Continuous production of oxytetracycline by immobilized growing Streptomyces rimosus cells

Summary Streptomyces rimosus cells were immobilized with urethane prepolymers and used in the production of oxytetracycline. Based on the criteria for oxytetracycline productivity, cell growth in gels, cell leakage from gels and mechanical strength of gel, a hydrophilic prepolymer, PU-1, the main chain of which was polyethylene glycol (molecular weight, approximately 1500) was employed as gel material among 11 kinds of urethane prepolymers. Use of glucose-free medium for cultivation of PU-1-entrapped cells increased the production rate of oxytetracycline and minimized cell leakage from the gels. When the gel-entrapped cells lost activity, treatment of the cell-entrapping gels with saline or 70% ethanol resulted in recovery of the oxytetracycline productivity. Continuous oxytetracycline fermentation using PU-1-entrapped growing cells was successfully achieved in air-bubbled reactor for at least 35 days with reactivation of the cells.     

Effect of high-cell-density fermentation of Candida utilis on kinetic parameters and the shift to respiro-fermentative metabolism

In this study, biodesulfurization (BDS) was carried out using immobilized Rhodococcus erythropolis KA2-5-1 in n-tetradecane containing dibenzothiophene (DBT) as a model oil (n-tetradecane/immobilized cell biphasic system). The cells were immobilized by entrapping them with calcium alginate, agar, photo-crosslinkable resin prepolymers (ENT-4000 and ENTP-4000), and urethane prepolymers (PU-3 and PU-6); and it was found that ENT-4000-immobilized cells had the highest DBT desulfurization activity in the model oil system without leakage of cells from the support. Furthermore, ENT4000-immobilized cells could catalyze BDS repeatedly in this system for more than 900 h with reactivation; and recovery of both the biocatalyst and the desulfurized model oil was easy. This study would give a solution to the problems in BDS, such as the troublesome process of recovering desulfurized oil and the short life of BDS biocatalysts.     

Entrapment of microbial cells and organelles with hydrophilic urethane prepolymers

Summary Microbial cells and cellular organelles were immobilized by mixing aqueous suspensions of the biocatalysts with water-miscible urethane prepolymers. Thus immobilized preparations of acetone-dried cells of Arthrobacter simplex and thawed cells of Nocardia rhodocrous showed appreciable {ie351-1} activities in the transformation of hydrocortisone into prednisolone and 4-androstene-3,17-dione to androst-1,4-diene-3,17-dione, respectively. The activities of catalase and alcohol oxidase were observed in the immobilized peroxisomes (microbodies) of a methanol-grown yeast Kloeckera sp. No. 2201. Yeast mitochondria entrapped with the prepolymer showed adenylate kinase activity. These results indicate the usefulness of the urethane prepolymers as convenient materials for entrapment of not only enzymes, but also organelles and microbial cells.     

Production of vitamin B12 by immobilized cells of a propionic acid bacterium

Summary The ability of immobilized cells of propionic acid bacteria to form vitamin B₁₂ has been investigated. Propionibacterium arl AKU 1251 having a considerable activity to produce the vitamin was selected as a test organism among six strains of propionic acid bacteria tested. The whole cells were entrapped with urethane prepolymers, photo-crosslinkable resin prepolymers or several other materials such as -carrageenan, agar or sodium alginate, and their vitamin B₁₂ productivity was compared. Based on the criteria of the convenience of preparation and the stability of the cell-entrapping gels, a hydrophilic urethane prepolymer, PU-9, was employed as gel material. Satisfactory vitamin B₁₂ production was obtained when 5–10 g of wet cells precultured to the late exponential growth phase were entrapped with 1 g of the prepolymer. Addition of a suitable amount of cobaltous ion and of 5,6-dimethyl benzimidazole to the culture medium was effective for the production of the vitamin by the immobilized cells. The repeated use of the immobilized cells was successfully achieved when a suitable amount of cells were entrapped and allowed the proliferation of cells inside gel matrices.     

Recent Advances in the use of Immobilized Lipases Directed Toward the Asymmetric Syntheses of Complex Molecules

Water-insoluble compounds can be substrates for enzymatic reactions when lipases are immobilized properly and suitable organic solvents are used. In this review, three type of lipase immobilization method and their application to the asymmetric syntheses of complex molecules are described. Lipases immobilized with Celite or synthetic prepolymers such as urethane prepolymer and photo-crosslinkable resin prepolymer have been applied for the kinetic resolution of many kinds of water-insoluble substrate.

Phospholipid-lipase aggregates with ether linkages are novel and have been found to function effectively as immobilized lipases in asymmetric hydrolysis or esterification reactions in water-saturated organic solvent. The phospholipid-lipase aggregates are considered to have a stacked bilayer based on X-ray diffraction analysis structure of the lipid in the crystalline phase.     

Improving immobilized biocatalysts by gel phase polymerization

A new method is presented for the treatment of gel-type supports, used for immobilizing microbial cells and enzymes, to obtain high mechanical strength. It is particularly useful for ethanol fermentation over gel beads containing immobilized viable cells, where the beads can be ruptured by gas production and the growth of cells within the gels. This method consists of treating agar or carrageenan gel with polyacrylamide to form a rigid support which retains the high catalytic activity characteristic of the untreated biocatalysts. The size and shape of the biocatalyst is unaffected by this treatment. The method involves the diffusion of acrylamide, N,N'-methylenebisacrylamide and beta-dimethylaminopropionitrile (or N,N,N',N'-tetramethyl-ethylenediamine) into the performed biocatalyst beads followed by the addition of an initiator to cause polymerization within the beads. Treated gels have been used for the continuous fermentation of glucose to ethanol in a packed column for over two months. During this operation, the gel beads maintained their rigidity, and the maximum productivity was as high as 50 g h(-1) L(-1) gel. There was no appreciable decay of cell activity.     

Synthesis and characterization of starch-modified polyurethane

Corn starch was reacted with urethane prepolymer in order to modifying starch and preparing new hydrophobic copolymers. These copolymers were prepared by two-step reactions. The polycaprolactone terminated hexamethylene diisocyanate (HDI) (as prepolymer) was prepared by introducing diisocyanate on both ends of PCL at a molar ratio of 1:2 (PCL:HDI). The grafting was performed by addition of polycaprolactone based prepolymer to starch solution of DMSO with different weight ratio of starch and prepolymer. The samples were characterized and examined by FTIR and ¹H NMR spectroscopy, DSC analysis, and scanning electron microscopy (SEM). By introducing NCO groups onto the PCL terminals, the FTIR spectrum shows a new sharp peak, representing the NCO groups and formation of prepolymer. By grafting this prepolymer onto starch a NH and urethane band were appeared. The effect of prepolymer percentage on hydrophobicity was measured through contact angle and it was found that increases with increasing amount of prepolymer. Glass transition temperature (T_g) is also affected with increasing amount of urethane linkages. Surface morphology of modified starch was studied by SEM. It was observed that the surfaces of modified starch are rougher and disordered than the surface of unmodified starch particles. This confirms the grafting and modification of starch. This modified starch can be used as filler in biodegradable starch based polymers.     

Bioconversion of lipophilic compounds by immobilized microbial cells in organic solvents

Microbial cells were gel-entrapped with photo-crosslinkable resin prepolymers or urethane prepolymers, respectively. The resulting gels have different tailor-made hydrophobic or hydrophilic character. They were used for successful bioconversion of hydrophobic steroids and terpenoids in watersaturated mixtures of organic solvents. The experiments show the influence of the hydrophobicity of the gels and the polarity of the solvent mixtures, respectively. Use of hydrophobic gels and less polar solvents is preferable for bioconversion of hydrophobic compounds. The selective formation of a desired product among diverse products from a single substrate by appropriate use of hydrophobic or hydrophilic gels is possible. In each case, tests should be made to select the appropriate gel and solvent mixture. Bioconversions tested are: dehydroepiandrosterone to 4-androstene-3,17-dione; cholesterol to cholestenone; β-sitosterol to β-sitostenone; stigmasterol to stigmastenone; pregnenolone to progesterone; testosterone to Δ¹-dehydrotestosterone or 4-androstene-3,17-dione, respectively; all with immobilized cells of Nocardia rhodocrous; and stereoselective hydrolysis of dl-menthyl-succinate to yield l-menthol with immobilized cells of Rhodotorula minuta var. texensis.     

Maximizing the stability of metabolic engineering‐derived whole‐cell biocatalysts

A systematic and powerful knowledge‐based framework exists for improving the activity and stability of chemical catalysts and for empowering the commercialization of respective processes. In contrast, corresponding biotechnological processes are still scarce and characterized by case‐by‐case development strategies. A systematic understanding of parameters affecting biocatalyst efficiency, that is, biocatalyst activity and stability, is essential for a rational generation of improved biocatalysts. Today, systematic approaches only exist for increasing the activity of whole‐cell biocatalysts. They are still largely missing for whole‐cell biocatalyst stability. In this review, we structure factors affecting biocatalyst stability and summarize existing, yet not completely exploited strategies to overcome respective limitations. The factors and mechanisms related to biocatalyst destabilization are discussed and demonstrated inter alia based on two case studies. The factors are similar for processes with different objectives regarding target molecule or metabolic pathway complexity and process scale, but are in turn highly interdependent. This review provides a systematic for the stabilization of whole‐cell biocatalysts. In combination with our knowledge on strategies to improve biocatalyst activity, this paves the way for the rational design of superior recombinant whole‐cell biocatalysts, which can then be employed in economically and ecologically competitive and sustainable bioprocesses.     

11α-Hydroxylation of progesterone by gel-entrapped living Rhizopus stolonifer mycelia

Summary Spores of Rhizopus stolonifer were immobilized aseptically by entrapment with photo-crosslinkable resin prepolymers, urethane prepolymers or several kinds of polysaccharides. The entrapped spores were allowed to germinate and develop in situ. The immobilized living mycelia so obtained were induced for the steroid 11-hydroxylation system and examined for their activity to hydroxylate progesterone at 11-position in a buffer system containing 2.5% of organic cosolvent. Of various water-miscible organic cosolvents, methanol was found to be most effective in terms of the activity of the entrapped mycelia and the solubility of the product, 11-hydroxyprogesterone. Though all the living mycelia entrapped in different gels exhibited the hydroxylation activity, mycelia entrapped in photo-crosslinked gels showed the maximum activity which was rather higher than that of the free mycelia. The net-work size of the photo-crosslinked resins, namely the chain length of the photo-crosslinkable resin prepolymers, affected markedly the mycelial growth in gels, and subsequently, the hydroxylation activity of the entrapped mycelia. Entrapment significantly enhanced the operational activity and stability of the 11-hydroxylation system in the mycelia, and permitted the intermittent reactivation of the system by incubating the entrapped mycelia in potato-dextrose broth.     

Application of immobilized lipase to regio-specific interesterification of triglyceride in organic solvent

Summary Lipase from Rhizopus delemar was immobilized by entrapment with photo-crosslinkable resin prepolymers or urethane prepolymers or by binding to various types of porous silica beads. The immobilized lipase preparations thus obtained were examined for their activity in converting olive oil to an interesterified fat (cacao butter-like fat), whose oleic acid moieties at 1- and 3-positions were replaced with stearic acid moieties, in the reaction solvent n-hexane. Although all of the immobilized preparations exhibited some activity, lipase adsorbed on Celite and then entrapped with a hydrophobic photo-crosslinkable resin prepolymer showed the highest activity, about 75% of that of lipase simply adsorbed onto Celite. Entrapment markedly enhanced the operational stability of lipase.Dedicated to Professor H. Holzer, Freiburg University, on his 60th birthday (June 13, 1981)     

Design of a nonuniformly distributed biocatalyst

The properties of a nonuniformly distributed biocatalyst, where the active enzymes are immobilized on the exterior or the interior portions o a solid support, are compared with those of a conventional biocatalyst which is uniformly distributed in a spherical geometry. To investigate the performance of nonuniformly distributed biocatalysts their effectiveness factors are computed and compared for six different enzyme distribution configurations: one-half core, one-half shell, one-third center space, one-third middle annulus, one-third outer shell, and the uniformly distributed. According to the results of numerical analysis, the biocatalyst performance of the exterior "shell" configuration is always far more effective for the immobilized enzymes with positive order reaction kinetics such as Michaelis-Menten and competitive product inhibition. However, in the case of negative order enzymatic reaction kinetics such as substrate inhibition, the interior "core" configuration of the biocatalyst can render far greater enzyme utilization efficiency.     

Immobilization of nitrifying bacteria in porous pellets of urethane gel for removal of ammonium nitrogen from waste-water

Summary The effects of immobilizing materials on the activity of nitrifying bacteria and removal of ammonium nitrogen (NH₄-N) from waste-water by immobilized nitrifying bacteria were investigated using six urethane prepolymers. With a urethane prepolymer containing 2.27% free isocyanate, a high activity yield of nitrifying bacteria was obtained. There was a drastic improvement over the conventional method of immobilization by acrylamide in the activity yield. Inorganic synthetic waste-water was treated at a high loading rate of 0.24 kg N·m^–3·day^–1. The NH₄-N concentration of the effluent could be reduced to 2 mg·1^–1 or less and the removal was 90%. The life of the pellets in terms of activity was at least 120 days. Offprint requests to: T. Sumino     

Preparation of L-aspartic acid by means of immobilized Alcaligenes metalcaligenes cells

Two types of biocatalysts based on immobilized cells of Alcaligenes metalcaligenes exhibiting aspartate ammonia-lyase activity (EC 4.3.1.1) were developed for the enzymic preparation of L-aspartic acid from ammonium fumarate. The first type of the biocatalyst consists in individual covalently crosslinked and permeabilized cells(I), while the second type is represented by cell aggregates (II). For the above preparation, biocatalyst I can be used only discontinuously in a mixed reactor. After termination of the reaction between individual cycles of its use, the biocatalyst is returned to the reactor in the form of a highly concentrated cell suspension or paste. Biocatalyst II can be used discontinuously or continuously in a fixed-bed column of the catalyst. The effects of pH, substrate concentration and temperature on the reaction velocity and effectivity of enzymic conversion was investigated. Optimal parameters of the reaction are as follows: pH 8.5, initial substrate concentration, 1.35 mol/L, temperature for discontinuous process, 37 degrees C, and temperature for continuous process, 25 degrees C. Under these conditions the enzymic conversion of substrate to product is quantitative. Under optimal toring conditions, the specific activity of both catalysts does not change within a period of one year. The operational half-life of the biocatalyst II during continuous use in a fixed-bed column of the catalyst under standard reaction conditions depends on the quality of the substrate. The discontinuous preparation of L-asparatic acid with the aid of biocatalyst I and continuous preparation of this product with the aid of biocatalyst II have been verified under pilot-plant conditions.     

Comparative study of spent grains and delignified spent grains as yeast supports for alcohol production from molasses

Fresh, defrosted and delignified brewer's spent grains (BSG) were used as yeast supports for alcoholic fermentation of molasses. Glucose solution (12%) with and without nutrients was used for cell immobilization on fresh BSG, without nutrients for cell immobilization on defrosted and with nutrients for cell immobilization on delignified BSG. Repeated fermentation batches were performed by the immobilized biocatalysts in molasses of 7, 10 and 12 initial Baume density without additional nutrients at 30 and 20 degrees C. Defrosted BSG immobilized biocatalyst was used only for repeated fermentation batches of 7 initial Baume density of molasses without nutrients at 30 and 20 degrees C. After immobilization, the immobilized microorganism population was at 10(9) cells/g support for all immobilized biocatalysts. Fresh BSG immobilized biocatalyst without additional nutrients for yeast immobilization resulted in higher fermentation rates, lower final Baume densities and higher ethanol productivities in molasses fermentation at 7, 10 and 12 initial degrees Be densities than the other above biocatalysts. Adaptation of defrosted BSG immobilized biocatalyst in the molasses fermentation system was observed from batch to batch approaching kinetic parameters reported in fresh BSG immobilized biocatalyst. The results of this study concerning the use of fresh or defrosted BSG as yeast supports could be promising for scale-up operation.     

Accessing microbial diversity for bioremediation and environmental restoration

Biological methods for decontamination promise an improved substitute for ineffective and costly physico-chemical remediation methods, although so far only a fraction of the total microbial diversity (i.e. the culturable fraction with metabolic potential) has been harnessed for this purpose. Exploring and exploiting the "overlooked" genetic resource might ameliorate concerns associated with the degradation of recalcitrant and xenobiotic pollutants that are not degraded or only poorly degraded by known culturable bacteria. Recent advances in the molecular genetics of biodegradation and in knowledge-based methods of rational protein modification provide insight into the development of "designer biocatalysts" for environmental restoration. The application of such genetically engineered microorganisms (GEMs) in the environment has been limited, however, owing to the risks associated with uncontrolled growth and proliferation of the introduced biocatalyst and horizontal gene transfer. Programming rapid death of the biocatalyst soon after the depletion of the pollutant could minimize the risks in developing these technologies for successful bioremediation.     

Oxygen diffusivity of synthetic gels derived from prepolymers

Summary The oxygen-diffusivity (D _m ) of 16 different gels formed with synthetic prepolymers (photo-crosslinkable resins, urethane resins and photosensitive resins), and that of calcium alginate (for comparison) was determined, using an oxygen electrode covered by the gel membranes with stepwise enzymatic removal of O₂ from the buffer solution. The water content of the gels was found to be decisive for the O₂-diffusivity of the gels: gels with the highest water content showed also the highest D _m . From these findings, the suitability of different polymeric gels for substrate conversion and biosensor systems could be predicted.Abbreviations A surface area of the cathode - c O₂-concentration in the membrane - d _m total thickness of the membrane - D _m O₂-diffusivity in the membrane - ENT, ENTP polymers prepared from hydroxyethylacrylate - ENTA, ENTC isophorone diisocyanate and linear skeleton of different molecular weight of poly(ethylene glycol) (ENT) or poly(propylene glycol) (ENTP), resp. ENTA in addition bears anionic groups, ENTC cationic groups - F Faraday's constant - i _s steady-state O₂ reduction current - N number of electrons per mole unit of reaction - PU polyurethane polymers with poly(ethylene glycol) and poly(propylene glycol) parts in the diol moiety and isocyanate functional groups at both terminals of the prepolymer - PVA-SbQ polyvinyl alcohol stilbazolium polymer     

Effectiveness factor for spherical biofilm catalysts

Immobilization is a method of avoiding wash-out of biocatalyst from a reactor system. For the modelling of these biocatalysts slab, cylinder, sphere and biofilm geometries are frequently used. A biofilm particle consists of an inert core which is used as a carrier for a layer that contains the enzymes or micro-organisms. This paper deals with the modelling and effectiveness factor calculations for such a biofilm particle and a general model for an immobilized, non-growing biocatalyst is presented. The model includes internal and external mass transfer resistance, the partitioning effect and inhibition or reversible reaction kinetics. Due to the non-linear reaction rate equations of the Michaelis Menten type, numerical techniques must be used for the solution of the combined diffusion reaction equation and calculation of the effectiveness factor. In this work we have used two different methods, orthogonal collocation and a method based on Runge-Kutta integration. Comparable use of CPU-time was found for these methods, but numerical stability and accuracy favour the Runge-Kutta method. In the case of Michaelis Menten kinetics (irreversible and without inhibition effects), an analytical expression for an approximate solution is presented. This method, which has an acceptable accuracy, takes far less CPU-time than the fore-mentioned numerical techniques.     

Biocatalyst-adsorbant systems: a viable alternative to proteolytic processes in solution

Proteolytic biocatalysts were adsorbed and stabilized using alumina as a support medium. Two biocatalyst-adsorbant systems were prepared with different physical characteristics of the adsorbant: alumina powder and alumina pearls. Direct adsorption onto the support medium has the main advantage, over other fixation methods, that preliminary steps are not required for a good interaction between the support and the biocatalyst. Proteases were adsorbed and stabilized without modifying or sterically hindering their active sites. Parameters affecting adsorption (pH, temperature, ionic strength) were varied so as to optimize adsorption conditions. Operational viability of the immobilized biocatalysts was demonstrated, taking into account the rate of desorption, resistance to microbial attack, and stability during storage. Desorption in water was studied in batch and continuous-flow processes, at various flow rates. The systems also proved to be resistant to microorganisms. Tests for stability during storage found the systems' activity remained constant after 60 days, and they performed better than biocatalysts in solution. Proteolysis of a solution of g per litre of azocasein was carried out in continuous-flow and batch modes, using our biocatalyst-adsorbant systems we prepared. In all cases, free amino group concentrations were around 2.5 times greater after treatment with biocatalyst-adsorbants than they were in the starting solution.     

Screening for novel biocatalysts

This review attempts to demonstrate the importance of goal-orientated screening for new biocatalysts. Examples of enzymes and microorganisms that have been developed and that have acquired commercial applications are described so as to illustrate the technological potential of biocatalysts. A survey of screening techniques and recently reported examples of screening from food, chemical, pharmaceutical and waste disposal applications etc. are also presented to demonstrate the feasibility of this approach for generating new biocatalysts. An appreciation of some of the difficulties involved, the achievements of Japanese researchers and some examples of the cornucopia of largely unrecognized and potentially valuable microbial activities are also given. An increased effort in screening would have the following benefits: an increased range of biocatalysts with different enzyme activities would be available and more biocatalysts with improved characteristics, suitable for use under industrial conditions, such as resistance to elevated temperatures, extremes of pH and organic solvents would be discovered. Secondly the manpower and other resources required to carry out screening programmes would be reduced, for instance by developing automated techniques. Thirdly, screening procedures would be made much more accessible to non-specialists. Fourthly, improved efforts and expertise in screening would supplement other emerging techniques such as protein engineering. The development of selective, non-random, goal-orientated screening techniques, methods of evaluating biocatalyst performance under operational conditions, and an approach that is more orientated towards commercially desirable goals are essential if these objectives are to be achieved. Screening of naturally occurring microorganisms still appears to be the best way to obtain new strains and/or enzymes for commercial applications. However, two major problems appear to exist. Firstly in identifying applications that are technically feasible and that have sufficient commercial potential to justify the research and development required to generate a new commercially viable biocatalyst and secondly the relatively small number of scientists outside Japan with skill and experience in screening for biocatalysts.