macroaffinity ligand. This ligand in this case was alginate/esterified alginate. The complex of the polymer-pectinase could be precipitated by adding calcium ions. In MLFTPP (carried out by adding tertiary butanol and ammonium sulfate to the aqueous solution of crude enzyme and the polymer), the polymer or its complex with the enzyme form an interfacial precipitate between tert-butyl alcohol phase and aqueous phase. It is believed that in both processes, while molecular recognition of alginate/esterified alginate to pectinase facilitates their selective binding to the enzyme, the correct refolding is facilitated by preventing molecular aggregation of unfolded enzyme molecules. Three-phase partitioning with esterified alginate as the macroaffinity ligand gave 100% recovery with 4-fold purification. Affinity precipitation with 1% alginate gave 52% yield with 18-fold purification. On the other hand, use of 0.5% esterified alginate gave only 7-fold purification but with 75% recovery of activity.     

Improved Method for Prufication of 2'',3''-Cyclic Nucleotide 3''-Phosphohydrolase from Bovine Cerebral White Matter

Abstract: An improved procedure of the solubilization and purification of 2′,3′-cyclic nucleotide 3′-phosphohydrolase (CNPase) from bovine cerebral white matter is reported. To remove easily extractable protein, the tissue was homogenised in 10 vol. of 0.5 M-ammonium acetate containing 10 mM-Tris. HCI, pH 6.9, at 4°C and centrifuged at 105,000 g for 60 min. The precipitate was extracted with 10 vol. of 0.5% Triton X-100 containing 10 mM-Tris. HCI, pH 6.9, and centrifuged, By this extraction, over 70% soluble protein could be removed in the supernatant and most CNPase activity was kept in the precipitate. The precipitate was extracted with 10 vol. of 1% Triton X-100 and 1 M-ammonium acetate mixture containing 10 mM-Tris.HCI, pH 8.2, and centrifuged at 105,000 g for 60 min. The extract contained 54% of CNPase and the specific activity was fivefold that of the original homogenate. Subsequently, the extractions were carried out with 2% Triton X-100-2 M-ammonium acetate and 4% Triton X-100-4 M-ammonium acetate at pH 8.2. The recovery of CNPase was found to be nearly 90% from the original homogenate, without loss of enzyme activity during extraction, while much CNPase activity was lost when guanidinium chloride was used as the extraction medium. Using the Triton X-100-ammonium acetate extract, several column chromatography techniques were applied to purify the enzyme. In the first step, Phenyl-Sepharose CL-4B column chromatography was performed by eluting with a double-linear gradient of ammonium acetate and Triton X-100. In the second step, the fraction containing CNPase after Phenyl-Sepharose CL-4B column chromatography was applied to a Sepharose 6B column and the enzyme was eluted with 1% Triton X-100- I M-ammonium acetate, pH 8.2. The peak containing CNPase was applied to CM-Sepharose CL-6B column chromatography in the final step. The enzyme was eluted with a linear gradient of KCI. In this step, CNPase eluted as a sharp peak and the specific activity was approximately 2300 pmol 2′-AMP formed/min/mg protein. The recovery of CNPase from the original homogenate was about 50%. By the isoelectrofocusing technique, the pI of CNPase was found to be 8.6. When Reisfeld polyacrylamide gel electrophoresis and SDS-polyacrylamide gel electrophoresis were carried out on the purified CNPase, only one protein band, corresponding to CNPase activity, was detected. Its molecular weight was estimated to be approximately 51,000 as the active enzyme form. K, value of the purified enzyme for 2′,3′-CAMP calculated from a Lineweaver-Burk plot was 3.13 mM.     

Production and extraction of pectinases obtained by solid state fermentation of agroindustrial residues with Aspergillus niger

In this work soy and wheat bran were employed as raw materials for the production of pectinases by Aspergillus niger through solid-state fermentation. Several fermentation and recovery parameters were studied. The kinetics of enzyme synthesis was investigated in the range from 13 to 96 h with moisture contents varying from 25% to 70% (w/w). A medium moisture content of 40% and a fermentation time of 22 h were selected, as these conditions resulted in high pectolytic activity and enhanced polygalacturonase productivity. In order to optimise the recovery step, the best combination of temperature of extraction, contact time and solvent type was investigated. Acetate buffer (pH 4.4), 35°C and 30 min provided the best recovery. The present results show that optimising the extraction conditions is a simple way of obtaining more concentrated enzyme extracts and could be a useful instrument to extract more selectively a desired biomolecule from fermented solids.     

Chemo-enzymatic synthesis of arginine-based gemini surfactants

A novel chemo-enzymatic synthesis of arginine-based gemini cationic surfactants bis(Args) is reported. These compounds consist of two single N(alpha)-acyl-arginine structures connected through the alfa-carboxylic groups of the arginine residues by a alpha, omega-diaminoalkane spacer chain. N(alpha)-Acyl-L-arginine alkyl ester derivatives were the starting building blocks for the synthesis. The best strategy found consisted of two steps. First, the quantitative acylation of one amino group of the spacer by the carboxylic ester of the N(alpha)-acyl-arginine took place spontaneously, at the melting point of the alpha,omega-diaminoalkane, in a solvent-free system. The second step was the papain-catalyzed reaction between another N(alpha)-acyl-arginine alkyl ester and the free aliphatic amino group of the derivative formed in the first step. Reactions were carried out in solid-to-solid and solution systems using low-toxic potential solvents. Changes in reaction performance and product yield were studied for the following variables: organic solvent, support for enzyme deposition and substrate concentration. The best yields (70%) were achieved in solid-to-solid systems and in ethanol at a(w) = 0.07. Bis(Args) analogs of 8, 10 and 12 carbon atoms using 1,3-diaminopropane and 1, 3-diamino-2-hydroxy-propane as hydrocarbon spacers were prepared at the 6-7 gram level employing the methodology developed. The overall yields which include reaction and purification varied from 51% to 65% of pure (97-98% by HPLC) product.     

Enzyme recovery during gas/liquid two-phase flow microfiltration of enzyme/yeast mixtures

The effect of a gas/liquid two-phase flow on the recovery of an enzyme was evaluated and compared with standard crossflow operation when confronted with the microfiltration of a high-fouling yeast suspension. Ceramic tubular and flat sheet membranes were used. At constant feed concentration (permeate recycling) and transmembrane pressure, the results obtained with the tubular membrane were dependent on the two-phase flow pattern. In comparison with single-phase flow performances at the same liquid velocity, the enzyme transmission was maintained at a high level with a bubble flow pattern but it decreased by 70% with a slug flow, whatever the flow rate ratio. Identical results were obtained with flat sheet membranes: for the highest flow rate ratio, the enzyme transmission was reduced by 70% even though the permeate flux was improved by 240%. During diafiltration experiments with the tubular membrane, it was found that a bubble flow pattern led to a 13% higher enzyme recovery compared to single-phase flow conditions, whereas with a slug flow the enzyme recovery was strongly reduced. With bubble flow conditions, energy consumption was minimal, confirming that this flow pattern was the most suitable for enzyme recovery.     

One-step purification of chitinase from Serratia marcescens NK1, a soil isolate

AIMS: A simple single step technique of gel filtration was developed for the purification of chitinase from Serratia marcescens NK1. METHODS AND RESULTS: Chitinase from Ser. marcescens NK1 was purified to homogeneity by gel filtration chromatography with 9.2% recovery. The enzyme had a pH optimum of 6.2 and a temperature optimum of 47 degrees C. It was stable in a wide pH range of 3.0 to 10.0, retaining 60% activity at pH 3.0 and 65% activity at pH 10.5. It retained 70% activity at 28 degrees C after 72 h and nearly 50% activity at 50 degrees C up to 24 h. CONCLUSION: The chitinase from Ser. marcescens NK1 can be efficiently purified in a single step by gel filtration chromatography. The chitinase of Ser. marcescens NK1, a soil isolate, is highly stable and as active as that of other reported isolates of Ser. marcescens. SIGNIFICANCE AND IMPACT OF THE STUDY: This purification scheme is advantageous because of its simplicity and can therefore be applied for the purification of other enzymes. The yield is sufficient for initial characterization studies of the enzyme, and an improved resolution can be obtained if the chromatography is done under fast flow systems.     

枯草芽孢杆菌SA-22 β-甘露聚糖酶的纯化及其特性

利用硫酸铵沉淀、羟基磷灰石柱层析、Sephadex G-75凝胶过滤和DEAE-52离子交换柱层析的方法,将枯草芽孢杆菌SA-22 β-甘露聚糖酶纯化了30.75倍,同时,该酶比活达到3478056 u/mg,收率达到23.43%。利用SDS-PAGE凝胶电泳和Sephadex G-75凝胶过滤的方法测得枯草芽孢杆菌SA-22 β-甘露聚糖酶的分子量分别为38 kD和34 kD。实验发现该酶的最适pH为6.5,在pH 5～10的范围内稳定;该酶最适温度为70℃,在50℃保温4h后其活力不变,在60℃保温4 h后剩余酶活为74.2%,70℃的酶活半衰期为3h。实验还发现Hg²⁺对酶活力有明显抑制作用。该酶对槐豆胶和魔芋胶的K_m和V_max值分别为11.30mg/mL, 4.76mg/mL和188.68(μmol·mL^-1·min^-1), 114.94(μmol·mL^-1·min^-1)。     

A simplified purification and some properties of ribulose 1,5-diphosphate carboxylase from barley

A rapid procedure was developed for purifying ribulose 1,5-diphosphate carboxylase from barley leaves. After (NH₄)₂SO₄ fractionation, the unique sedimentation properties of the enzyme were exploited to effect a single step purification to 90% homogeneity. High speed centrifugation pelleted the enzyme with complete recovery of activity. Residual impurities were then removed by diethylaminoethyl cellulose chromatography and density gradient centrifugation. The purified protein exhibited size heterogeneity due to polymerization. The polymerization products were enzymatically active aggregates of ribulose 1,5-diphosphate carboxylase and were precipitated by an antibody specific for the enzyme.     

Purification and characterization of extracellular dextranase from a novel producer, Hypocrea lixii F1002, and its use in oligodextran production

Fungi were isolated from natural soil samples and screened for extracellular dextranase synthesis. The strain F1002 was identified as Hypocrea lixii using a standard internal transcribed spacer ribosomal DNA analysis and was selected for extracellular dextranase synthesis. The enzyme was purified via ammonium sulfate precipitation and Sepharose 6B chromatography, which resulted in an 8.3-fold increase in the specific activity and a 10.73% recovery. This enzyme is a monomeric protein with a molecular mass of 62 kDa, as determined by sodium dodecyl sulfate-polyacrylamide gel electrophoresis. The purified enzyme, which was identified as an endodextranase, had an optimum pH of 5.0 and an optimum temperature of 25 °C. The dextranase activity was enhanced by Mg²⁺, Al³⁺, and especially Zn²⁺ at a low concentration, which improved its activity to 124.22%. The enzyme has a very high hydrolytic affinity toward high-molecular weight dextrans. Setting the concentrations of the H. lixii F1002 dextranase (2.31 U/mL) and dextrans (6%), as well as the reaction time (45 min), allowed the dextranase to hydrolyze dextrans of controlled molecular weights (20–70 kDa). Three types of oligodextrans with different molecular weights (namely, 69,376, 38,251, and 21,364 Da) were obtained, with a total yield of 80.32%.     

Quality Assessment and Circularity Potential of Recovery Systems for Household Plastic Waste

Plastic recycling is promoted in the transition toward a circular economy and a closed plastic loop, typically using mass‐based recycling targets. Plastic from household waste (HHW) is contaminated and heterogeneous, and recycled plastic from HHW often has a limited application range, due to reduced quality. To correctly assess the ability to close plastic loops via recycling, both plastic quantities and qualities need to be evaluated. This study defines a circularity potential representing the ability of a recovery system to close material loops assuming steady‐state market conditions. Based on an average plastic waste composition including impurities, 84 recovery scenarios representing a wide range of sorting schemes, source‐separation efficiencies, and material recovery facility (MRF) configurations and performances were assessed. The qualities of the recovered fractions were assessed based on contamination and the circularity potential calculated for each scenario in a European context. Across all scenarios, 17% to 100% of the generated plastic mass could be recovered, with higher source‐separation and MRF efficiencies leading to higher recovery. Including quality, however, at best 55% of the generated plastic was suitable for recycling due to contamination. Source‐separation, a high number of target fractions, and efficient MRF recovery were found to be critical. The circularity potential illustrated that less than 42% of the plastic loop can be closed with current technology and raw material demands. Hence, Europe is still far from able to close the plastic loop. When transitioning toward a circular economy, the focus should be on limiting impurities and losses through product design, technology improvement, and more targeted plastic waste management.     

Immobilized enzymes in reverse micelles: studies with gel-entrapped trypsin and alpha-chymotrypsin in AOT reverse micelles

Trypsin and alpha-chymotrypsin were immobilized by gelentrapment in polyacrylamide cross-linked with N,N(1)-methylenebisacrylamide. The immobilized enzymes are catalytically efficient in suspensions of reverse micelles formed in isooctane by bis(2-ethylhexyl) sodium sulfosuccinate (AOT) and water. Both entrapped enzymes are stable in reverse micellar suspension at room temperature and pH 8.2 for 3 days and lose 30-40% activity after 1 week. The enzymes obey Michaelis-Menten kinetics in the investigated concentration range with K(m) values higher than those in solution. Activity of the enzymes is independent of the water content of the micellar solution. No shift in pH optimum was observed for immobilized trypsin activity toward Nalpha-benzoyl-L-arginine ethyl ester. The utility of the procedure, which combines the advantage of enzyme immobilization and enzymology in reverse micelles, is illustrated by an example of peptide synthesis. In particular, peptide synthesis (e. g., Z--Ala--Phe--Leu--NH(2)) using water-insoluble substrate has been performed with gelentrapped alpha-chymotrypsin in reverse micellar suspension with the advantage of efficient enzyme recycling.     

Enhancement of hydrolytic activity of sphingolipid ceramide N-deacylase in the aqueous-organic biphasic system

Lysoglycosphingolipids were produced from glycosphingolipids by using sphingolipid ceramide N-deacylase, which cleaves the N-acyl linkage between fatty acids and sphingosine bases in various glycosphingolipids. The enzyme reaction was done in a biphasic media prepared with water;-immiscible organic solvent and aqueous buffer solution containing the enzyme. We investigated the effects of organic solvents and detergents on lysoglycosphingolipid production in the biphasic system. Among the organic solvents tested, n-butylbenzene, cumene, cyclodecane, cyclohexane, n-decane, diisopropylether, n-heptadecane, and methylcyclohexane promoted hydrolysis of GM1, whereas benzene, chloroform, ethyl acetate, and toluene inhibited GM1 hydrolysis. Hydrolysis of asialo GM1, GD1a, GalCer, and sulfatide was also enhanced by the addition of n-decane. The hydrolytic activity of the enzyme was enhanced by the addition of 0.8% sodium taurodeoxycholate or sodium cholate to the aqueous phase. The most effective hydrolysis of various glycosphingolipids by the enzyme was thus obtained in the aqueous-n-decane biphasic system containing 0.8% sodium taurodeoxycholate. Under this condition, the fatty acids released from GM1 by the action of the enzyme were trapped and diffused into the organic phase, while lysoGM1 remained in the aqueous phase.Thus the almost complete hydrolysis of GM1 was achieved using the biphasic system, while at most 70% of hydrolysis was obtained using normal aqueous media possibly due to the inhibition of hydrolysis reaction by accumulation of fatty acids in the reaction mixture.