Hydrolysis of lactose by immobilized microorganisms.

Cells of Lactobacillus bulgaricus, Escherichia coli, and Kluyveromyces (Saccharomyces) lactis immobilized in polyacrylamide gel beads retained 27 to 61% of the beta-galactosidase activity of intact cells. Optimum temperature and pH and thermostability of these microbial beta-galactosidases were negligibly affected by the immobilization. Km values of beta-galactosidase in immobilized cells of L. bulgaricus, E. coli, and K. lactis toward lactose were 4.2, 5.4, and 30 mM, respectively. Neither inhibition nor activation of beta-galactosidase in immobilized L. bulgaricus and E. coli appeared in the presence of galactose, but remarkable inhibition by galactose was detected in the case of the enzyme of immobilized K. lactis. Glucose inhibited noncompetitively the activity of three species of immobilized microbial cells. These kinetic properties were almost the same as those of free beta-galactosidase extracted from individual microorganisms. The activity of immobilized K. lactis was fairly stable during repeated runs, but those of E. coli and L. bulgaricus decreased gradually. These immobilized microbial cells, when introduced into skim milk, demonstrated high activity for converting lactose to monosaccharides. The flavor of skim milk was hardly affected by treatment with these immobilized cells, although the degree of sweetness was raised considerably.     

Hydrolysis of milk lactose by immobilized beta-galactosidase-hen egg white powder

Immobilized beta-galactosidase was obtained by crosslinking the enzyme with hen egg white using 2% glutaraldehyde. The gel obtained could be lyophilized to give a dry enzyme powder. The pH optimum of both the soluble and immobilized enzyme was found to be 6.8. The immobilized enzyme showed a higher K(m) for the substrates. The extent of enzyme inhibition by galactose was reduced upon immobilization. The stability towards inactivation by heat, urea, gamma irradiation, and protease treatment were enhanced. The bound enzyme as tested in a batch reactor could be used repeatedly for the hydrolysis of milk lactose. The possible application of this system for small-scale domestic use has been suggested.     

Hydrolysis of lactose in skim milk by immobilized beta-galactosidase (bacillus circulans)

A novel chemical reactor, consisting of beta-galactosidase from Bacillus circulans immobilized onto a ribbed membrane made from polyvinylchloride and silica, was used to hydrolyze the lactose constituent of skim milk. Multiresponse nonlinear regression methods were employed to determine the kinetic parameters of rate expressions based on a proposed enzymatic mechanism that includes the formation of oligosaccharides. High-performance liquid chromatography (HPLC) methods were employed to monitor the concentrations of all species present in the effluent stream. For the experimental conditions used in this research, rate expressions which include the formation of trisaccharides, the inhibition effects of both the alpha and beta anomers of galactose, and the corresponding mutarotation reaction are sufficient to model the reaction network.     

Hydrolysis of lactose in skim milk by immobilized beta-galactosidase in a spiral flow reactor

beta-galactosidase from Aspergillus Oryzae immobilized in a spiral flow reactor was used to effect the hydrolysis of the lactose component of skim milk. Residence time distribution measurements were used to assess the amount of longitudinal dispersion occurring as a consequence of the spiral flow pattern and the semiporous nature of the polymeric material used to construct the spiral. It was possible to model the flow conditions as tubular flow with a Peclet number that was a linear function of the reactor space time. Nonlinear regression methods were used to determine the kinetic parameters of three proposed enzymatic rate expressions. The best fit of the data was obtained using a rate expression containing separate terms for competitive inhibition of the reaction by both the a and beta anomers of galactose. This kinetic model also incorporates the kinetics of the mutarotation between these forms. At 30 degrees C and a space time of 7 minutes, 80% of the lactose present in skim milk can be converted to glucose and galactose.     

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.     

Recovery of uranium by immobilized microorganisms

Summary Some attempts were made to recover uranium from sea and fresh water using immobilized Streptomyces viridochromogenes and Chlorella regularis cells. The cells immobilized in polyacrylamide gel have the most favorable features for uranium recovery; high adsorption ability, good mechanical properties, and applicability in a column system. The adsorption of uranium by the immobilized cells is not affected by the pH values between 4 and 9. These results show that uranium adsorption becomes independent of pH after immobilization. The amounts of uranium adsorbed by the immobilized cells increased linearly with temperature, suggesting that the adsorption of uranium by the immobilized cells is an endothermic reaction. The immobilized cells can recover uranium almost quantitatively from both fresh and sea water containing uranium, and almost all uranium adsorbed is desorbed with a solution of Na₂CO₃. Thus the immobilized cells of Streptomyces and Chlorella can be used repeatedly in adsorption-desorption process.Studies on the Accumulation of Heavy Metal Elements in Biological Systems. XXI     

Green biosynthesis of floxuridine by immobilized microorganisms

This work describes an efficient, simple, and green bioprocess for obtaining 5-halogenated pyrimidine nucleosides from thymidine by transglycosylation using whole cells. Biosynthesis of 5-fluoro-2'-deoxyuridine (floxuridine) was achieved by free and immobilized Aeromonas salmonicida ATCC 27013 with an 80% and 65% conversion occurring in 1 h, respectively. The immobilized biocatalyst was stable for more than 4 months in storage conditions (4 °C) and could be reused at least 30 times without loss of its activity. This microorganism was able to biosynthesize 2.0 mg L(-1) min(-1) (60%) of 5-chloro-2'-deoxyuridine in 3 h. These halogenated pyrimidine 2'-deoxynucleosides are used as antitumoral agents.     

Hydrolysis of lactose in whey permeate by immobilized β-galactosidase from Kluyveromyces fragilis

Neutral β-galactosidase from Kluyveromyces fragilis was immobilized on silanized porous glass modified by glutaraldehyde binding, with retention of more than 90% of its activity. Marked shifts in optimum pH (from 7.0 to 6.0) and temperature (from 35°C to 50°C) of the solid-phase enzyme were observed together with high catalytic activity and reasonable stability at wider pH and temperature ranges than those of the free enzyme. Highly efficient lactose saccharification (86–90%) in whey permeate was achieved both in a batch process and in a recycling packed-bed bioreactor.     

Increased H2 production by immobilized microorganisms

Viable cells of H₂-producers (Bacillus licheniformis and a mixed microbial culture) were immobilized on brick dust and in calcium alginate beads. In batch culture, cells of the mixed culture in the free state yielded 8.2 l H₂/mol glucose utilized, whereasB. licheniformis evolved 13.1 l H₂. Immobilized cells, however, gave 4-fold more H₂ than the free bacteria. Highest yields were from the cells immobilized on brick dust. High H₂-production rates continued over two rounds of re-use of the immobilized cells.A. Kumar, S.R. Jain and A.P. Joshi were and V. C. Kalia is with the Centre for Biochemical Technology (CSIR), University Campus, Mall Road, Delhi-110 007, India; C.B. Sharma is with the Department of Biosciences and Biotechnology, University of Roorkee, Roorkee-247 667, India. A. Kumar is now with the Biochemistry Laboratory, Department of Chemistry, Indian Institute of Technology, New Delhi-110 016, India, S.R. Jain is now with the Centre for Biomedical Engineering, Indian Institute of Technology, New Delhi-110 016, India, and A.P. Joshi is now with the Chemical Engineering Division, National Chemical Laboratory, Pune-411 008, India.     

Ethanol production from pentoses by immobilized microorganisms

The capabilities of immobilized Fusarium oxysporum f. sp. lini, Mucor sp., and Saccharomyces cerevisiae in fermenting pentose to ethanol have been compared. S. cerevisiae was found to have the best fermentation rate on d-xylulose of 0.3 g l^?1 h^?1. By using a separate isomerase column for converting d-xylose to d-xylulose and a yeast column for converting d-xylulose to ethanol, an ethanol concentration of 32 g l^?1 was obtained from 10% d-xylose. The ethanol yield was calculated to be 64% of the theoretical yield.     

竹炭固定化微生物对水中壬基酚的降解效率

竹炭是一种优质生物质炭,不仅比表面积大,孔隙发达,而且机械强度高,是微生物固定化载体的最佳选择之一.本文采用正交试验确定了竹炭固定化微生物的最佳制备条件,对比了竹炭固定菌和游离菌对水中类雌激素壬基酚的降解效果,并考察了竹炭固定菌的重复利用性.结果表明:固定化后降解菌大量地附着在竹炭表面及内部孔隙中,其最佳制备条件为温度30℃、pH=7、竹炭粒径35目.壬基酚的降解符合一级动力学方程,在不同的壬基酚初始浓度下(30、50、80、100 mg·L^-1),竹炭固定菌对壬基酚的7 d降解率分别为100%、75.3%、67.3%和78.7%,显著优于游离菌(54.2%、51.5%、30.6%和23.5%).经过8轮重复利用后,竹炭固定菌对壬基酚的降解率仍可达到36.5%,而此时游离菌的降解率仅为8.9%,说明竹炭固定菌具有长期可重复利用性,在去除废水有机污染物中具有较好的工程应用前景.     

Production of galacto-oligosaccharides from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth.

The production of galacto-oligosaccharides (GOS) from lactose by A. oryzae beta-galactosidase immobilized on cotton cloth was studied. The total amounts and types of GOS produced were mainly affected by the initial lactose concentration in the reaction media. In general, more and larger GOS can be produced with higher initial lactose concentrations. A maximum GOS production of 27% (w/w) of initial lactose was achieved at 50% lactose conversion with 500 g/L of initial lactose concentration. Tri-saccharides were the major types of GOS formed, accounting for more than 70% of the total GOS produced in the reactions. Temperature and pH affected the reaction rate, but did not result in any changes in GOS formation. The presence of galactose and glucose at the concentrations encountered near maximum GOS greatly inhibited the reactions and reduced GOS yield by as much as 15%. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme, suggesting no diffusion limitation in the enzyme carrier. The thermal stability of the enzyme increased approximately 25-fold upon immobilization on cotton cloth. The half-life for the immobilized enzyme on cotton cloth was more than 1 year at 40 degrees C and 48 days at 50 degrees C. Stable, continuous operation in a plugflow reactor was demonstrated for 2 weeks without any apparent problem. A maximum GOS production of 21 and 26% (w/w) of total sugars was attained with a feed solution containing 200 and 400 g/L of lactose, respectively, at pH 4.5 and 40 degrees C. The corresponding reactor productivities were 80 and 106 g/L/h, respectively, which are at least several-fold higher than those previously reported.     

Multistep reactions with immobilized microorganisms

This review presents some examples of new semicontinuous and continuous processes for product formation and for degradation of xenobiotics with immobilized microorganisms. A semicontinuous process for glycerol formation with Saccharomyces cerevisiae cells, adsorbed on sintered glass, and a continuous production of citric acid with Aspergillus niger, entrapped in calcium alginate, are given as examples of the production of primary metabolites. The production of ergot alkaloids with entrapped Claviceps purpurea demonstrates the possibilities of production of secondary metabolites. The continuous degradation of phenolic substances and that of 4-chlorophenol by entrapped and adsorbed microorganisms are given as examples of the possibility of a continuous degradation of xenobiotics by immobilized microorganisms. The continuous degradation of these substances was successful not only in artificial solutions but also in sterile and nonsterile wastewater.     

Hydrolysis of soyabean by papain immobilized on wood by radiation polymerization

Summary Papain was immobilized on wood chips by radiation polymerization without substantial loss of enzyme activity. The immobilized papain was used to hydrolyse soyabean meal and found to be stable upto 6 cycles of operation. Maximum hydrolysis occurred with 15% (W/V) immobilized matrix.