Production of androsta-1,4-diene-3,17-dione from cholesterol using immobilized growing cells of Mycobacterium sp. NRRL B-3683 adsorbed on solid carriers

Summary Living cells of Mycobacterium sp. NRRL B-3683 were immobilized by adsorption on different types of solid carriers in order to produce androsta-1,4-diene-3,17-dione (ADD) from cholesterol. Activated alumina proved to be the most preferred carrier for long-term operation when glucose and peptone were added to the reaction medium. In a repeated-batch process, the maximum productivity of ADD was about 0.19 g/l per day with a molar conversion rate of 77% when 1.0 g/l of cholesterol was added to the reaction medium. The half-life of the immobilized cells was more than 45 days and the system could be reactivated by incubating the immobilized cells in a cell growth medium.     

The enzymatic transformation of water-insoluble reactants in nonaqueous solvents. Conversion of cholesterol to cholest-4-ene-3-one by a Ncardia sp.

The rapid conversion of cholesterol to cholestenone by Nocardia in the presence of high proportions of water-immiscible solvent has been demonstrated. At high agitator speeds, the reaction rate was not limited by the rates of transfer of oxygen or cholesterol to the microorganisms. Using 100 g of thawed cells in 200 ml of carbon tetrachloride containing 16% (w/v) cholesterol, at 20°C cholestenone was formed at 7 g/hr. Cells could be separated easily from the organic solvent and reused. After 7 runs (69 hr) the reaction rate had fallen only to half the value for the first run.     

Microbial Transformation of Sterols

Cholesterol decomposing ability of 1589 microbial strains was examined. Two hundreds and thirty six strains from actinomycetes, bacteria, molds, and yeasts were found capable of oxidizing cholesterol into cholestenone. Cholesta-1,4-dien-3-one was produced by 5 strains of Streptomyces. The complete decomposition of cholesterol molecule was observed in the genera: Arthrobacter, Bacillus, Brevibacterium, Corynebacterium, Microbacterium, Mycobacterium, Nocardia, Protaminobacter, Serratia, and Streptomyces. α,α′-Dipyridyl and arsenite inhibited decomposing enzymes giving rise to cholestenone, cholesta-1,4-dien-3-one, and an intermediate probably devoid of the sterol side chain.

Selective cleavage of the side chains of various sterols at C-17, giving rise to androsta-1,4-diene-3,17-dione (ADD), occurred in the presence of α,α′-dipyridyl by microorganisms of the following genera: Arthrobacter, Bacillus, Brevibacterium, Corynebacterium, Microbacterium, Mycobacterium, Nocardia, Protaminobacter, Serratia, and Streptomyces. The degradation pathway of cholesterol, for example, was shown as follows:

Other sterols such as campesterol, β-sitosterol, stigmasterol and 7-dehydrocholesterol were degraded by the same sequence. The pathway exemplified in cholesterol is considered to be the general degradation pathway of sterols by their decomposing microorganisms.

It was further demonstrated that ADD thus formed from sterols was converted into 3-hydroxy-9,10-secoandrosta-1,3,5(10)-triene-9,17-dione.     

Fermentation ofd-xylose,d-glucose andl-arabinose mixture byPichia stipitis Y 7124: sugar tolerance

Summary The effect of substrate concentration (S ₀) on the fermentation parameters of a sugar mixture byPichia stipitis Y 7124 was investigated under anaerobic and microaerobic conditions. Under microaerobiosisP. stipitis maintained high ethanol yield and productivity when initial substrate concentration did not exceed 150 g/l; ethanol yield of about 0.40 g/g and volumetric productivity up to 0.39 g/l per hour were obtained. Optimal specific ethanol productivity (0.2 g/g per hour) was observed withS ₀=110 g/l. Under anaerobic conditionsP. stipitis exhibited the highest fermentative performances atS ₀=20 g/l; it produced ethanol with a yield of 0.42 g/g, with a specific rate of 1.1 g/g per day. When the initial substrate level increased, specific ethanol productivity declined gradually and ethanol yield was dependent on the degree of utilization of each sugar in the mixture.Abbreviations E _m maximum produced ethanol (g/l) - E ₀ initial ethanol (g/l) - E _v evaporated ethanol (g/l) - Q _p volumetric productivity of ethanol (g ethanol/l per hour or g/l per day) - q _p specific productivity of ethanol (g ethanol/g cells per hour) - q _pm maximum specific productivity of ethanol (g/l per hour) - S ₀ initial substrate concentration (g/l) - t _f time at which produced ethanol is maximum (h) - Y _p/s ethanol yield (g ethanol produced/g substrate utilized) - Y _x/s cell yeild (g cells produced/g substrate utilized) - Y _xo/xy xylitol yield (g xylitol produced/g xylose utilized) - probability coefficient - specific growth rate coefficient (h^-1 or d^-1)     

Continuous production ofl-lactic acid from whey permeate by immobilizedLactobacillus casei subsp.casei

Summary The production of l-lactic acid from whey permeate, a waste product of the dairy industry, by fermentation with the lactic acid bacterium Lactobacillus casei subsp. casei was investigated. A fermentation medium consisting of permeate and supplements, which enables exponential growth of the organisms, was developed. A fast method for determination of free and immobilized biomass in solid-rich media, based on measurement of cellular ATP, was evolved. Continuous fermentations in a stirred tank reactor (STR) and in a fluidized bed reactor (FBR) with immobilized biomass were compared. In the STR a volumetric productivity of 5.5 g/l per hour at 100% substrate conversion [dilution rate (D) = 0.22 h^–1] was determined. In the FBR porous sintered glass beads were used for immobilization and a maximum biomass concentration of 105 g/kg support was measured. A productivity of 10 g/l per hour was obtained at D = 0.4 h^–1 (substrate conversion 93%) and of 13.5 g/l per hour at D = 1.0 h^–1 (substrate conversion 50%). Offprint requests to: W. Krischke     

Conversion of soybean sterols into 3,17-diketosteroids using actinobacteria <Emphasis Type="Italic">Mycobacterium neoaurum,Pimelobacter simplex</Emphasis>, and <Emphasis Type="Italic">Rhodococcus erythropolis</Emphasis>

Soybean sterols were converted into androst-4-ene-3,17-dione (AD) and 9α-hydroxyandrost-4-ene-3,17-dione (9-OH-AD) using three actinobacterium strains. The transformation of a microcrystallic substrate (particle size 5–15 μm) or the transformation in the presence of randomly methylated β-cyclodextrin (MCD) were carried out by Mycobacterium neoaurum with a phytosterol load of 30 g/l over 144 h with an AD content of 14.5 and 15.2 g/l, respectively. AD obtained in the presence of MCD was transformed into ADD (13.5 g/l) by Pimelobacter simplex cells over 3 h and into 9-OH-AD by Rhodococcus erythropolis cells after 22 h without the isolation of AD from the cultural liquid. The crude product ADD was obtained in 75% yield, based on phytosterol. It contained as by-products 1.25% of AD and 1.5% of 1,2-dehydrotestosterone. In a control experiment—the process of 1,2-dehydrogenation of 20 g/l AD in the water solution of MCD—no by-products were isolated. Thus, it is more expedient to introduce the 1,2-double bond into pure AD, whereas R. erythropolis strain with low destructive activity towards steroid nucleus can be used in the mixed culture with M. neoaurum. The crystal product contained, according to HPLC, 80% of 9-OH-AD, and 1.5% AD was obtained. The yield of 9-OH-AD (m.p. 218–220°C) based on transformed phytosterol was 56%.     

The reduction of xylose to xylitol by Candida guilliermondii and Candida parapsilosis: Incidence of oxygen and pH

Summary The ability of C. guilliermondii and C. parapsilosis to ferment xylose to xylitol was evaluated under different oxygen transfer rates in order to enhance the xylitol yield. In C. guilliermondii, a maximal xylitol yield of 0.66 g/g was obtained when oxygen transfer rate was 2.2 mmol/l.h. Optimal conditions to produce xylitol by C. parapsilosis (0.75 g/g) arose from cultures at pH 4.75 with 0.4 mmoles of oxygen/l.h. The response of the yeasts to anaerobic conditions has shown that oxygen was required for xylose metabolism.Nomenclature max maximum specific growth rate (per hour) - qSmax maximum specific rate of xylose consumption (g xylose per g dry biomass per hour) - qpmax maximum specific productivity of xylitol (g xylitol per g dry biomass per hour) - Qp average volumetric productivity of xylitol (g xylitol per liter per hour) - Y_P/S xylitol yield (g xylitol per g substrate utilized) - Y_P'/S glycerol yield (g glycerol per g substrate utilized) - Y_X/S biomass yield (g dry biomass per g substrate utilized)     

High ethanol productivities using small Ca-alginate beads of immobilized cells of Zymomonas mobilis

Summary Zymomonas mobilis cells were immobilized into small 1 mm diameter beads of Ca-alginate in order to minimize mass transfer limitations and maximize immobilized cell activity. A combination of small bead size with a high cell concentration of 58 g dry wt. cell per lit. bead volume resulted in high ethanol productivities using a newly designed packed bed bioreactor system. Steady-state dilution rates ranging from 0.4 h^-1 to 3.9 h^-1 were run resulting in a maximum productivity of 102 g ethanol/l/h for an inlet substrate concentration of 100 g glu/l and 87% conversion. The bioreactor was run continuously at a fixed dilution rate for 384 h and short intermittent treatment of the beads with CaCl₂ temporarily increased ethanol productivity to a maximum of 116 g ethanol/l/h.     

Production of ethanol from cellulose,Solka Floc BW 200, in a fedbatch mixed culture of Trichoderma reesei,C 30, and Saccharomyces cerevisiae

Summary Solka floc BW 200 was converted to ethanol in a multistep conversion using Saccharomyces cerevisiae in combination with Trichoderma reesei, C 30. Up to 40 g/l ethanol was obtained with these mixed cultures and a maximum yield of 83% and productivity of 0.2 g/l·h was achieved. The limiting factor in the process was the activity of the cellulolytic enzymes produced by T. reesei, C 30. It is suggested that oxygen can be used in this type of a mixed culture as an external regulator for maintaining an optimal cellulolytic enzyme activity in the system, thus giving an overall optimal conversion of cellulose to ethanol.     

The enzymatic transformation of water-insoluble reactants in nonaqueous solvents. Conversion of cholesterol to cholest-4-ene-3-one by a Nocardia sp. Reprinted from Biotechnology and Bioengineering, Vol. XVII, Pages 815-826 (1975)

The rapid conversion of cholesterol to cholestenone by Nocardia in the presence of high proportions of water-immiscible solvent has been demonstrated. At high agitator speeds, the reaction rate was not limited by the rates of transfer of oxygen or cholesterol to the microorganisms. Using 100 g of thawed cells in 200 ml of carbon tetrachloride containing 16% (w/v) cholesterol, at 20 degrees C cholestenone was formed at 7 g/hr. Cells could be separated easily from the organic solvent and reused. After 7 runs (69 hr) the reaction rate had fallen only to half the value for the first run.     

Xylitol production from D-xylose byCandida guillermondii: Fermentation behaviour

Summary The ability ofCandida guillermondii to produce xylitol from xylose and to ferment individual non xylose hemicellulosic derived sugars was investigated in microaerobic conditions. Xylose was converted into xylitol with a yield of 0,63 g/g and ethanol was produced in negligible amounts. The strain did not convert glucose, mannose and galactose into their corresponding polyols but only into ethanol and cell mass. By contrast, fermentation of arabinose lead to the formation of arabitol. On D-xylose medium,Candida guillermondii exhibited high yield and rate of xylitol production when the initial sugar concentration exceeded 110 g/l. A final xylitol concentration of 221 g/l was obtained from 300 g/l D-xylose with a yield of 82,6% of theoretical and an average specific rate of 0,19 g/g.h.Nomenclature Q_p average volumetric productivity of xylitol (g xylitol/l per hour) - q_p average specific productivity of xylitol (g xylitol/g of cells per hour) - So initial xylose concentration (g/l) - tf incubation time (hours) - Y_P/S xylitol yield (g of xylitol produced/g of xylose utilized) - Y_E/S ethanol yield (g of ethanol produced/g of substrate utilized) - Y_X/S cells yield (g of cells/g of substrate utilized) - specific growth rate coefficient (h^–1) - _max maximum specific growth rate coefficient (h^–1)     

Effect of oleic acid on the production of ethanol and fructose from glucose/fructose mixtures in an immobilized cell reactor

Saccharomyces cerevisiae ATCC 39859 was immobilized onto small cubes of wood to produce ethanol and very enriched fructose syrup from glucose/fructose mixtures through the selective fermentation of glucose. A maximum ethanol productivity of 21.9 g/l-h was attained from a feed containing 9.7% (w/v) glucose and 9.9% (w/v) fructose. An ethanol concentration, glucose conversion and fructose yield of 29.6 g/l, 62% and 99% were obtained, respectively. This resulted in a final fructose/glucose ratio of 2.7. At lower ethanol productivity levels the fructose/glucose ratio increases, as does the ethanol concentration in the effluent. The addition of 30 mg/l oleic acid to the medium increased the ethanol productivity and its concentration by 13% at a dilution rate of 0.74 h^?1.     

Accumulation of androstadiene-dione by overexpression of heterologous 3-ketosteroid Δ1-dehydrogenase in Mycobacterium neoaurum NwIB-01

Mycobacterium neoaurum NwIB-01 exhibits powerful ability to cleave the side chain of soybean phytosterols to accumulate 4-androstene-3,17-dione (AD) and 1,4-androstadiene-3,17-dione (ADD). The difficulty in separation of AD from ADD is one of the key bottlenecks to the microbial transformation of phytosterols in the industry. To enhance ADD quantity in products, 3-ketosteroid Δ¹-dehydrogenase genes (kstD _M and kstD _A) were obtained from M. neoaurum NwIB-01 and Arthrobacter simplex respectively. Using replicating vector pMV261, kstD _M and kstD _A were overexpressed in M. neoaurum NwIB-01. For foreign gene stable expression, the integration vector pMV306 was used for kstD _M/kstD _A overexpression and the relevant sequences of promoter and kanamycin antibiotic resistance gene sequences were amplified by PCR to verify plasmid integrity. The resultant plasmid and mutant strain were verified and the kstD augmentation mutants were good ADD-producing strains. The ADD producing capacity of NwIB-04 and NwIB-05 was 0.1401 and 0.1740 g/l (cultured in shake bottles with 0.4 g/l phytosterols), and the molar ratio of ADD in products was 98.34 and 98.60 %, respectively. This study on the manipulation of the main kstD_M gene in Mycobacterium sp. provides a feasible way to achieve excellent phytosterol-transformation strains with high product purity.     

Production of glycerol by immobilizedPichia farinosa

Summary Cells of the osmophilic yeastPichia farinosa were immobilized in sintered glass Raschig rings for the production of glycerol. The kinetics of production were observed under different conditions in batch, fed-batch and semicontinuous fermentations in fixed-bed column reactors and compared with those of free cells. 2.6 × 10⁹ cells/g sintered glass were adsorbed. The glycerol productivity amounted to 8.1 g/l per day. The highest concentration reached in batch culture was 86 g/l with immobilized cells. Fermentations using immobilized cells were accelerated compared to fermentations using free cells and maximum yield and productivity were reached at lower initial sugar concentrations. Using scanning electron microscopy it was observed that the shape of the cells was related to the sugar concentration in the medium. The experiments show thatP. farinosa produces glycerol with a high and constant productivity over long periods of time.     

The effect of pH,temperature and sucrose concentration on high productivity continuous ethanol fermentation using Zymomonas mobilis

Summary A flocculent strain of Zymomonas mobilis was used for ethanol production from sucrose. Using a fermentor with cell recycle (internal and external settler) high sugar conversion and ethanol productivity were obtained. At a dilution rate of 0.5 h^-1 (giving 96% sugar conversion) the ethanol productivity, yield and concentrations respectively were 20 g/l/h, 0.45 g/g and 40 g/l using a medium containing 100 g/l sucrose. At a sucrose concentration of 150 g/l, the ethanol concentration reached 60 g/l. The ethanol yield was 80% theoretical due to levan and fructo-oligomer formation. No sorbitol was detected. This fermentation was conducted at a range of conditions from 30 to 36°C and from pH 4.0 to 5.5.     

Continuous production of gluconic acid by immobilized Gluconobacter oxydans cell bioreactor

Summary Living Gluconobacter oxydans cells were attached on fibrous nylon carrier. Free gluconic acid was directly continuously produced in an aerated tubular immobilized-cell bioreactor for at least 6 months, with a volumetric productivity of at least 5 g/lh at 100 g/l substrate glucose and about 80 g/l product gluconic acid concentrations. The highest volumetric productivity in respect to glucose concentration was obtained with 175 g/l glucose, with about 120 g/l product gluconic acid level. With self-directing optimization procedure in respect to maximum product gluconic acid level, productivities as high as about 12–15 g/lh were obtained at relatively high substrate feed rate of 0.166 l/lh and relatively low aeration rate of 0.5 l/lmin. The highest glucose conversion of about 96% was obtained with a long residence time, at the lowest substrate feed rate used at a relatively low aeration rate, resulting however in a significant increase in ketogluconic acid production.     

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.     

Comparative study of reactor performance for the resolution of d,l-amino acids

The racemic resolution of l-valine and l-serine by fungal aminoacylase has been evaluated by comparing the performance of various reactor configurations including an anion exchange nylon tangential flow membrane reactor, a tubular reactor with aminoacylase adsorbed onto DEAE-Sephadex as support and a continuous stirred tank reactor with enzyme recycling using a flat ultrafiltration module (CSTR/UF). Among the substrates tested, the N-chloroacetyl-d,l-amino acids were the preferred substrates, showing the highest catalytic efficiency (V_m/K_m).Optimum reactor operational conditions obtained in discontinuous assays were selected to study the behaviour of the reactors in a continuous mode. DEAE-Sephadex loaded six-fold more enzyme than anion exchange nylon (60 and 10 gE/litre, respectively, related to reactor volume), whereas enzyme concentration within the CSTR/UF reactor was limited only by enzyme solubility.The tangential flow membrane reactor configuration with a 10 g/litre enzyme concentration produced higher productivity values (0·35 kg l-valine/litre per day, and 80% conversion degree) and operational stability (t = 161 days) than the CSTR/UF reactor (0·24 kg l-valine/litre per day, and 80% conversion degree) performing with the same enzyme concentration. The tubular reactor with the enzyme adsorbed onto DEAE-Sephadex (60 g/litre enzyme load) showed higher productivity values (1·9 kg l-valine/litre per day, and 80% conversion degree) and operational stability (t = 70 days) than the CSTR/UF reactor (1·05 kg l-valine/litre per day, and 80% conversion degree). However, the CSTR/UF reactor was the preferred configuration, as it had the highest enzyme load and productivity (1·95 kg l-valine/litre per day of reactor volume, and 80% conversion degree), a half-life of 55 days at 50°C, and the possibility of easy continuous enzyme addition.     

Influence of hydroxypropyl-β-cyclodextrin on phytosterol biotransformation by different strains of Mycobacterium neoaurum

Cyclodextrins (CDs) can improve productivity in the biotransformation of steroids by increasing conversion rate, conversion ratio, or substrate concentration. However, little is known of the proportion of products formed by multi-catabolic enzymes, e.g., via sterol side chain cleavage. Using three strains with different androst-1,4-diene-3,17-dione (ADD) to androst-4-ene-3,17-dione (AD) ratios, Mycobacterium neoaurum TCCC 11028 (MNR), M. neoaurum TCCC 11028 M1 (MNR M1), and M. neoaurum TCCC 11028 M3 (MNR M3), we found that hydroxypropyl-β-cyclodextrin (HP-β-CD) can appreciably increase the ratio of ADD to AD, the reaction rate, and the molar conversion. In the presence of HP-β-CD, conversion of 0.5?g/L of phytosterol (PS) was 2.4, 2.4, and 2.3 times higher in the MNR, MNR M1, and MNR M3 systems, respectively, than in the controls. The ADD proportion increased by 38.4, 61.5, and 5.9?% compared with the control experiment, which resulted in a strong shift in the ADD/AD ratio in the ADD direction. Our results imply that the three PS-biotransforming strains cause efficient side chain degradation of PS, and the increased conversion of PS when using HP-β-CD may be associated with the higher PS concentration in each case. A similar solubilizing effect may not induce a prominent influence on the ADD/AD ratio. However, the different activities of the Δ(1)-dehydrogenase of PS-biotransforming strains result in different incremental percentage yields of ADD and ADD/AD ratio in the presence of HP-β-CD.     

Continuous alpha-amylase production using Bacillus amyloliquefaciens adsorbed on an ion exchange resin

Summary A method for the continuous production of extracellular alpha amylase by surface immobilized cells of Bacillus amyloliquefaciens NRC 2147 has been developed. A large-pore, macroreticular anionic exchange resin was capable of initially immobilizing an effective cell concentration of 17.5 g DW/1 (based on a total reactor volume of 160 ml). The reactor was operated continuously with a nutrient medium containing 15 g/l soluble starch, as well as yeast extract and salts. Aeration was achieved by sparging oxygen enriched air into the column inlet. Fermentor plugging by cells was avoided by periodically substituting the nutrient medium with medium lacking in both soluble starch and yeast extract. This fermentor was operated for over 200 h and obtained a steady state enzyme concentration of 18700 amylase activity units per litre (18.7 kU/l), and an enzyme volumetric productivity of 9700 amylase activity units per litre per hour (9.7 kU/l-h). Parallel fermentations were performed using a 2 l stirred vessel fermentor capable of operation in batch and continuous mode. All fermentation conditions employed were identical to those of the immobilized cell experiments in order to assess the performance of the immobilized cell reactor. Batch stirred tank operation yielded a maximum amylase activity of 150 kU/l and a volumetric productivity of 2.45 kU/l-h. The maximum cell concentration obtained was 5.85 g DW/l. Continuous stirred tank fermentation obtained a maximum effluent amylase activity of 6.9 kU/l and a maximum enzyme volumetric productivity of 2.73 kU/l-h. Both of these maximum values were observed at a dilution rate of 0.345 l/h. The immobilized cell reactor was observed to achieve larger volumetric productivities than either mode of stirred tank fermentation, but achieved an enzyme activity concentration lower than that of the batch stirred tank fermentor.