Production enhancement of Rhizopus arrhizus lipase by feeding oleic acid

A strategy for Rhizopus arrhizus lipase production enhancement by feeding oleic acid was developed. The oleic acid was proved to have strong inducing effect on lipase production, but high concentration oleic acid could repress lipase production. The decrease rate of oleic acid concentration using peanut oil as initial carbon source was figured out according to the change of oleic acid concentration in the fermentation broth. Our feeding strategy designed based on the decrease rate of oleic acid could avoid the repression of lipase production that is caused by high concentration of oleic acid in the fermenting liquor, and this strategy worked as a new feeding method showing excellent performance. The maximum lipase activity was gained by feeding dilute oleic acid every 12 h starting at 60 h, which maintained the oleic acid concentration around 18 mg/L, and the lipase activity was 31% higher than that of no feeding.     

Enhanced sophorolipid production by feeding-rate-controlled fed-batch culture

To develop the easier control method for fed-batch culture of sophorolipid production, we chose rapeseed oil as the most productive oil and compared their productivities in relation to different concentrations of glucose. The optimal concentration of glucose was 30 g/L for sophorolipid production. A fed-batch method was conducted using Candida bombicola ATCC 22214 with rapeseed oil as a secondary substrate. The feeding rate of rapeseed oil was dependent on pH and was calculated by the consumption rate of NaOH and rapeseed oil. The glucose concentration was constantly maintained between 30 and 40 g/L. As a result, we have produced a crude sophorolipid up to 365 g/L for 8 days through a feeding-rate-controlled fed-batch process.     

Continuous synthesis of alkyl ferulate by immobilized Candida antarctica lipase at high temperature

1-Pentyl, 1-hexyl and 1-heptyl ferulates were continuously synthesized at 60–90°C using a reactor system in which a column packed with ferulic acid powders and another column packed with immobilized Candida antarctica lipase particles were connected in series. Conversions greater than 0.9 were achieved for the synthesis of the 1-hexyl and 1-heptyl ferulates at 90°C. The system could be stably operated for the 1-heptyl ferulate synthesis at 90°C for at least two weeks.     

Enhanced yield of medium-chain-length polyhydroxyalkanoates from nonanoic acid by co-feeding glucose in carbon-limited, fed-batch culture

Medium-chain-length polyhydroxyalkanoates (MCL-PHAs) were produced in carbon-limited, single-stage, fed-batch fermentations of Pseudomonas putida KT2440 by co-feeding nonanoic acid (NA) and glucose (G) to enhance the yield of PHA from NA. An exponential (μ = 0.25 h⁻¹) followed by a linear feeding strategy at a NA:G ratio of 1:1 (w/w) achieved 71 g l⁻¹ biomass containing 56% PHA. Although the same overall PHA productivity (1.44 g l⁻¹ h⁻¹) was obtained when NA alone was fed at the same specific growth rate, the overall yield of PHA from NA increased by 25% (0.66 g PHA g NA⁻¹ versus 0.53 g g⁻¹) with glucose co-feeding. Further increasing glucose in the feed (NA:G = 1:1.5) resulted in a slightly higher yield (0.69 g PHA g NA⁻¹) but lower PHA content (48%) and productivity (1.16 g l⁻¹ h⁻¹). There was very little change in the PHA composition.     

Studies on a novel carbon source and cosolvent for lipase production by<Emphasis Type="Italic"> Candida rugosa</Emphasis>

Oleic acid esters were shown to be the best carbon source for both cell growth and lipase production by Candida rugosa. Use of a cosolvent, dodecane, in fermentations improved the solubility of solid substrates and increased oxygen solubility. This resulted in the highest lipase activity in batch fermentation with glycerol trioleate and dodecane. Lipase activity reached 77.1 units ml^–1.     

Capsaicin hydrolysis by Candida antarctica lipase

Capsaicin was hydrolysed by lipase B from Candida antarctica into vanillylamine and 8-methyl-6-trans-nonenoic acid. Conversions of 70% were obtained after 72 h at 70 °C in water but decreased to only 15% when capsaicin was solubilized in 15% (v/v) ethanol/water after 72 h at 45 °C. No activity occurred in chloroform/water mixtures. According to our knowledge, this is the first report concerning amide hydrolysis by a lipase.     

Agrocybe cylindracea lectin is a member of the galectin family

The complete amino acid sequence of Agrocybe cylindracea lectin was determined from the peptides obtained by chemical cleavages and enzymatic hydrolyses. The sequence shows 19.1% and 36.8% identity with those of human galectin-1 and Coprinus lectin-1, a fungal galectin, respectively. Seven residues, which are commonly found in carbohydrate recognizing domain (CRD) of galectins, were conserved. However, several insertions in the sequence, compared with those of human galectin-1 and Coprinus lectin-1, suggest that -strands S2, F3, and S4 and the loop structures between -strands F2 & S3 and F5 & S2 are different from those of galectins reported so far.     

Production of nattokinase by high cell density fed-batch culture of Bacillus subtilis

Bacillus subtilis was cultivated to high cell density for nattokinase production by pH-stat fed-batch culture. A concentrated mixture solution of glucose and peptone was automatically added by acid-supplying pump when culture pH rose above high limit. Effect of the ratio of glucose to peptone in feeding solution was investigated on cell growth and nattokinase production by changing the ratio from 0.2 to 5 g glucose/g peptone. The highest cell concentration was 77 g/L when the ratio was 0.2 g glucose/g peptone. Cell concentration decreased with increasing the ratio of glucose to peptone in feeding solution, while the optimum condition existed for nattokinase production. The highest nattokinase activity was 14,500 unit/mL at a ratio of 0.33 g glucose/g peptone, which was 4.3 times higher than that in batch culture.     

Production of extracellular lipase by Candida cylindracea CBS 6330

In this study we investigated the influences of aeration, substrate type and concentration on extracellular lipase production in a batch fermentor. The use of air enriched with pure oxygen is the most suitable for the lipase production. Additionally, we found that the presence of fats in the culture broth did not affect the value of the volumetric mass transfer coefficient of oxygen in our system. Olive oil or oleic acid was used as carbon sources. In both cases, the maximal specific rate of growth, μ_max, was the same but the highest activity was obtained when 10?g/dm³ of olive oil were used as an initial substrate concentration.     

Enhanced Resolution of a Secondary Alcohol by Hydrolysis of a Bichiral Ester Catalyzed by Lipase from Candida cylindracea

The effect of a chiral centre in the acyl group on the resolution of esters prepared from a racemic alcohol was investigated. R-2-chloropropionic acid afforded a higher enantiomeric ratio than S-2-chioropropionic acid in the hydrolysis of the corresponding esters of racemic 1-phenylethanol catalyzed by Candida cylindracea lipase. Even when a mixture of esters prepared from racemic acid and racemic alcohol was used for resolution of the alcohol, a noteworthy high enantioselectivity was observed. The hydrolysis of a bichiral ester offers an amplification in the resolution of enantiomers of alcohols by the combination of a chemical diastereoselectivity and an enzymatic enantio- and diastereoselectivity.     

Enzymatic synthesis of sialic acid derivative by immobilized lipase from Candida antarctica

The effects of important reaction parameters on the enhancement of sialic acid derivative lipophilic properties through the lipase-catalyzed esterification of N-acetyl neuraminic acid methyl ester are investigated in this study. It is found that the lipase Novozym 435 from Candida antarctica is particularly useful in the preparation of sialic acid methyl ester monononanoate (SAMEMN). The optimum temperature for the SAMEMN synthesis reaction using Novozym 435 is 60 °C, and nonanoic anhydride is found to be the best substrate among all acyl donors. The Novozym 435-catalyzed esterification of N-acetyl neuraminic acid methyl ester gave a maximum yield of 87.7% after 6 h in acetonitrile at 60 °C. Because the novel method developed is simple, yet effective, it could potentially be used industrially for the production of sialic acid derivatives.     

Enhanced Resolution of a Secondary Alcohol by Hydrolysis of a Bichiral Ester Catalyzed by Lipase from Candida cylindracea

The effect of a chiral centre in the acyl group on the resolution of esters prepared from a racemic alcohol was investigated. R-2-chloropropionic acid afforded a higher enantiomeric ratio than S-2-chioropropionic acid in the hydrolysis of the corresponding esters of racemic 1-phenylethanol catalyzed by Candida cylindracea lipase. Even when a mixture of esters prepared from racemic acid and racemic alcohol was used for resolution of the alcohol, a noteworthy high enantioselectivity was observed. The hydrolysis of a bichiral ester offers an amplification in the resolution of enantiomers of alcohols by the combination of a chemical diastereoselectivity and an enzymatic enantio- and diastereoselectivity.     

Aminolysis of 2-hydroxy esters catalyzed by Candida antarctica lipase

Candida antarctica lipase catalyzed the aminolysis of 2-hydroxy esters with amines in organic solvents to yield the corresponding 2-hydroxy amides. The reactions proceeded at 28–30 °C in dioxane for 6 h with 3 mM substrates with yields ranging between 45% (w/w) (for branched substrates) to 88% (w/w) (for linear substrates). Although the reaction was not enantioselective, because of its simplicity it represents an alternative method for the synthesis of functionalised amides.     

Assessment of olive-mill wastewater as a growth medium for lipase production by Candida cylindracea in bench-top reactor

Olive-mill wastewater (OMW) was investigated for its suitability to serve as a medium for lipase production by Candida cylindracea NRRL Y-17506. The OMW that best supported enzyme production was characterized by low COD and low total sugars content. In shake flask batch cultures, OMW supplementation with 2.4 g l⁻¹ NH₄Cl and 3 g l⁻¹ olive oil led to an enzyme activity of about 10 U ml⁻¹. The addition of glucose or malt extract and supplements containing organic N (e.g., peptone, yeast extract) either depressed or did not affect the enzyme production. Further experiments were then performed in a 3-l stirred tank reactor to assess the impact of medium pH and stirring speed on the yeast enzyme activity. The lipase activity was low (1.8 U ml⁻¹) when the pH was held constant at 6.5, significantly increased (18.7 U ml⁻¹) with uncontrolled pH and was maximum (20.4 U ml⁻¹) when the pH was let free to vary below 6.5. A stirring regime, that varied depending on the dissolved oxygen concentration in the medium, both prevented the occurrence of anoxic conditions during the exponential growth phase and enabled good lipase production (i.e., 21.6 U ml⁻¹) and mean volumetric productivity (i.e., 123.5 U l⁻¹ h⁻¹).     

Regioselective acylation of several polyhydroxylated natural compounds by Candida antarctica lipase B

Regioselective acylation of four polyhydroxylated natural compounds, deacetyl asperulosidic acid (1), asperulosidic acid (2), puerarin (3) and resveratrol (4) by Candida antarctica Lipase B in the presence of various acyl donors (vinyl acetate, vinyl decanoate or vinyl cinnamoate) was studied. Compounds 1, 2 and 4 were regioselectively acetylated with vinyl acetate to afford products, 3'-O-acetyl-10-O-deacetylasperulosidic acid (1a), 3',6'-O-diacetyl-10-O-deacetylasperulosidic acid (1b), 3'-O-acetylasperulosidic acid (2a), 3',6'-O-diacetylasperulosidic acid (2b), 4'-O-acetylresveratrol (4a), respectively, with yields of 22 to 50%, while reactions with vinyl decanoate and vinyl cinnamoate were slow with lower yields. Compound 3 was readily acylated with all three acyl donors and quantitatively converted to products 6'-O-acetylpuerarin (3a), 6'-O-decanoylpuerarin (3b), 6'-O-cinnamoylpuerarin (3c), respectively. The structures of these acylated products were determined by spectroscopic methods (MS and NMR).     

Regioselective acylation of several polyhydroxylated natural compounds by Candida antarctica lipase B

Regioselective acylation of four polyhydroxylated natural compounds, deacetyl asperulosidic acid (1), asperulosidic acid (2), puerarin (3) and resveratrol (4) by Candida antarctica Lipase B in the presence of various acyl donors (vinyl acetate, vinyl decanoate or vinyl cinnamoate) was studied. Compounds 1, 2 and 4 were regioselectively acetylated with vinyl acetate to afford products, 3′-O-acetyl-10-O-deacetylasperulosidic acid (1a), 3′,6′-O-diacetyl-10-O-deacetylasperulosidic acid (1b), 3′-O-acetylasperulosidic acid (2a), 3′,6′-O-diacetylasperulosidic acid (2b), 4′-O-acetylresveratrol (4a), respectively, with yields of 22 to 50%, while reactions with vinyl decanoate and vinyl cinnamoate were slow with lower yields. Compound 3 was readily acylated with all three acyl donors and quantitatively converted to products 6″-O-acetylpuerarin (3a), 6″-O-decanoylpuerarin (3b), 6″-O-cinnamoylpuerarin (3c), respectively. The structures of these acylated products were determined by spectroscopic methods (MS and NMR).     

Production of xylitol in cell recycle fermentations of Candida tropicalis

Xylitol was produced a in two-substrate, batch fermentation with cell recycling of Candida tropicalis ATCC 13803. A series of cell-recycle experiments showed that the feeding of xylose, glucose and yeast extract in the xylitol production phase was most effective in enhancing xylitol productivity. The optimized cell recycle fermentation resulted in 0.82 g xylitol/g xylose yield, 4.94 g xylitol l^–1 h^–1 productivity, and final xylitol concentration of 189 g l^–1. These results were 1.3 times higher in volumetric xylitol productivity and 2.2 times higher in final product concentration compared with the corresponding values of the optimized two-substrate batch culture.     

Carbon-limited fed-batch production of medium-chain-length polyhydroxyalkanoates from nonanoic acid by <Emphasis Type="Italic">Pseudomonas putida</Emphasis> KT2440

Pseudomonas putida KT2440 grew on glucose at a specific rate of 0.48 h⁻¹ but accumulated almost no poly-3-hydroxyalkanoates (PHA). Subsequent nitrogen limitation on nonanoic acid resulted in the accumulation of only 27% medium-chain-length PHA (MCL-PHA). In contrast, exponential nonanoic acid-limited growth (μ = 0.15 h⁻¹) produced 70 g l⁻¹ biomass containing 75% PHA. At a higher exponential feed rate (μ = 0.25 h⁻¹), the overall productivity was increased but less biomass (56 g l⁻¹) was produced due to higher oxygen demand, and the biomass contained less PHA (67%). It was concluded that carbon-limited exponential feeding of nonanoic acid or related substrates to cultures of P. putida KT2440 is a simple and highly effective method of producing MCL-PHA. Nitrogen limitation is unnecessary.     

Phytase production by high cell density culture of recombinant Bacillus subtilis

Bacillus subtilis BD170, harboring a plasmid pGT44[phyC] carrying the phytase gene (phyC) and a phosphate-depletion inducible pst-promoter, was grown in a 2 l bioreactor. Using a controlled feeding of glucose, high cell densities of 32 and 56 g dry cell weight l^–1 were achieved with peptone and yeast extract, respectively, as the complex nitrogen sources in a semi-defined growth medium. The fed-batch protocol was applied to production of recombinant phytase and a high extracellular phytase activity (48 U ml^–1) was reached with peptone. Although the yeast extract feeding resulted in a higher cell density, it was unsuitable as a medium component for phytase expression due to its relatively high phosphate content.     

Optimization of erythritol production by Candida magnoliae in fed-batch culture

A two-stage fed-batch process was designed to enhance erythritol productivity by the mutant strain of Candida magnoliae. The first stage (or growth stage) was performed in the fed-batch mode where the growth medium was fed when the pH of the culture broth dropped below 4.5. The second stage (or production stage) was started with addition of glucose powder into the culture broth when the cell mass reached about 75 g dry cell weight l⁻¹. When the initial glucose concentration was adjusted to 400 g l⁻¹ in the production stage, 2.8 g l⁻¹ h⁻¹ of overall erythritol productivity and 41% of erythritol conversion yield were achieved, which represented a fivefold increase in erythritol productivity compared with the simple batch fermentation process. A high glucose concentration in the production phase resulted in formation of organic acids including citrate and butyrate. An increase in dissolved oxygen level caused formation of gluconic acid instead of citric acid. Journal of Industrial Microbiology & Biotechnology (2000) 25, 100–103. Received 25 February 2000/ Accepted in revised form 08 June 2000