Quantitative analysis on inactivation and reactivation of recombinant glycerol dehydratase from Klebsiella pneumoniae XJPD-Li

The genes encoding glycerol dehydratase were cloned and characterized by genomic DNA from Klebsiella pneumoniae XJPD-Li, and the assigned accession number EF634063 was available from the GenBank database. The DNA sequence analysis showed that the clone included three ORFs (dhaB, dhaC and dhaE, encoding α, β and γ subunit of glycerol dehydratase, respectively). Among three subunits of glycerol dehydratase, amino acid residues H₁₃, S₁₉₃, N₃₅₉, E₄₀₇, and M₅₁₅ of α subunit, N₄₇, L₁₅₀, V₁₈₉ of β subunit are different with what had been reported. Subsequently, the expression vector was constructed and transformed into E. coli BL21, and the colony carried genes of glycerol dehydratase were selected. SDS-PAGE examination showed that the three subunits were well expressed. The specific activity of recombined glycerol dehydratase reached to 0.299 U mg^?1, which was about 3 times comparing with that of the wild strain. The research also displayed that both glycerol and O₂ could inactive the glycerol dehydratase expressed in E. coli quickly in 10 min. The inactivated glycerol dehydratase could be effectively reactivated under the system as follows: the concentration of ATP, Mg²⁺ and coenzyme B₁₂ were 50 mM, 10 mM and 3 μM, respectively, when the ratio (W/W) of glycerol dehydratase to reactivation factor was 4:1. The O₂-inactivated and glycerol-inactivated dehydratase could be reactivated to 97.3% and 98.9% of initial activity in 10 min in above-mentioned conditions, respectively. The reactivation factor together with ATP was considered as the “ON/OFF” reactivating condition.     

New integrated bioprocess for the continuous production,extraction and purification of lipopeptides produced by Bacillus subtilis in membrane bioreactor

Recently, a bubbleless membrane bioreactor (BMBR) has been successfully developed for biosurfactant production by Bacillus subtilis [1]. In this study, for the first time, continuous culture were carried out for the production of surfactin in a BMBR, both with or without a coupled microfiltration membrane. Results from continuous culture showed that a significant part of biomass was immobilized onto the air/liquid membrane contactor. Immobilized biomass activity onto the air/liquid membrane contactor was monitored using a respirometric analysis. Kinetics of growth, surfactin and primary metabolites production were investigated. Planktonic biomass, immobilized biomass and surfactin production and productivity obtained in batch culture (3 L) of 1.5 days of culture were 4.5 g DW, 1.3 g DW, 1.8 g and 17.4 mg L^?1 h^?1, respectively. In continuous culture without total cell recycling (TCR), the planktonic biomass was leached, but immobilized biomass reached a steady state at an estimated 6.6 g DW. 11.5 g of surfactin was produced after 3 days of culture, this gave an average surfactin productivity of 54.7 mg L^?1 h^?1 for the continuous culture, which presented a surfactin productivity of 30 mg L^?1 h^?1 at the steady state. TCR was then investigated for the continuous production, extraction and purification of surfactin using a coupled ultrafiltration step. In continuous culture with TCR at a dilution rate of 0.1 h^?1, planktonic biomass, immobilized biomass, surfactin production and productivity reached 7.5 g DW, 5.5 g DW, 7.1 g and 41.6 mg L^?1 h^?1 respectively, after 2 days of culture. After this time, biomass and surfactin productions stopped. Increasing dilution rate to 0.2 h^?1 led to the resumption of biomass and surfactin production and these values reached 11.1 g DW, 10.5 g DW, 7.9 g and 110.1 mg L^?1 h^?1, respectively, after 3 days of culture. This study has therefore shown that with this new integrated bioprocess, it was possible to continuously extract and purify several grams of biosurfactant, with purity up to 95%.     

The effect of dietary l-carnitine supplementation on cold tolerance and growth of the ornamental cichlid fish Pelvicachromis pulcher—preliminary results

The effect of dietary l-carnitine supplementation on cold tolerance, growth and survival of the ornamental cichlid Pelvicachromis pulcher was tested under laboratory conditions. Fish were reared for a period of 82 days on a diet containing different levels of added l-carnitine: 0, 500 (3.1 mmol), 1000 (6.2 mmol) and 2000 (12.4 mmol) mg/kg. At the end of the growth period the fish were exposed to a cold shock. Fish which received dietary l-carnitine supplementation (at all tested levels) exhibited significantly better survival rates following exposure to a cold shock, and readapted quicker to normal temperatures compared to the control group which had no l-carnitine added to their diet. The addition of l-carnitine to the diet at a level of 1000 mg/kg seems to yield the best protection against exposure to cold shock.Growth differences among the treated fish were not significant, although the fish which received 500 mg/kg supplementation exhibited slightly better growth.     

Continuous production of selenomethionine-enriched Chlorella sorokiniana biomass in a photobioreactor

This article describes the enrichment of the fresh-water green microalga Chlorella sorokiniana in selenomethionine (SeMet). The microalga was cultivated in a 2.2 L glass-vessel photobioreactor, in a culture medium supplemented with selenate (SeO₄^2?) concentrations ranging from 5 to 50 mg L^?1. Although selenate exposure lowered culture viability, C. sorokiniana grew well at all tested selenate concentrations, however cultures supplemented with 50 mg L^?1 selenate did not remain stable at steady state. A suitable selenate concentration in fresh culture medium for continuous operation was determined, which allowed stable long-term cultivation at steady state and maximal SeMet productivity. In order to do that, the effect of dilution rate on biomass productivity, viability and SeMet content of C. sorokiniana at several selenate concentrations were determined in the photobioreactor. A maximal SeMet productivity of 21 μg L^?1 day^?1 was obtained with 40 mg L^?1 selenate in the culture medium. Then a continuous cultivation process at several dilution rates was performed at 40 mg L^?1 selenate obtaining a maximum of 246 μg L^?1 day^?1 SeMet at a low dilution rate of 0.49 day^?1, calculated on total daily effluent volume. This paper describes for the first time an efficient long-term continuous cultivation of C. sorokiniana for the production of biomass enriched in the high value amino acid SeMet, at laboratory scale.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Continuous 2-keto-gluconic acid (2KGA) production from corn starch hydrolysate by Pseudomonas fluorescens AR4

A continuous fermentation process for 2-keto-gluconic acid (2KGA) production from cheap raw material corn starch hydrolysate was developed using the strain Pseudomonas fluorescens AR4. The dilution rate and feeding glucose concentration had a significant effect on the cell concentrations, glucose utilization and 2KGA production performance. The optimal operating factors were obtained as: 0.065 h⁻¹ of dilution rate, 180 g/L of feeding glucose concentration, and 16 h of batch fermentation time as the starting point. Under these conditions, the steady state had the 135.92 g/L of produced 2KGA concentration, 8.83 g/L.h of average volumetric productivity, and 0.9510 g/g of yield. In conclusion, the proposed efficient and stable continuous fermentation process for 2KGA production by the strain P. fluorescens AR4 is potentially competitive for industrial production from corn starch hydrolysate in terms of 2KGA productivity and yield.     

Analysis of Escherichia coli cell state by flow cytometry during whole cell catalyzed biotransformation for l-carnitine production

Flow cytometry was used to monitor Escherichia coli cellular state during the biotransformation of crotonobetaine into l-carnitine using growing and resting cells in batch and high-cell-recycle continuous membrane reactors. The cell physiological state and the DNA, RNA and protein cell content were analyzed during the bioprocess. The cell growth cycle was followed by reference to cellular DNA concentration and the entry in the stationary phase resulted in an increase in intracellular protein. The biochemical activity of resting cells was assessed for the first time at the molecular level, protein synthesis being observed despite the absence of nutrients. Freely suspended growing, both in batch and continuous cultures, and, more importantly, resting E. coli cells were seen to be made up of subpopulations differing in reproductive ability, metabolic activity and membrane integrity. In the case of growing cells, biotransformation was mostly performed by fully viable cells (68–75%), while in a resting cell system, also dead cells (1–5%) and cells with doubtful viability (60–70%) appeared to be involved in the process; in later stages, a population made up of phantom cells, containing little or no cellular DNA, was detected. In cell-recycle continuous reactors, the recording of DNA (40 to 60 fg), RNA (50 to 120 fg) and protein (100 to 220 fg) levels per unit of cell, and the evolution of cell population heterogeneity (three different populations of cells) threw light on the stress conditions imposed by high cell densities. The use of FCM allowed to follow the recovery of cell catalytic activity for resting biotransformation batch processes, thus showing its potential for the optimization of bioprocesses.     

An annual cycle of biomass and productivity of Vallisneria americana in a subtropical spring-fed estuary

An annual cycle of biomass and productivity of wild celery (Vallisneria americana) was studied in Kings Bay, FL, USA. In situ growth rates were measured monthly between March 2001 and June 2002 in high-density stands, using a modified hole-punching technique, and applied to shoot density data to obtain areal estimates of production. Mean shoot density varied greatly over the study period, ranging between 200 and 800 shoots m⁻². Mean total biomass ranged between 162 and 1013 g m⁻², with aboveground material comprising, on average, 70% of total biomass. Total annual estimated production of new attached shoots was 519 g m⁻². Leaf growth rates peaked at >50 mg shoot⁻¹ d⁻¹, and mass-specific leaf growth ranged 0.6–1.8% d⁻¹. Annually, individual shoots produced 7.4 g of leaf material and completely replaced standing leaf biomass 3.5 times. Areal leaf production was highest in late spring/summer of 2001, and ranged between 3.6 and 23.0 g m⁻² d⁻¹. Annual total leaf production was 2704 g m⁻². Seasonality was not apparent in most variables monitored monthly; only 1 of the 64 relationships we examined between environmental variables (nutrients, chlorophyll a, and irradiance) and Vallisneria biological variables were significant, with relative growth rate increasing linearly with irradiance. Peak biomass and productivity of Vallisneria in Kings Bay were high compared to literature values for other Vallisneria populations as well as global averages for well-studied seagrasses, emphasizing the potential importance of Vallisneria to whole ecosystem functioning in springs, lakes, and oligohaline reaches of many estuaries.     

Poly(3-hydroxybutyrate) production by Cupriavidus necator using waste glycerol

Polyhydroxyalkanoates (PHAs) have been recognized as good substitutes for the non-biodegradable petrochemically produced polymers. However, their high (real or estimated) current production cost limits their industrial applications. This work exploits two strategies to enhance PHAs substitution potential: the increase in PHA volumetric productivity in high density cultures and the use of waste glycerol (GRP), a by-product from the biodiesel industry, as primary carbon source for cell growth and polymer synthesis. Cupriavidus necator DSM 545 was used to accumulate poly(3-hydroxybutyrate) (P(3HB)) from GRP and from commercial glycerol (PG) as control substrate. On PG, productivities between 0.6 g_PHB L^?1 h^?1 and 1.5 g_PHB L^?1 h^?1 were attained. The maximum cell DW was 82.5 g_DW L^?1, the P(3HB) content being 62%. When GRP was used, 68.8 g_DW L^?1 with a P(3HB) accumulation of 38% resulting in a final productivity of 0.84 g_PHB L^?1 h^?1 was obtained. By decreasing the biomass concentration at which accumulation was triggered, a productivity of 1.1 g_PHB L^?1 h^?1 (50% P(3HB), w/w) was attained using GRP. P(3HB) molecular weights (M_w) ranged from 7.9 × 10⁵ to 9.6 × 10⁵ Da.     

Enhanced ethanol production by continuous fermentation in a two-tank system with cell recycling

An experimental method for producing ethanol continuously was designed and tested with a cell-recycling two-tank system, which was composed of two fermentors, each of which was individually equipped with a settler for recycling flocculent yeast. This system was effective for the continuous fermentation of ethanol from sucrose at high cell-recycling (r = 0.8–0.9) and dilution (up to 0.48 h^?1) rates. The system has several advantages; the high cell concentration in the fermentors and relief of substrate and product inhibition. Thus, the enhanced productivity using this continuous fermentation with the two-tank cell-recycling system was significantly higher compared with that of the batch fermentation. The results indicate that increased recycling ratios caused an increase in biomass concentration and subsequently, product concentration in the tank. The ethanol productivity increased with the dilution rate, but higher dilution rates could render increasing amounts of sugar unconverted. Continuous fermentation with the sugar feed concentration of 160 g/l at r = 0.9 and dilution rate of 0.2 h^?1 achieved the highest productivity with less than 2% of the unconverted sugar in the product steam. Under the same cell recycling ratios a productivity range of 6.9–7.5 g/l h^?1 could be achieved with feeding concentrations of 80–200 g/l, while batch fermentation at these sugar concentrations led to productivities of 3.85–4.48 g/l h^?1.     

Effect of orally administered l-carnitine on selected biochemical indicators of lactating Tuj-ewes

The effect of orally administered l-carnitine on biochemical parameters was examined in lactating Tuj-ewes. Ewes were orally given 500 mg of l-carnitine daily for 3 weeks. To evaluate the changes on selected blood indicators (total protein, albumin, glucose, triglyceride, cholesterol, urea, aspartate amino transferase, alanine amino transferase, lipase, triiodothyronine and thyroxine), blood samples were collected at the beginning of the study, and at the end of 1st, 2nd and 3rd week of study. Oral administration of supplemental carnitine significantly decreased serum triglyceride (P < 0.05), glucose (P < 0.05), cholesterol (P < 0.05) and triiodothyronine (P < 0.05) concentrations. In addition, serum thyroxine (P < 0.001) and albumin (P < 0.01) concentrations were significantly elevated as a result of oral carnitine treatment. These results suggest that supplemental l-carnitine improves selected biochemical indicators in Tuj-ewes.     

Methanol vapor biofiltration coupled with continuous production of recombinant endochitinase Ech42 by Pichia Pastoris

Methanol biofiltration using methylotrophic microorganisms has been previously reported by various authors. In a previous study, a modified strain of Pichia pastoris was tested for the ability to produce endochitinase (Ech42) when coupled with methanol vapor biodegradation in batch tests. The next challenge was to validate the process in a continuous system. Thus, in the present study, a biofilter packed with perlite and inoculated with P. pastoris transformed with the plasmid pPIC-ech42 was used for methanol vapor biofiltration and the continuous production of recombinant endochitinase (Ech42) for 60 days. The maximum elimination capacity (EC) of methanol obtained was 1320 g m^?3 h^?1 at a loading rate of 1465 g m^?3 h^?1. The extracellular protein production rate in the leachate was 2360 μg h^?1 with a chitinase enzymatic activity of 123 U L^?1. The protein content on the biofilm samples was negligible, indicating the effectiveness of the overall process and of P. pastoris to excrete proteins. The carbon balance indicated that 81% of the consumed methanol was mineralized and 5.8% was incorporated into biomass. The results of this study and the economic balance underscore the promising application of linking methanol vapor biofiltration to the continuous production of recombinant proteins.     

The effect of dietary supplementation with calcium salts of long chain fatty acids and/or l-carnitine on ovarian activity of Rahmani ewes

This study investigated the effect of dietary supplementation with calcium salts of long chain fatty acids with or without of l-carnitine on ovarian activity using 24 Rahmani ewes randomly allocated to four treatments. Control animals (n = 6) were fed a basal diet of hay (64.2%) and barley grain (35.0%) plus minerals and vitamins (0.8%). Ewes on the three treatments received the same basal diet supplemented with calcium salts of long chain fatty acids (CSFA) at 3% of the basal diet dry matter intake (1.4 kg/ewe/d); 250 ppm l-carnitine (LC); or both these supplements (CSFA + LC). All use exhibited natural estrus on one or two occasions and were weighed at the start and the end of the study as well as body condition score was assessed at the end of study. All ewes were then synchronised for estrus using intravaginal sponges for 12 d prior to the start of the nutritional treatments and three weeks after the nutritional treatments began. The nutritional treatments were imposed for a total of 8 weeks. Blood samples were collected prior to the start of treatments and every two weeks thereafter except after sponge removal of first and second synchronisation where the blood samples were collected daily for progesterone assay. The results revealed that Rahmani ewes received basal diet (control) and l-carnitine had significantly decrease final body weight and body condition score (36.3 ± 0.4; 36.8 ± 0.3; 2.2 ± 0.04; 2.1 ± 0.05; p < 0.05, respectively) than those on CSFA and CSFA + LC (38.6 ± 0.9; 39.5 ± 0.6; 3.3 ± 0.07; 3.4 ± 0.06; respectively). At the second ultrasound examination, the control animals had significantly fewer total follicles (7.3 ± 0.8; p < 0.05) than those on the CSFA (8.4 ± 0.8), l-carnitine (8.7 ± 1.5) and CSFA + LC (8.0 ± 0.6) treatments. The increased numbers occurred in the medium and large categories of follicles. In addition, the ovulation rates were significantly lower (p < 0.05) for control (1.3 ± 0.2) and l-carnitine (1.5 ± 0.00) than for CSFA (2.5 ± 0.3) and CSFA + LC (2.3 ± 0.2). Furthermore, serum progesterone concentrations had risen and were significantly higher (p < 0.05) for CSFA (2.5 ± 0.3 ng/ml) and CSFA + LC (2.7 ± 0.1 ng/ml) than for control (1.1 ± 0.7 ng/ml) and l-carnitine (1.5 ± 0.4 ng/ml). It was concluded that supplementation of the basal diet with l-carnitine alone did not improve performance of ewes or the ovarian response. However, the addition of calcium salts of long chain fatty acids to the basal diet alone or in combination with l-carnitine significantly improved the number and size of ovarian preovulatory follicles, and the ovulation rate of Rahmani ewes. Further evidence was required to study their influence on follicular atresia.     

Simplified feeding strategies for fed-batch cultivation of Kluyveromyces marxianus in cheese whey

The present work reports the effect of simple feeding strategies to obtain high-cell-density cultures of Kluyveromyces marxianus maximizing β-galactosidase productivity using cheese whey as basic medium. Linear and exponential feeding strategies, with feeding times of 20, 25 and 35 h, and three different feeding media concentrations (140 g/L, 210 g/L, and 280 g/L lactose concentration), were tested. Final biomass concentration reached 35 g cells dry weight/L and our results showed that continuous lactose addition to culture were able to produce high specific enzyme activities, consequently improving volumetric activities of β-galactosidase when compared to batch cultivations. The best fed-batch strategy, which was the feeding of three-fold lactose concentration in the cheese whey-medium during 25 h, resulted in β-galactosidase productivity of 291 U/L h, representing an increase of more than 50% compared to batch cultivations.     

Evaluation of distant carbon sources in biosurfactant production by a gamma ray-induced Pseudomonas putida mutant

Pseudomonas putida 33 wild strain, subjected to gamma ray mutagenesis and designated as P. putida 300-B mutant was used as microbial rhamnolipid-producer by using distant carbon sources (viz. hydrocarbons, waste frying oils ‘WFOs’, vegetable oil refinery wastes and molasses) in the minimal media under shake flask conditions. The behavior of glucose as co-substrate and growth initiator was examined. The 300-B mutant strain showed its ability to grow on all the substrates tested and produced rhamnolipid surfactants to different extents however; soybean and corn WFOs were observed to be preferred carbon sources followed by kerosene and paraffin oils, respectively. The best cell biomass (3.5 g l⁻¹) and rhamnolipids yield (4.1 g l⁻¹) were obtained with soybean WFO as carbon source and glucose as growth initiator under fed-batch cultivation showing an optimum specific growth rate (μ) of 0.272 h⁻¹, specific product yield (q_p) of 0.318 g g⁻¹ h and volumetric productivity (P_V) of 0.024 g l⁻¹ h. The critical micelle concentration of its culture supernatant was observed to be 91 mg rhamnolipids l⁻¹ and surface tension as 31.2 mN m⁻¹.     

Fermentation process for continuous production of succinic acid in a fibrous bed bioreactor

Succinic acid (SA) was produced from Actinobacillus succinogenes with high cell density by continuous fermentation using fibrous bed bioreactor (FBB). The effects of feeding glucose concentration, dilution rate, and pH on continuous production of SA were examined to achieve an efficient and economical bioprocess. The optimum feeding glucose concentration, dilution rate, and pH were 80 g/L, 0.05 1/h, and 6.0–6.5, respectively. A SA concentration of 55.3 ± 0.8 g/L, productivity of 2.77 ± 0.04 g/L/h, and yield of 0.8 ± 0.02 g/g were obtained, and the continuous fermentation exhibited long-term stability for as long as 18 days (440 h) with no obvious fluctuations in both SA and biomass levels. The Jerusalimsky equation for the specific rate of SA production presented the inhibition phenomenon of the product, demonstrating that 60 g/L SA might be a critical concentration in this continuous FBB system. The results obtained could be beneficial for future fermentor designs and improvements in SA production.     

Effects of pellet morphology on broth rheology in fermentations of Aspergillus terreus

Effects of pellet morphology on broth rheology are reported for pelleted submerged cultures of the lovastatin producing filamentous fungus Aspergillus terreus, growing in fluidized bed and stirred tank bioreactors. The pellet diameter and compactness were affected by the agitation intensity of the broth; however, the total biomass productivity was not affected. In fluidized beds and stirred tanks with agitation intensity of up to 300 rpm (impeller tip speed of 1.02 m s⁻¹), the fungal pellets were stable at diameters of up to about 2300 μm. In more intensely agitated stirred tanks (≥600 rpm; impeller tip speed of ≥2.03 m s⁻¹), the stable pellet size was only about ≤900 μm. The biomass concentration and the pellet diameter were the main factors that influenced the flow index and the consistency index of the power-law broths. Because the biomass productivity was the same in all experiments in a given type of reactor and the oxygen concentration was kept at ∼400% of air saturation, the pellet size and morphology were not influenced by oxygen mass transfer effects. Pellets were always dense in the core region and no necrosis of the biomass occurred.     

Production of l-phenylalanine from glucose by metabolic engineering of wild type Escherichia coli W3110

The market of l-phenylalanine has been stimulated by the great demand for the low-calorie sweetener aspartame. In this paper, the effects of pivotal genes on l-phenylalanine production were evaluated by metabolic engineering of wild type Escherichia coli. The bifunctional PheA protein contains two catalytic domains (chorismate mutase and prephenate dehydratase activities) as well as one R-domain (for feedback inhibition by l-phenylalanine). The catalytic domain of PheA was overexpressed to increase l-phenylalanine production. It was firstly indicated that this domain could enhance the metabolic influx to overproduce l-phenylalanine and improve the survival ability under m-Fluoro-dl-phenylalanine stress. Furthermore, the fermentation performance of aroG feedback inhibition resistant mutants was firstly compared, aroG29 and aroG15 increased the l-phenylalanine concentration by 5-fold. After that the expression of aroK and ydiB was also elevated, and the l-phenylalanine yield on cell (0.79 g/g) and maximum l-phenylalanine productivity (0.073 g/L/h) were subsequently doubled. Meanwhile, the l-phenylalanine yield on glucose increased from 0.124 g/g to 0.153 g/g. It was found that genes ydiB and aroK could elevate the l-phenylalanine yield and productivity and shorten the lag phase.     

Inhibition of serine and proline racemases by substrate-product analogues

d-Amino acids can play important roles as specific biosynthetic building blocks required by organisms or act as regulatory molecules. Consequently, amino acid racemases that catalyze the formation of d-amino acids are potential therapeutic targets. Serine racemase catalyzes the reversible formation of d-serine (a modulator of neurotransmission) from l-serine, while proline racemase (an essential enzymatic and mitogenic protein in trypanosomes) catalyzes the reversible conversion of l-proline to d-proline. We show the substrate-product analogue α-(hydroxymethyl)serine is a modest, linear mixed-type inhibitor of serine racemase from Schizosaccharomyces pombe (K_i = 167 ± 21 mM, K_i′ = 661 ± 81 mM, cf. K_m = 19 ± 2 mM). The bicyclic substrate-product analogue of proline, 7-azabicyclo[2.2.1]heptan-7-ium-1-carboxylate is a weak inhibitor of proline racemase from Clostridium sticklandii, giving only 29% inhibition at 142.5 mM. However, the more flexible bicyclic substrate-product analogue tetrahydro-1H-pyrrolizine-7a(5H)-carboxylate is a noncompetitive inhibitor of proline racemase from C. sticklandii (K_i = 111 ± 15 mM, cf. K_m = 5.7 ± 0.5 mM). These results suggest that substrate-product analogue inhibitors of racemases may only be effective when the active site is capacious and/or plastic, or when the inhibitor is sufficiently flexible.     

Tween 80 influences the production of intracellular lipase by Schizochytrium S31 in a stirred tank reactor

Marine microorganisms are a potential source of enzymes with structural stability, high activity at low temperature and unique substrate selectivity. Thraustochytrids are marine heterotrophic microbes, well known for the production of omega-3 fatty acids. In this study the effect of Tween 80 as a carbon source was investigated with regard to biomass, lipase and lipid productivity in Schizochytrium sp. S31. Tween 80 (1%) and 120 h of incubation were the optimum condition period for biomass, lipid and lipase productivity in a stirred tank reactor. The yields obtained were 0.9 g L⁻¹ of biomass, 300 mg g⁻¹ of lipid and 39 U/g of lipase activity. Sonication was optimised in terms of time and acoustic power to maximise the yield of extracted lipase. The extracted lipase from Schizochytrium S31 was observed to hydrolyse long chain polyunsaturated fatty acids DHA and EPA.