Stabilization of a raw-starch-digesting amylase by multipoint covalent attachment on glutaraldehyde-activated amberlite beads

Raw-starch-digesting enzyme (RSDA) was immobilized on Amberlite beads by conjugation of glutaraldehyde/ polyglutaraldehyde (PG)-activated beads or by crosslinking. The effect of immobilization on enzyme stability and catalytic efficiency was evaluated. Immobilization conditions greatly influenced the immobilization efficiency. Optimum pH values shifted from pH 5 to 6 for spontaneous crosslinking and sequential crosslinking, to pH 6-8 for RSDA covalently attached on polyglutaraldehyde-activated Amberlite beads, and to pH 7 for RSDA on glutaraldehyde-activated Amberlite. RSDA on glutaraldehyde-activated Amberlite beads had no loss of activity after 2 h storage at pH 9; enzyme on PG-activated beads lost 9%, whereas soluble enzyme lost 65% of its initial activity. Soluble enzyme lost 50% initial activity after 3 h incubation at 60 degrees C, whereas glutaraldehyde-activated derivative lost only 7.7% initial activity. RSDA derivatives retained over 90% activity after 10 batch reuse at 40 degrees C. The apparent Km of the enzyme reduced from 0.35 mg/ml to 0.32 mg/ml for RSDA on glutaraldehyde-activated RSDA but increased to 0.42 mg/ml for the PG-activated RSDA derivative. Covalent immobilization on glutaraldehyde Amberlite beads was most stable and promises to address the instability and contamination issues that impede the industrial use of RSDAs. Moreover, the cheap, porous, and non-toxic nature of Amberlite, ease of immobilization, and high yield make it more interesting for the immobilization of this enzyme.     

Adsorption of peroxidase on Celite 545 directly from ammonium sulfate fractionated white radish (Raphanus sativus) proteins

This paper demonstrates the direct immobilization of peroxidase from ammonium sulfate fractionated white radish proteins on an inorganic support, Celite 545. The adsorbed peroxidase was crosslinked by using glutaraldehyde. The activity yield for white radish peroxidase was adsorbed on Celite 545 was 70% and this activity was decreased and remained 60% of the initial activity after crosslinking by glutaraldehyde. The pH and temperature-optima for both soluble and immobilized peroxidase was at pH 5.5 and 40°C. Immobilized peroxidase retained higher stability against heat and water-miscible organic solvents. In the presence of 5.0 mM mercuric chloride, immobilized white radish peroxidase retained 41% of its initial activity while the free enzyme lost 93% activity. Soluble enzyme lost 61% of its initial activity while immobilized peroxidase retained 86% of the original activity when exposed to 0.02 mM sodium azide for 1 h. The K_m values were 0.056 and 0.07 mM for free and immobilized enzyme, respectively. Immobilized white radish peroxidase exhibited lower V_max as compared to the soluble enzyme. Immobilized peroxidase preparation showed better storage stability as compared to its soluble counterpart.     

环氧交联剂和氨基载体固定化海洋假丝酵母脂肪酶*

游离酶经过固定化后,稳定性和环境耐受性得到提高,在食品、医药、化工、环境和皮革等领域可以很好的提高酶的利用率并降低生产成本,具有极大的应用潜力。新型交联剂在固定化酶工艺的应用极大推进了固定化酶研究的深入。借助新型交联剂聚乙二醇二缩水甘油醚(PEGDGE),利用氨基载体LX-1000HA固定化海洋假丝酵母脂肪酶,结合单因素和正交试验优化得到交联及固定化条件为:交联温度30℃,交联2h,交联剂浓度0.75%,pH7.0,加酶量800U,载体量0.5g,固定化2h,固定化温度45℃。根据上述最佳固定化工艺,制备得到固定化酶LX-1000HA-PEGDGE-CRL在最适条件下测得酶活达到160.81U/g,约为此前制备的固定化酶LX-1000HA-GA-CRL(由LX-1000HA和戊二醛交联脂肪酶得到)和LX-1000EA-PEGDGE-CRL(由短链氨基载体LX-1000EA和PEGDGE交联脂肪酶得到)酶活的2倍,发现固定化酶LX-1000HA-PEGDGE-CRL的最适反应温度相比于游离酶提高15℃;在70℃的环境中3h后酶活仍存留70%;循环使用6次后残留65%左右的酶活;酸碱耐受性和储存稳定性也表现良好,4℃保存30天后剩余约70%的初始酶活。同时,将制备的固定化酶LX-1000HA-PEGDGE-CRL与游离酶、固定化酶LX-1000HA-GA-CRL、固定化酶LX-1000EA-PEGDGE-CRL进行了比较,发现固定化酶LX-1000HA-PEGDGE-CRL在温度耐受性和重复使用性等方面具有更好的使用效果。     

Glutaraldehyde crosslinking analysis of the C12E8 solubilized H,K-ATPase

A soluble porcine H,K-ATPase preparation was obtained with the nonionic detergent, C12E8. ATP hydrolysis by the soluble H,K-ATPase was stimulated with respect to the native preparation at pH 6.1, while the K(+)-phosphatase activity was comparable to the native enzyme. The soluble enzyme demonstrated characteristic ligand-dependent effects on ATP hydrolysis, including ATP activation of K(+)-stimulated hydrolysis with a K0.5 of 28 +/- 4 microM ATP, and inhibition with an IC50 of 2.1 mM ATP. The activation and inhibition of ATP hydrolysis by K+ was also observed with a K0.5 for activation of 2.8 +/- 0.4 mM KCl at 2.0 mM ATP (pH 6.1) and inhibition with an IC50 of 135 mM KCl at 0.05 mM ATP. 2-Methyl-8-(phenylmethoxy)imidazo[1,2a]pyridine-3-acetonitrile (SCH 28080), a specific inhibitor of the native H,K-ATPase, competitively inhibited the K(+)-stimulated activity with a Ki of 0.035 microM. The soluble enzyme was stable with a t0.5 for ATPase activity of 6 h between 4 and 11 degrees C. The demonstration of these related ligand responses in the catalytic reactions of the soluble preparation indicates that it is an appropriate medium for investigation of the subunit associations of the functional H,K-ATPase. Subunit associations of the active soluble enzyme were assessed following treatment with the crosslinking reagent, glutaraldehyde. The distribution of crosslinked particles was independent of the soluble protein concentration in the crosslinking buffer within the protein range 0.3 to 2.0 mg/ml or the detergent to protein ratio varied from 1 to 15 (w/w). The crosslinked pattern was unaffected by the presence or absence of K during crosslinking or nucleotide concentration. These observations suggest that crosslinking occurs in associated subunits that do not undergo rapid associations dependent upon enzyme turnover. Phosphorylation of the soluble enzyme with 0.1 mM MgATP produced a phosphoprotein at 94 kDa. A phosphoprotein obtained after glutaraldehyde treatment exhibited identical electrophoretic mobility to the crosslinked particle identified by silver stain. Glutaraldehyde treatment of soluble protein fractions resolved on a linear 10-35% glycerol gradient revealed several smaller peptides partially resolved from the crosslinked pump particle, but no active fraction enriched in the monomeric H,K-ATPase. This data indicates that the functional porcine gastric H,K-ATPase is organized as a structural dimer.     

Calcium alginate entrapped preparations of Aspergillus oryzae beta galactosidase: its stability and applications in the hydrolysis of lactose

Insoluble concanavalin A-beta galactosidase complex was obtained by using jack bean extract and this complex was crosslinked with glutaraldehyde, in order to maintain the integrity of complex in the presence of its substrate or products. Concanavalin A-beta galactosidase complex retained 92% of the initial enzyme activity whereas crosslinked complex showed 88% activity. Entrapment of concanavalin A-beta galactosidase complex into calcium alginate beads provided suitability to use this preparation in reactors. Temperature- and pH-optima of the various immobilized beta galactosidase preparations were the same as its soluble counterpart. Entrapped crosslinked concanavalin A-beta galactosidase complex retained more than 50% activity after 1h exposure with 4.0 M urea at room temperature. Moreover, entrapped crosslinked concanavalin A-beta galactosidase complex retained 81 and 62% of the original enzymatic activity in the presence of 5% calcium chloride and 5% galactose, respectively. Entrapped crosslinked concanavalin A-beta galactosidase complex preparation was more superior in the continuous hydrolysis of lactose in a batch process as compared to the other entrapped preparations. This entrapped crosslinked concanavalin A-beta galactosidase complex retained 95% activity after seventh repeated use and 93% of its original activity even after 2 months storage at 4 degrees C.     

Immobilization of urease on vermiculite

Urease (EC 3.5.1.5) of high activity was obtained when the enzyme was immobilized on vermiculite crosslinked with 2.5% glutaraldehyde in chilled EDTA-phosphate buffer (pH 5.5). The highest activity of the immobilized enzyme was at 65°C and pH 6.5 while the optimum temperature for free urease was found to be 25°C. The thermal stability of immobilized urease was observed to be much better than that of the free urease. When stored at 4°C, urease immobilized on vermiculite retained 69 to 81% of its activity after 60 days and 61 to 75% of its original activity was retained after 4 repeated uses.     

Enzymatic properties of immobilized Alcaligenes faecalis cells with cell-associated beta-glucosidase activity

Enzymatic properties of Alcaligenes faecalis cells immobilized in polyacrylamide were characterized and compared with those reported for the extracted enzyme, and with those measured for free cells. Many of the properties reflected those of the extracted enzyme rather than those measured in the free whole cells prior to immobilization, suggesting cell disruption during immobilization. These properties included the pH activity profile, a slightly broader pH stability profile, and the activation energy. Electron micrographs showed evidence of cell debris among the polymer matrix. The immobilized cells were not viable, and did not consume glucose. Thermal stability was less after immobilization with a half-life of 16 h at 45 degrees C, and 3.5 h at 50 degrees C. The immobilized preparation was more stable when stored lyophilized rather than in buffer, losing 23 and 52% activity, respectively, after six months. The enzyme was irreversibly inhibited by both acetate and citrate buffers. If the immobilized enzyme is to be used in conjunction with cellulases from Trichoderma reesei for cellulase saccharification, the optimal conditions would be pH 5.5 and 45 degrees C in a buffer containing no carboxylic acid groups.     

Immobilization of β-glucosidase from Scytalidium lignicola on Chitosan

Chitosan was found to be a better support than alginate beads for immobilization of β-glucosidase from Scytalidium lignicola. The optimum concentration of glutaraldehyde for enzyme immobilization was 0.2%. Immobolized β-glucosidase was more able in the pH range of 3–6. Immobilized β-glucosidase retained about 70% of its activity at 50%C after 72 h of incubation while free enzyme lost most of its activity. The log of activity retained vs time was a straight line with free enzyme but was curved for immnobilized enzyme. Lineweaver-Burk plots of free and immoblized β-glucosidase gave K_m values of 2 × 10⁻⁴ M and 5.5 × 10⁻⁴ M for p-nitrophenyl β-d-glucopyranoside, respectively. Addition of immobilized β-glucosidase to a saccharification system gave a 30% increase in reducing sugar availability compared to free enzyme addition and was at least 4 times reusable without appreciable loss in enzyme activity.     

Thermostable, alkalophilic and cellulase free xylanase production by Thermoactinomyces thalophilus subgroup C

Thermoactinomyces thalophilus produced cellulase free extracellular endo-1,4-beta-xylanase (EC 3.2.1.8) at 50 degrees C and pH 8.5. Maximum xylanase production was achieved in fermentation medium using birchwood xylan as substrate after 96 h of growth at 50 degrees C. Other agricultural substrates such as wheat bran, wheat straw, sugarcane bagasse and cornstover produced less xylanase. The crude enzyme preparation from mutant T. thalophilus P2 grown under optimised fermentation conditions showed no cellulase contamination and maximum xylanase activity of 42 U/ml at 65%deg;C and pH 8.5-9.0. This enzyme with initial xylanase activity of 42 U/ml was found thermostable up to 65 degrees C and retaining 50% of its activity after its incubation for 125 min at 65 degrees C.     

Calcium alginate entrapped preparation of α-galactosidase: its stability and application in hydrolysis of soymilk galactooligosaccharides

Thermostable α-galactosidase from Aspergillus terreus _GR was insolubilized using concanavalin A obtained from jack bean extract and in order to maintain the integrity of complex in the presence of its substrate or products, this complex was crosslinked with glutaraldehyde. Soluble α-galactosidase entrapped in calcium alginate retained 82% of enzyme activity whereas, Con A-α-galactosidase complex entrapped in calcium alginate and crosslinked Con A-α-galactosidase complex entrapped calcium alginate retained 74 and 61% activity, respectively. A fluidized bed reactor was constructed for continuous hydrolysis of galactooligosaccharides in soymilk using crosslinked Con A-α-galactosidase complex entrapped calcium alginate. Optimum conditions such as pH (5.0) and temperature (65°C) were the same for all immobilized enzyme preparations and soluble enzyme. Crosslinked Con A-α-galactosidase entrapped complex exhibited enhanced thermostability and showed 62% of activity (38%) after 360 min at 65°C. Entrapped crosslinked Con A-α-galactosidase complex preparation was superior in the continuous hydrolysis of oligosaccharides in soymilk by batch processes compared to the other entrapped preparations. The entrapped crosslinked concanavalin A-α-galactosidase complex retained 95% activity after eight cycles of use.     

Hydrolysis of lactose in whey permeate by immobilized β-galactosidase from Penicillium notatum

A new low-cost β-galactosidase (lactase) preparation for whey permeate saccharification was developed and characterized. A biocatalyst with a lactase activity of 10 U/mg, a low transgalactosylase activity and a protein content of 0.22 mg protein/mg was obtained from a fermenter culture of the fungus Penicillium notatum. Factors influencing the enzymatic hydrolysis of lactose, such as reaction time, pH, temperature and enzyme and substrate concentration were standardized to maximize sugar yield from whey permeate. Thus, a 98.1% conversion of 5% lactose in whey permeate to sweet (glucose-galactose) syrup was reached in 48 h using 650 β-galactosidase units/g hydrolyzed substrate. After the immobilization of the acid β-galactosidase from Penicillium notatum on silanized porous glass modified by glutaraldehyde binding, more than 90% of the activity was retained. The marked shifts in the pH value (from 4.0 to 5.0) and optimum temperatures (from 50°C to 60°C) of the solid-phase enzyme were observed and discussed. The immobilized preparation showed high catalytic activity and stability at wider pH and temperature ranges than those of the free enzyme, and under the best operating conditions (lactose, 5%; β-galactosidase, 610–650 U/g lactose; pH 5.0; temperature 55°C), a high efficiency of lactose saccharification (84–88%) in whey permeate was achieved when lactolysis was performed both in a batch process and in a recycling packed-bed bioreactor. It seems that the promising results obtained during the assays performed on a laboratory scale make this immobilizate a new and very viable preparation of β-galactosidase for application in the processing of whey and whey permeates.     

Effect of immobilization on stability and kinetic properties of alpha-L-fucosidase from Turbo cornutus

An amount of alpha-L-fucosidase from T. cornutus liver was copolymerized with glutaraldehyde using bovine serum albumin as the carrier protein. The properties of the native, the soluble enzyme polymer complex, and the insoluble enzyme polymer complex were studied and compared under various conditions of pH, temperature, substrate, and inhibitor concentration. Native alpha-L-fucosidase was heat labile and lost more than 85% of its activity when incubated at 55 degrees C for 5 min. In contrast, under equivalent incubation conditions, both the soluble and the insoluble enzyme polymer complexes exhibited enhanced resistance to thermal inactivation and after 5 min lost only 65 and 40% of their original activity, respectively. Polymerzation also resulted in the shift of pH optima towards the acidic range, a decrease in activation energy and a change in the apparent K(m) values towards the p-nitrophenyl-alpha-L-fucopyranoside substrate.     

漆酶在磁性壳聚糖微球上的固定及其酶学性质研究

以磁性壳聚糖微球为载体,戊二醛为交联剂,共价结合制备固定化漆酶。探讨了漆酶固定化的影响因素,并对固定化漆酶的性质进行了研究。确定漆酶固定化适宜条件为：50 mg磁性壳聚糖微球,加入10mL 0.8mg/mL 漆酶磷酸盐缓冲液（0.1mol/L,pH 7.0）,在4℃固定2h。固定化酶最适pH为3.0, 最适温度分别为10℃和55℃,均比游离酶降低5℃。在pH 3.0,温度37℃时,固定化酶对ABTS的表观米氏常数为171.1μmol/L。与游离酶相比,该固定化漆酶热稳定性明显提高,并具有良好的操作和存储稳定性。     

In vitro and in vivo enzyme studies of polyhemoglobin-tyrosinase

Melanoma is now the fifth most common type of cancer in North America. At present, there is no optimal treatment for this cancer. However, the lowering of the tyrosine level can inhibit the growth of melanoma. Unfortunately, this diet restriction cannot be humanly tolerated and causes vomiting, nausea, and severe body weight loss. To prevent these problems, we are studying a new approach involving the preparation intermolecularly crosslinked hemoglobin and tyrosinase for intravenous injection. In this article we describe the method of preparation and the structural and functional properties of polyhemoglobin-tyrosinase. We evaluate the effects of varying glutaraldehyde ratio, crosslinking time, and enzyme concentration on the enzyme activity of polyhemoglobin-tyrosinase. We also optimize the molecular weight distribution of polyhemoglobin-tyrosinase. The stability of polyhemoglobin-tyrosinase at 37 degrees C is much more stable when compared to noncrosslinked tyrosinase solution. Animal studies show that a higher degree of polymerization correlates with a longer circulation time of polyhemoglobin-tyrosinase, and the optimal crosslinking time is 24 hours. One intravenous injection of polyhemoglobin-tyrosinase lowers the plasma tyrosine to about 10% of its original level within one hour.     

Immobilization of Kluyveromyces marxianus cells containing inulinase activity in open pore gelatin matrix: 1. Preparation and enzymatic properties

Kluyveromyces marxianus cells with inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) activity have been immobilized in open pore gelatin pellets with retention of > 90% of the original activity. The open pore gelatin pellets with entrapped yeast cells were obtained by selective leaching out of calcium alginate from the composite matrix, followed by crosslinking with glutaraldehyde. Enzymatic properties of the gelatin-entrapped cells were studied and compared with those of the free cells. The immobilization procedure did not alter the optimum pH of the enzymatic preparation; the optimum for both free and immobilized cells was pH 6.0. The optimum temperature of inulin hydrolysis was 10°C higher for immobilized cells. Activation energies for the reaction with the free and immobilized cells were calculated to be 6.35 and 2.26 kcal mol^?1, respectively. K_m values were 8 mM inulin for the free cells and 9.52 mM for the immobilized cells. The thermal stability of the enzyme was improved by immobilization. Free and immobilized cells showed fairly stable activities between pH 4 and 7, but free cell inulinase was more labile at pH values below 4 and above 7 compared to the immobilized form. There was no loss of enzyme activity of the immobilized cells on storage at 4°C for 30 days. Over the same period at room temperature only 6% of the original activity was lost.     

Immobilization of permeabilized whole cell penicillin G acylase from Alcaligenes faecalis using pore matrix crosslinked with glutaraldehyde

The activity of penicillin G acylase from Alcaligenes faecalis increased 7.5-fold when cells were permeabilized with 0.3% (w/v) CTAB. The treated cells were entrapped by polyvinyl alcohol crosslinked with boric acid, and crosslinked with 2% (v/v) glutaraldehyde to increase the stability. The conversion yield of penicillin G to 6-aminopenicillanic acid was 75% by immobilized system in batch reaction. No activity was lost after 15 cycles and about 65% enzyme activity was retained at the end of the 31th cycle.     

Preparation of cross-linked enzyme aggregates by using bovine serum albumin as a proteic feeder

Addition of bovine serum albumin (BSA) as a proteic feeder facilitates obtaining cross-linked enzyme aggregates (CLEAs) in cases where the protein concentration in the enzyme preparation is low and/or the enzyme activity is vulnerable to the high concentration of glutaraldehyde required to obtain aggregates. CLEAs of Pseudomonas cepacia lipase and penicillin acylase were prepared. CLEA of lipase prepared in the presence of BSA retained 100% activity whereas CLEA prepared without BSA retained only 0.4% activity of the starting enzyme preparation. Lipase CLEA showed 12-fold increase in activity over free enzyme powder when the CLEA was used in transesterification of tributyrin. For the transesterification of Jatropha oil, while free enzyme powder required 8 h and 50 mg lipase to obtain 77% conversion, CLEA required only 6 h and 6.25 mg lipase to obtain 90% conversion. In the case of penicillin acylase, 86% activity could be retained in CLEA prepared with BSA whereas CLEA made without BSA retained only 50% activity. CLEA prepared without BSA lost 20% activity after 8 h at 45 degrees C whereas CLEA with BSA retained full activity. CLEA prepared with BSA showed Vmax/Km of 36.3 min-1 whereas CLEA prepared without BSA had Vmax/Km of 17.4 min-1 only. Scanning electron microscopy analysis showed that CLEAs prepared in the presence of BSA were less amorphous and closer in morphology to CLEAs of other enzymes described in the literature.     

Crosslinked enzyme crystals of glucoamylase as a potent catalyst for biotransformations

Glucoamylase (E.C: 3.2.1.3, alpha-(1-->4)-glucan glucohydrolase) mainly hydrolyzes starch and has been extensively used in the starch, glucose (dextrose), and fermentation industries. Immobilized glucoamylase has an inherent disadvantage of lower conversion rates and low thermostability of less than 55 degrees C when used in continuous operations. We have developed crosslinked enzyme crystals (CLEC) of glucoamylase that overcome the above disadvantages, possess good thermal stability and retain 98.6% of their original activity at 70 degrees C for 1h, 77% activity at 80 degrees C for 1h, and 51.4% activity at 90 degrees C for 0.5h. CLEC glucoamylase has a specific activity of 0.0687 IU/mg and a yield of 50.7% of the original activity of the enzyme under optimum conditions with starch as the substrate. The crystals obtained are rhombohedral in shape having a size approximately 10-100 microm, a density of 1.8926 g/cm(3) and a surface area of 0.7867 m(2)/g. The pH optimum of the glucoamylase crystals was sharp at pH 4.5, unlike the soluble enzyme. The kinetic constants V(max) and K(m) exhibited a 10-fold increase as a consequence of crystallization and crosslinking. The continuous production of glucose from 10% soluble starch and 10% maltodextrin (12.5 DE) by a packed-bed reactor at 60 degrees C had a productivity of 110.58 g/L/h at a residence time of 7.6 min and 714.1g/L/h at a residence time of 3.4 min, respectively. The CLEC glucoamylase had a half-life of 10h with 4% starch substrate at 60 degrees C.     

Immobilization of catalases from Bacillus SF on alumina for the treatment of textile bleaching effluents

A catalase preparation from a newly isolated Bacillus sp. was covalently immobilized on silanized alumina using glutaraldehyde as crosslinking agent. The effect of the coupling time of the enzyme-support reaction was determined in terms of protein recovery and immobilization yield and a certain balance point was found after which the activity recovery decreased. The activity profile of the immobilized catalase at high pH and temperature was investigated. The immobilized enzyme showed higher stabilities (214 h at pH 11, 30°C) at alkaline pH than the free enzyme (10 h at pH 11, 30°C). The immobilized catalase was inhibited by anionic stabilizers or surfactants added to the hydrogen peroxide substrate solution.     

1,3‐Regiospecific ethanolysis of soybean oil catalyzed by crosslinked porcine pancreas lipase aggregates

The preparation of crosslinked aggregates of pancreatic porcine lipase (PPL‐CLEA) was systematically studied, evaluating the influence of three precipitants and two crosslinking agents, as well as the use of soy protein as an alternative feeder protein on the catalytic properties and stability of the immobilized PPL. Standard CLEAs showed a global yield (CLEA’ observed activity/offered total activity) of less than 4%, whereas with the addition of soy protein (PPL:soy protein mass ratio of 1:3) the global yield was approximately fivefold higher. The CLEA of PPL prepared with soy protein as feeder (PPL:soy protein mass ratio of 1:3) and glutaraldehyde as crosslinking reagent (10 μmol of aldehyde groups/mg of total protein) was more active mainly because of the reduced enzyme leaching in the washing step. This CLEA, named PPL‐SOY‐CLEA, had an immobilization yield around 60% and an expressed activity around 40%. In the ethanolysis of soybean oil, the PPL‐SOY‐CLEA yielded maximum fatty acid ethyl ester (FAEE) concentration around 12‐fold higher than that achieved using soluble PPL (34 h reaction at 30°C, 300 rpm stirring, soybean oil/ethanol molar ratio of 1:5) with an enzyme load around 2‐fold lower (very likely due to free enzyme inactivation). The operational stability of the PPL‐SOY‐CLEA in the ethanolysis of soybean oil in a vortex flow type reactor showed that FAEE yield was higher than 50% during ten reaction cycles of 24 h. This reactor configuration may be an attractive alternative to the conventional stirred reactors for biotransformations in industrial plants using carrier‐free biocatalysts. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:910–920, 2018