Adsorptive bioconversion of ethylene glycol to glycolic acid by Gluconobacter oxydans DSM 2003

An integrated bioprocess for the production of glycolic acid from ethylene glycol with Gluconobacter oxydans DSM 2003 and in situ product removal were investigated. A slight substrate inhibition was observed as substrate concentration was above 20 g/l and the product inhibition was much stronger. Bioconversion of glycolic acid is an end-product-inhibited reaction. In order to increase the productivity of glycolic acid and reduce the end-product inhibition of bioconversion, an adsorptive bioconversion for glycolic acid production from ethylene glycol catalyzed by resting cells of G. oxydans DSM 2003, was developed by using anion exchange resin D315 as the adsorbent for selective removal of glycolic acid from the reaction mixture. This approach allowed the yield of glycolic acid to be increased to 93.2 g/l, compared to 74.5 g/l obtained from a conventional fed-batch mode.     

Adsorptive bioconversion of ethylene glycol to glycolic acid by Gluconobacter oxydans DSM 2003

An integrated bioprocess for the production of glycolic acid from ethylene glycol with Gluconobacter oxydans DSM 2003 and in situ product removal were investigated. A slight substrate inhibition was observed as substrate concentration was above 20 g/l and the product inhibition was much stronger. Bioconversion of glycolic acid is an end-product-inhibited reaction. In order to increase the productivity of glycolic acid and reduce the end-product inhibition of bioconversion, an adsorptive bioconversion for glycolic acid production from ethylene glycol catalyzed by resting cells of G. oxydans DSM 2003, was developed by using anion exchange resin D315 as the adsorbent for selective removal of glycolic acid from the reaction mixture. This approach allowed the yield of glycolic acid to be increased to 93.2 g/l, compared to 74.5 g/l obtained from a conventional fed-batch mode.     

(S)-3-Pentyn-2-ol production through microbial enzyme-catalyzed, highly enantioselective hydrolysis of racemic 3-pentyn-2-ol esters

Air-dried cells of Hansenula nonfermentans AKU 4332 catalyzed the production of (S)-3-pentyn-2-ol from (RS)-3- pentyn-2-ol acetate ester at 10% (v/v). The product was formed at 96.6% e.e. with a molar yield of 45% in 24 h. © Rapid Science Ltd. 1998     

High cell density fermentation of <Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> DSM 2003 for glycolic acid production

Gluconobacter oxydans has a lower biomass yield. Uniform design (UD) was applied to determine the optimum composition of the critical media and their mutual interactions for increased biomass yield of Gluconobacter oxydans DSM 2003 in shake flasks. Fed-batch fermentation process for biomass was optimized in a 3.7-l fermentor. By undertaking a preliminary and improved fed-batch fermentation-process strategy, a cell density of 6.0 g/l (DCW) was achieved in 22 h and 14.1 g/l (DCW) in 35 h, which is the highest cell density of G. oxydans produced thus far in a 3.7-l bioreactor. The biomass production was increased by 135% compared with that using the original cultivation strategy. Bioconversion of ethylene glycol to glycolic acid was catalyzed by the resting cells of G. oxydans DSM 2003, and conversion rate reached 86.7% in 48 h. In summary, the approach including high-density fermentation of G. oxydans DSM 2003 and bioconversion process was established and proved to be an effective method for glycolic acid production.     

一株乙二醇氧化酶菌株的筛选及催化特性的初步研究

利用富集培养技术从土壤中筛选获得1株高活性二醇氧化活性菌株Brevibacterium sp.CCZU12-1。以Brevibacterium sp.CCZU12-1静息细胞为催化剂,最适催化反应温度、反应pH和金属离子添加量分别为30℃、6.5和Mn2＋0.1 mmol/L。在最佳条件下,转化200 mmol/L乙二醇24 h,羟基乙酸的产率为94.6%,分批补料乙二醇5批,羟基乙酸的累积浓度为972 mmol/L。     

Regioselective hydroxylation of quinolinic acid,lutidinic acid and isocinchomeronic acid by resting cells of pyridine dicarboxylic acid-degrading microorganisms

Microorganisms aerobically degrading quinolinic acid, lutidinic acid or isocinchomeronic acid were isolated and the microbial regioselective hydroxylation of these pyridine dicarboxylic acids was studied. Alcaligenes sp. UK21 cells converted quinolinic acid into 6-hydroxypicolinic acid, suggesting the involvement of two enzyme reactions catalyzing hydroxylation at position C6 and decarboxylation at position C3 of quinolinic acid. Resting cells of Alcaligenes sp. UK21 accumulated 94.9 mM 6-hydroxypicolinic acid (13.2 g l(-1)), with a 96% molar conversion yield by 48 h incubation. Rhizobium sp. LA17 and Hydrogenophaga sp. IMA01 catalyzed the regioselective hydroxylation of lutidinic acid and isocinchomeronic acid into 6-hydroxylutidinic acid and 6-hydroxyisocinchomeronic acid, respectively. 6-Hydroxylutidinic acid accumulated up to 95.4 mM (17.5 g l(-1)) by 24 h incubation in the resting cells reaction, using Rhizobium sp. LA17, with a 99% molar conversion yield. Resting cells of Hydrogenophaga sp. IMA01 produced 88.7 mM 6-hydroxyisocinchomeronic acid (16.2 g l(-1)) by 24 h incubation, with a 81% molar conversion yield.     

Microbial production of chiral pantothenonitrile through stereospecific reduction of 2′-ketopantothenonitrile

Summary A novel enzymatic process for the synthesis of chiral pantothenonitrile through the asymmetric reduction of 2-ketopantothenonitrile is described.Sporidiobolus salmonicolor AKU 4440 was found to convert 2-ketopantothenonitrile (50 mg/ml) to D-(+)-pantothenonitrile (93.6% e.e.), with a molar yield of 95.6%. In a similar manner, conversion to L-(–)-pantothenonitrile occurred on incubation with washed cells ofRhodotorula glutinis AKU 4845 as the catalyst.     

High-level expression of Rhodotorula gracilis d-amino acid oxidase in Pichia pastoris

By combining gene design and heterologous over-expression of Rhodotorula gracilis D-amino acid oxidase (RgDAO) in Pichia pastoris, enzyme production was enhanced by one order of magnitude compared to literature benchmarks, giving 350 kUnits/l of fed-batch bioreactor culture with a productivity of 3.1 kUnits/l h. P. pastoris cells permeabilized by freeze-drying and incubation in 2-propanol (10% v/v) produce a highly active (1.6 kUnits/g dry matter) and stable oxidase preparation. Critical bottlenecks in the development of an RgDAO catalyst for industrial applications have been eliminated.     

Enzymic acylation of 6-aminopenicillanic acid

The enzymic synthesis of benzylpenicillin from 6-aminopenicillanic acid in the presence of poly (ethylene glycol) has been studied. With equimolar initial concentrations (20 mM) of 6-aminopenicillanic acid and phenylacetic acid a 60% conversion to benzylpenicillin can be achieved at 10°C and pH 5.2 in the presence of 45% (w/v) poly(ethylene glycol). Under these conditions the lactam ring of the benzylpenicillin and 6-aminopenicillanic acid and the enzyme, penicillin acylase (penicillin amidase, penicillin amidohydrolase, EC 3.5.1.11), were more stable than in the absence of the polyol.     

Effect of glycerol,polyethylene glycol and glutaraldehyde on stability of phenylalanine ammonia-lyase activity in yeast

Summary The polyhydric alcohols, glycerol and sorbitol, significantly increased the rate ofl-phenylalanine production from trans-cinnamic acid using whole cells ofRhodotorula rubra. Chloride ions and oxygen prevented the stimulatory effect of the polyhydric alcohols. Furthermore, the severe inhibition, of the biotransformation by high trans-cinnamic acid concentrations was alleviated in the presence of glycerol, and sorbitol. The rate of conversion could be manipulated still further, even with high trnas-cinnamic acid concentrations, by elevating the reaction pH to, 12 in the presence of polyhydric alcohol. When cells were also treated first with glutaradehyde (0.1% v/v) and then polyethylene glycol (15% v/v), although neither compound stimulated the actual rate of bioconversion, the reaction was markedly stabilised and gave a 73% yield after 28 days of continuous operation.     

Effect of Aerva lanata on calcium oxalate urolithiasis in rats

Calcium oxalate (CaOx) stone was induced in rats using 0.75% of ethylene glycol in drinking water for 28 days. Ethylene glycol treated rats showed significant increase in the activities of oxalate synthesizing enzymes such as glycolic acid oxidase (GAO) in liver and lactate dehydrogenase (LDH) in liver and kidney. CaOx crystal deposition, as indicated by increased excretion of stone-forming constituents in urine, such as calcium, oxalate, uric acid, phosphorus and protein and decreased concentration of inhibitors, such as citrate and magnesium was observed in ethylene glycol induced urolithic rats. Histopathological studies also confirmed the deposition of CaOx crystals. Administration of Aerva lanata aqueous suspension (2g/kg body wt/dose/day for 28 days) to CaOx urolithic rats had reduced the oxalate synthesizing enzymes, diminished the markers of crystal deposition in the kidney. The results of the present study confirmed that A. lanata can be used as an curative agent for urolithiasis.     

赤霉烯酮的微生物还原

用Rhodtorula sp.Saccharomyces sp.Arthorbacter sp.和Candida sp．四属20株菌对由Fusarium graminearum 产生的类雌激素——赤霉烯酮(Zearalenone)的还原转化进行了研究。实验结果证明,Rhodotorula sp和 Arthrobacter sp．的还原产物主要是α-赤霉烯醇(α-Zearalenol,经HPLC鉴定含量分别为96％和84％)。Saccharomyces sp．和Candidasp.的主要还原产物是β-赤霉烯醇(β-Zearalenol,经HPLC鉴定含量分别为91％和92％)。产物均经HPLC、13C—NMR和MS鉴定确证。     

Poly(ethylene glycol)-mediated molar mass control of short-chain- and medium-chain-length poly(hydroxyalkanoates) from Pseudomonas oleovorans

Three strains of Pseudomonas oleovorans, a well known poly(hydroxyalkanoate) (PHA) producer, were tested for the ability to control PHA molar mass and end group structure by addition of poly(ethylene glycol) (PEG) to the fermentation medium. Each strain of P. oleovorans - NRRL B-14682 (B-14682), NRRL B-14683 (B-14683), and NRRL B-778 (B-778) - synthesized a different type of PHA from oleic acid when cultured under identical growth conditions. Strain B-14682 produced poly(3-hydroxybutyrate) (PHB), while B-14683 synthesized a medium-chain-length PHA ( mcl-PHA) with a repeat unit composition ranging from C4 to C14 and some mono-unsaturation in the C14 alkyl side chains. Strain B-778 synthesized a mixture of PHB (95 mol%) and mcl-PHA (5 mol%). The addition of 0.5% (v/v) PEG (M(n) =200 g/mol, PEG-200) to the fermentation broth of strains B-14682 and B-778 resulted in chain termination through esterification at the carboxyl terminus of the PHB with PEG chain segments, thus reducing the molar mass by 54% and 23%, respectively. The molar mass of the mcl-PHA produced by strains B-14683 and B-778 also showed a 34% and 47% reduction in the presence of PEG-200, respectively, but no evidence of esterification was present. PEG-400 (M(n) =400 g/mol) had a reduced effect on PHA molar mass. In fact, the molar masses of the mcl-PHA derived from strain B-14683 and both the PHB and mcl-PHA from B-778 were unchanged by PEG-400. In contrast, the PHB produced by B-14682 showed a 35% reduction in molar mass in the presence of PEG-400.     

Selective and continuous degradation of carbazole contained in petroleum oil by resting cells of Sphingomonas sp. CDH-7.

Microbial degradation of carbazole (CA), a model of hard-removal heterocyclic nitrogen compounds contained in petroleum oil, was examined using Sphingomonas sp. CDH-7 isolated from a soil sample by screening for CA-assimilating microorganisms. CDH-7 used CA as a sole source of carbon and nitrogen, and metabolized CA to ammonia via anthranilic acid as an intermediate product. When CDH-7 was cultivated in the medium containing CA at the concentration of 500 mg/l (2.99 mM), CA was completely degraded within 50 h. By the reaction with the resting cells of CDH-7, 500 mg/l of CA was completely degraded within 4 h, with 1.64 mM of ammonia accumulated in the reaction mixture. When CA was added at the concentration of 100 mg/l (0.599 mM) periodically to the reaction mixture ten times, 925 mg/l (5.54 mM) of CA was degraded within 48 h by the resting cells, and 4.50 mM of ammonia was accumulated in the reaction mixture with a 75.1% molar conversion yield based on total CA added. The resting cells could almost completely degrade CA in a two-liquid-phase system which consists of water and organic solvent, even in the presence of 20% (v/v) isooctane, n-hexane, cyclohexane, and kerosene as a model petroleum oil. In the presence of an organic solvent system such as 20% (v/v) pxylene, toluene, and heptanol, however, CA degradation yields decreased.     

A study on cryoprotectant solution suitable for vitrification of rat two-cell stage embryos

The present study was performed to develop a suitable cryoprotectant solution for cryopreservation of rat two-cell stage embryos. First, we examined the cell permeability of several cryoprotectants; propylene glycol had the fastest permeability compared to dimethyl sulfoxide, ethylene glycol, and glycerol. Embryos were then exposed to a solution containing propylene glycol to evaluate its effects on fetal development. As the development was similar to that of fresh embryos, P10 (10% v/v propylene glycol in PB1) was used as a pretreatment solution. Next, the effects of the vitrification solution components (sucrose, propylene glycol, ethylene glycol, and Percoll) were examined by observing the vitrification status; 10% v/v propylene glycol, 30% v/v ethylene glycol, 0.3 mol sucrose, and 20% v/v Percoll in PB1 (PEPeS) was the minimum essential concentration for effective vitrification without the formation of ice crystals or freeze fractures.     

Production of androsta-1,4-diene-3,17-dione from cholesterol using two-step microbial transformation

A novel two-step transformation process for the production of androsta-l by microorganisms-diene-3,17-dione (ADD) from a high concetration of cholesterol by microorganisms is proposed. Cholesterol (20 g/l) was initially converted to cholest-4-en-3-one (cholestenone) by an inducible cholesterol oxidase-producing bacterium, Arthrobacter simplex U-S-A-18. The maximum productivity of cholestenone was 8 g/l per day and the molar conversion rate was 80%. Subsequently, a fine suspension of cholestenone (50 g/l), which was prepared directly from the fermentation broth of A. simplex, was converted to ADD by Mycobacterium sp. NRRL B-3683 in the presence of an androstenone adsorbent, Amberlite XAD-7. The maximum productivity of ADD was 0.91 g/l per day and the molar conversion rate was 35%. Correspondence to: W.-H. Liu     

Production of (R )-3-pentyn-2-ol through stereospecific hydrolysis of racemic 3-pentyn-2-ol esters with microbial enzymes

Microorganisms and commercial enzymes were screened for their ability to produce (R)-3-pentyn-2-ol from racemic 3-pentyn-2-ol esters through stereospecific hydrolysis. Among the esters formed with acetic acid, propionic acid, hexanoic acid and benzoic acid, the acetate was most effectively hydrolyzed by microbial cells and commercial lipases with high stereospecificity. Rhodococcus rubropertinctus AKU NOC082 was a good catalyst for (R)-3-pentyn-2-ol production through the hydrolytic resolution of racemic 3-pentyn-2-yl acetate. With 15%, 25% and 50% (v/v) racemic 3-pentyn-2-yl acetate as the substrate, 42.6%, 40.8% and 40.0% was hydrolyzed in 5 h, 10 h and 98 h respectively, under the optimized conditions (pH 7.0, 30 °C, 7.5% wet cell concentration), the (R) enantiomer of 3-pentyn-2-ol being formed with an optical purity of 97.8%, 98.0% and 94.2% respectively. Received: 2 June 1998 / Received revision: 3 August 1998 / Accepted: 3 September 1998     

Regio- and Stereo-selective Hydroxylation of Abietic Acid Derivatives by Mucor circinelloides and Mortierella isabellina

Mucor circinelloides and Mortierella isabellina hydroxylated dehydroabietic acid (DehA). DehA was converted regio- and stereo-selectively by whole cells of Mr. circinelloides to give 2α-hydroxydehydroabietic acid in a 75% molar conversion yield (11 mM from 14.7 mM DehA) after 72 h in the cultivation medium containing 3% (v/v) Tween 80. With cells of Ma. isabellina, under the same conditions, 20.5 mM (6.5 g l⁻¹) 2–hydroxydehydroabietic acid (α/β=81/19) was formed from 26.4 mM DehA.     

Physical polymer matrices based on affinity interactions between peptides and polysaccharides

A rapidly forming polymer matrix with affinity-based controlled release properties was developed based upon interactions between heparin-binding peptides and heparin. Dynamic mechanical testing of 10% (w/v) compositions consisting of a 3:1 molar ratio of poly(ethylene glycol)-co-peptide (approximately 18,000 g/mol) to heparin (approximately 18,000 g/mol) revealed a viscoelastic profile similar to that of concentrated, large molecular weight polymer solutions and melts. In addition, the biopolymer mixtures recovered quickly following thermal denaturation and mechanical insult. These gel-like materials were able to sequester exogenous heparin-binding peptides and could release these peptides over several days at rates dependent on relative heparin affinity. The initial release rates ranged from 3.3% per hour for a peptide with low heparin affinity to 0.025% per hour for a peptide with strong heparin affinity. By altering the affinity of peptides to heparin, a series of peptides can be developed to yield a range of release profiles useful for controlled in vivo delivery of therapeutics.     

l-Pantoyl lactone dehydrogenase from Rhodococcus erythropolis: genetic analyses and application to the stereospecific oxidation of l-pantoyl lactone

The 1,2-propanediol (1,2-PD) inducible membrane-bound L-pantoyl lactone (L-PL) dehydrogenase (LPLDH) has been isolated from Rhodococcus erythropolis AKU2103 (Kataoka et al. in Eur J Biochem 204:799, 1992). Based on the N-terminal amino acid sequence of LPLDH and the highly conserved amino acid sequence in homology search results, the LPLDH gene (lpldh) was cloned. The gene consists of 1,179 bases and encodes a protein of 392 amino acid residues. The deduced amino acid sequence showed high similarity to the proteins of the FMN-dependent α-hydroxy acid dehydrogenase/oxidase family. The overexpression vector pKLPLDH containing lpldh with its upstream region (1,940 bp) was constructed and introduced into R. erythropolis AKU2103. The recombinant R. erythropolis AKU2103 harboring pKLPLDH showed six times higher LPLDH activity than the wild-type strain. Conversion of L-PL to ketopantoyl lactone was achieved with 92% or 80% conversion yield when the substrate concentration was 0.768 or 1.15 M, respectively. Stereoinversion of L-PL to D-PL was also carried out by using the combination of recombinant R. erythropolis AKU2103 harboring pKLPLDH and ketopantoic acid-reducing Escherichia coli.