Effect of culture pH on recombinant antibody production by a new human cell line, F2N78, grown in suspension at 33.0 °C and 37.0 °C

The human host cell line, F2N78, is a new somatic hybrid cell line designed for therapeutic antibody production. To verify its potential as a human host cell line, recombinant F2N78 cells that produce antibody against rabies virus (rF2N78) were cultivated at different culture pH (6.8, 7.0, 7.2, 7.4, and 7.6) and temperatures (33.0 °C and 37.0 °C). Regardless of the culture temperature, the highest specific growth rate was obtained at a pH of 7.0–7.4. Lowering the culture temperature from 37.0 °C to 33.0 °C suppressed cell growth while allowing maintenance of high cell viability for a longer period. However, it did not enhance antibody production because specific antibody productivity did not increase at 33.0 °C. The highest maximum antibody concentration was obtained at 37.0 °C and pH 6.8. The N-linked glycosylation of the antibody was affected by the culture pH rather than the temperature. Nevertheless, G1F was dominant and G2F occupied a larger portion than G0F in all culture conditions. Compared to the same antibody produced from recombinant CHO cells, the antibody produced from rF2N78 cells has more galactose capping and was more similar to human plasma IgG. Taken together, the results obtained here demonstrate the potential of F2N78 as an alternative human host cell line for therapeutic antibody production.     

A novel isolate of <Emphasis Type="Italic">Clostridium butyricum</Emphasis> for efficient butyric acid production by xylose fermentation

Bacterial fermentation of lignocellulose has been regarded as a sustainable approach to butyric acid production. However, the yield of butyric acid is hindered by the conversion efficiency of hydrolysate xylose. A mesophilic alkaline-tolerant strain designated as Clostridium butyricum B10 was isolated by xylose fermentation with acetic and butyric acids as the principal liquid products. To enhance butyric acid production, performance of the strain in batch fermentation was evaluated with various temperatures (20–47 °C), initial pH (5.0–10.0), and xylose concentration (6–20 g/L). The results showed that the optimal temperature, initial pH, and xylose concentration for butyric acid production were 37 °C, 9.0, and 8.00 g/L, respectively. Under the optimal condition, the yield and specific yield of butyric acid reached about 2.58 g/L and 0.36 g/g xylose, respectively, with 75.00% butyric acid in the total volatile fatty acids. As renewable energy, hydrogen was also collected from the xylose fermentation with a yield of about 73.86 mmol/L. The kinetics of growth and product formation indicated that the maximal cell growth rate (μ _m ) and the specific butyric acid yield were 0.1466 h^?1 and 3.6274 g/g cell (dry weight), respectively. The better performance in xylose fermentation showed C. butyricum B10 a potential application in efficient butyric acid production from lignocellulose.     

Significances of pH and temperature on the production of heat-shock protein glycoprotein 96 by MethA tumor cell suspension culture in stirred-tank bioreactors

Heat-shock protein, glycoprotein 96 (gp96), elicits both innate and adaptive immune responses against tumors or viral infections. In our laboratory, MethA tumor cell suspension culture process has been recently developed for gp96 production in spinner flask. In this work, significances of pH and temperature on the novel bioprocess were studied in stirred-tank bioreactor. Lowering of culture pH and temperature led to a significant reduction of average specific growth rate but cell viability remained high for a prolonged cultivation time resulting in a higher integral of viable cells. Both the maximal viable cell density and gp96 production were attained at a pH of 7.0. Interestingly, gp96 production was increased above and below 37 °C, presumably because gp96 biosynthesis was induced when MethA tumor cell underwent heat or cold. For MethA tumor cell growth 37 °C was desirable, while gp96 production and productivity was obtained at their peak values at 40 °C. The results of this work might be useful to scale-up the bioprocess into the pilot scale.     

Improving arachidonic acid fermentation by Mortierella alpina through multistage temperature and aeration rate control in bioreactor

Effective production of arachidonic acid (ARA) using Mortierella alpina was conducted in a 30-L airlift bioreactor. Varying the aeration rate and temperature significantly influenced cell morphology, cell growth, and ARA production, while the optimal aeration rate and temperature for cell growth and product formation were quite different. As a result, a two-stage aeration rate control strategy was constructed based on monitoring of cell morphology and ARA production under various aeration rate control levels (0.6–1.8 vvm). Using this strategy, ARA yield reached 4.7 g/L, an increase of 38.2% compared with the control (constant aeration rate control at 1.0 vvm). Dynamic temperature-control strategy was implemented based on the fermentation performance at various temperatures (13–28°C), with ARA level in total cellular lipid increased by 37.1% comparing to a constant-temperature control (25°C). On that basis, the combinatorial fermentation strategy of two-stage aeration rate control and dynamic temperature control was applied and ARA production achieved the highest level of 5.8 g/L.     

Production and biochemical characterization of a novel cellulase-poor alkali-thermo-tolerant xylanase from <Emphasis Type="Italic">Coprinellus disseminatus</Emphasis> SW-1 NTCC 1165

Fungi producing xylanases are plentiful but alkali-thermo-tolerant fungi producing cellulase-poor xylanase are rare. Out of 12 fungal strains isolated from various sources, Coprinellus disseminatus SW-1 NTCC 1165 yielded the highest xylanase activity (362.1 IU/ml) with minimal cellulase contamination (0.64 IU/ml). The solid state fermentation was more effective yielding 88.59% higher xylanase activity than that of submerged fermentation. An incubation period of 7 days at 37°C and pH 6.4 accelerated the xylanase production up to the maximum level. Among various inexpensive agro-residues used as carbon source, wheat bran induced the maximum xylanase titres (469.45 IU/ml) while soya bean meal was the best nitrogen source (478.5 IU/ml). A solid substrate to moisture content ratio of 1:3 was suitable for xylanase production while xylanase titre was repressed with the addition of glucose and lactose. The xylanase and laccase activities under optimized conditions were 499.60 and 25.5 IU/ml, respectively along with negligible cellulase contamination (0.86 IU/ml). Biochemical characterization revealed that optimal xylanase activity was observed at pH 6.4 and temperature 55°C and xylanase is active up to pH 9 (40.33 IU/ml) and temperature 85°C (48.81 IU/ml). SDS–PAGE and zymogram analysis indicated that molecular weight of alkali-thermo-tolerant xylanase produced by C. disseminatus SW-1 NTCC 1165 was 43 kDa.     

Enhancement of polysialic acid yield by reducing initial phosphate and feeding ammonia water to <Emphasis Type="Italic">Escherichia coli</Emphasis> CCTCC M208088

Polysialic acid (PSA) is a capsular polysaccharide obtained from aerobic fermentation with Escherichia coli. To enhance PSA production and eliminate the influence of phosphate on the PSA purification process, a lower level of initial phosphate was adopted with pH control. The resulting PSA yield reached 4.1 g/L in fed-batch fermentation with 2.5 g/L K₂HPO₄ and E. coli strain CCTCC M208088. In addition, an ammonia water (NH₄OH) feeding strategy to control the pH at 6.4 was developed resulting in PSA production that reached as high as 5.2 g/L. NMR spectra confirmed the purified biopolymer as a α-2,8 linked PSA, identical to the published NMR spectra, with a molecular weight in the range of 16 ∼ 50 kDa.     

Optimization of Fermentation Conditions for Phytase Production by Two Strains of Bacillus licheniformis (LF1 and LH1) Isolated from the Intestine of Rohu, Labeo rohita (Hamilton)

The culture conditions for extracellular production of phytase by two strains of Bacillus licheniformis (LF1 and LH1) isolated from the proximal and distal intestine of rohu (Labeo rohita) were optimized to obtain maximum level of phytase. Both the strains were cultured TSA broth for 24 h at 37 ± 2 °C, when average viable count of 9.75 × 10⁷ cells ml^?1 culture broth was obtained. This was used as the inoculum for the production medium. Sesame (Sesamum indicum) oilseed meal was used as the source of phytic acid (substrate). The effects of moisture, pH, temperature, fermentation period, inoculum size, different nitrogen sources, vitamins and surfactants on phytase production by these two strains were evaluated. Phytase yield was highest (1.87 U in LF1 and 1.57 U in LH1) in solid-state fermentation. Enzyme production in both the isolates increased in an optimum pH range of 5.5–6.5. Minimum phytase production was observed at 50 °C, while maximum production was obtained at 40 °C. To standardize the fermentation period for phytase production, production rate was measured at 12-h intervals up to 120 h. Enzyme production increased for 72 h of fermentation in both strains, and decreased thereafter. The enzyme production increased with increased inoculum size up to 3.0 percentage points for the strain LF1 and up to 2.0 % for the strains LH1. Ammonium sulphate as the nitrogen source was most effective in LF1, while beef extract proved useful to maximize enzyme production by LH1.     

Influence of pH and temperature on the expression of sboA and ituD genes in Bacillus sp. P11

Temperature and pH are key factors influencing the production of antimicrobial peptides. In this work, qRT-PCR methodology was used to demonstrate the effect of these two variables on sboA (subtilosin A) and ituD (iturin A) expression in Bacillus sp. P11, an isolate from aquatic environment of the Amazon. Bacillus sp. P11 was incubated in BHI broth for 36 h at 30, 37 and 42 °C, and the pH values were 6.0, 7.4 and 8.0. The production of subtilosin A and iturin A was confirmed by mass spectrometry. The sboA expression increased 200-fold when the initial pH was 8.0. In contrast, ituD expression was maximum at pH 6.0. Increased temperature (42 °C) was adverse for both genes, but ituD expression increased at 37 °C. Expression of sboA and ituD was strongly affected by pH and temperature and qRT-PCR proved to be a powerful tool to investigate the potential of Bacillus strains to produce subtilosin A and iturin A.     

Effect of two-stage temperature on pullulan production by Aureobasidium pullulans

The effect of a two-stage cultivation temperature on the production of pullulan synthesized by Aureobasidium pullulans CGMCC1234 was investigated. Pullulan production was affected by temperature; although the optimum temperature for pullulan production was 26°C, the optimal temperature for cell growth was 32°C. Maximum pullulan production was achieved by growing A. pullulans in a first stage of 32°C for 2 days, and then in a second stage of 26°C for 2 days. Pullulan production using these two-stage temperatures significantly increased: about 27.80% (w/w) compared to constant-temperature fermentation (26°C for 4 days). The morphology of the A. pullulans (CGMCC 1234) was also affected by temperature; the lower temperature (26°C) supported unicellular biomass growth. Results of this study indicate that fermentation using two temperature stages is a promising method for pullulan production.     

High temperature stimulates acetic acid accumulation and enhances the growth inhibition and ethanol production by Saccharomyces cerevisiae under fermenting conditions

Cellular responses of Saccharomyces cerevisiae to high temperatures of up to 42 °C during ethanol fermentation at a high glucose concentration (i.e., 100 g/L) were investigated. Increased temperature correlated with stimulated glucose uptake to produce not only the thermal protectant glycerol but also ethanol and acetic acid. Carbon flux into the tricarboxylic acid (TCA) cycle correlated positively with cultivation temperature. These results indicate that the increased demand for energy (in the form of ATP), most likely caused by multiple stressors, including heat, acetic acid, and ethanol, was matched by both the fermentation and respiration pathways. Notably, acetic acid production was substantially stimulated compared to that of other metabolites during growth at increased temperature. The acetic acid produced in addition to ethanol seemed to subsequently result in adverse effects, leading to increased production of reactive oxygen species. This, in turn, appeared to cause the specific growth rate, and glucose uptake rate reduced leading to a decrease of the specific ethanol production rate far before glucose depletion. These results suggest that adverse effects from heat, acetic acid, ethanol, and oxidative stressors are synergistic, resulting in a decrease of the specific growth rate and ethanol production rate and, hence, are major determinants of cell stability and ethanol fermentation performance of S. cerevisiae at high temperatures. The results are discussed in the context of possible applications.     

Fermentation production of keratinase from Bacillus licheniformisPWD-1 and a recombinant B. subtilis FDB-29

Bacillus licheniformis PWD-1, the parent strain, and B. subtilis FDB-29, a recombinant strain. In both strains, keratinase was induced by proteinaceous media, and repressed by carbohydrates. A seed culture of B. licheniformis PWD-1 at early age, 6–10 h, is crucial to keratinase production during fermentation, but B. subtilis FDB-29 is insensitive to the seed culture age. During the batch fermentation by both strains, the pH changed from 7.0 to 8.5 while the keratinase activity and productivity stayed at high levels. Control of pH, therefore, is not necessary. The temperature for maximum keratinase production is 37°C for both strains, though B. licheniformis is thermophilic and grows best at 50°C. Optimal levels of dissolved oxygen are 10% and 20% for B. licheniformis and B. subtilis respectively. A scale-up procedure using constant temperature at 37°C was adopted for B. subtilis. On the other hand, a temperature-shift procedure by which an 8-h fermentation at 50°C for growth followed by a shift to 37°C for enzyme production was used for B. licheniformis to shorten the fermentation time and increase enzyme productivity. Production of keratinase by B. licheniformis increased by ten-fold following this new procedure. After respective optimization of fermentation conditions, keratinase production by B. licheniformis PWD-1 is approximately 40% higher than that by B. subtilis FDB-29. Received 16 July 1998/ Accepted in revised form 07 March 1999     

木糖发酵产氢菌的筛选及其生长产氢特性研究

利用改进的Hungate厌氧技术, 从牛粪堆肥中分离出一株能有效利用木糖发酵产氢的中温菌HR-1。通过16S rRNA系统发育树分析表明, 菌株 HR-1 与丙酮丁醇梭菌Clostridium acetobutylicum ATCC 824 相似性最高为96%, 结合生理生化和生长特性分析表明, HR-1是梭菌属Clostridium的一个新种, 命名为Clostridium sp. HR-1。菌株HR-1为单胞生长的规则杆状菌(0.3 mm ~0.6 mm)×(1.4 mm~2.3 mm), 革兰氏染色为阴性, 无荚膜、无鞭毛、表面光滑、无明显凸起, 专性厌氧菌。HR-1可在10°C~45°C, pH 4.0~10.0条件下生长; 37°C和pH 8.0分别为其最适生长条件。发酵PYG的主要发酵产物有氢气、二氧化碳、乙酸、丁酸及少量乙醇。HR-1可以利用有机氮源和无机氮源生长并产氢, 酵母提取物是其最佳产氢氮源。HR-1在木糖浓度为3 g/L和初始pH 6.5条件下, 其比产氢量为1.84 mol-H2/mol-木糖, 最大比产氢速率为10.52 mmol H2/h·g-细胞干重。HR-1可以亦利用葡萄糖、半乳糖、纤维二糖、甘露糖和果糖等碳源生长并发酵产氢, 发酵葡萄糖时比产氢量为2.36 mol-H2/mol-葡萄糖。     

Comparison of the optimal culture conditions for cell growth and tissue plasminogen activator production by human embryo lung cells on microcarriers

Optimization of culture conditions such as the dissolved O₂ (DO) concentration, temperature and pH was attempted regarding both cell growth and the production of tissue plasminogen activator (TPA) in a microcarrier cell culture of human embryo lung cells. The growth rate was suppressed at a DO concentration below 30% saturation. From the pH range 7.2–7.6, both the specific growth rate and maximal cell concentration decreased. At a lower temperature than 37°C, although both the specific growth rate and the maximal cell concentration decreased, the cell concentration was maintained for a longer time during the production period, high TPA productivity being maintained. As the optimal conditions for culture growth, a DO concentration of 30% saturation or over, temperature of 37°C and pH of 7.4 are recommended. However, for TPA production after cell culture growth, the DO concentration should be in the range 20–30% O₂ saturation, and the temperature and pH should be lowered to 33°C and 6.8, respectively.     

Temperature significantly affects retroviral vector production and deactivation rates, and thereby determines retroviral titers

The retroviral titer obtained from the pMFG/ψCRIP producer cell line is determined by a dynamic interplay of vector production and deactivation rates. Both these rates are influenced by temperature. It was determined that; (i) the retroviral half-lives are strongly influenced by temperature and the temperature dependency can be described by the Arrhenius equation with an activation energy of 39 kcal/gmol; (ii) the actual retroviral vector productivity per cell is highest at 37?°C with retroviral production rate of 24.4(±7.0; ±?standard deviation) colony forming unit (CFU)/cell/day; (iii) the dynamic interplay of these two factors produces an optimal temperature of 34?°C for pMFG/ψCRIP cells under the culture conditions used; and (iv) the cellular growth rate is highest at 37?°C at 26.8 hr doubling time. Taken together, these parameters can be used to optimize a two-step retroviral production protocol, where the cells are first grown under optimal growth conditions (37?°C) and second, the virus is produced at 34?°C to yield the highest titer. These results have significant implications for optimal retroviral production protocols.     

Increased alkalotolerant and thermostable ribonuclease (RNase) production from alkaliphilic Streptomyces sp. M49-1 by optimizing the growth conditions using response surface methodology

Total of 171 alkaliphilic actinomycetes were evaluated for extracellular RNase production and Streptomyces sp. M49-1 was selected for further experiments. Fermentation optimization for RNase production was implemented in two steps using response surface methodology with central composite design. In the first step, the effect of independent fermentation variables including temperature, initial pH and process time were investigated. After identification of carbon and nitrogen sources affecting the production by one variable at a time method, concentrations of glucose and yeast extract and also inoculum size were chosen for the second central composite design. A maximum RNase activity was obtained under optimal conditions of 4.14 % glucose concentration, 4.63 % yeast extract concentration, 6.7 × 10⁶ spores as inoculum size for 50 ml medium, 42.9 °C, 91.2 h process time and medium initial pH 9.0. Optimum activity of the enzyme is achieved at pH 11 and temperature 60 °C. The enzyme is highly stable at pH range 9.0–12.0 and at 90 °C after 2 h. Statistical optimization experiments provide 2.25 fold increases in the activity of alkalotolerant and thermostable RNase and shortened the fermentation time compared to that of unoptimized condition. The members of Streptomyces can be promising qualified RNase producer for pharmaceutical industries.     

Relationship between prostate-specific antigen levels and ambient temperature

We examined the association between prostate-specific antigen (PSA) and daily mean ambient temperature on the day of the test in healthy men who had three annual checkups. We investigated 9,694 men who visited a hospital for routine health checkups in 2007, 2008, and 2009. Although the means and medians of ambient temperature for the three years were similar, the mode in 2008 (15.8 °C) was very different from those in 2007 and 2009 (22.4 °C and 23.2 °C). After controlling for age, body mass index, and hematocrit, a multiple regression analysis revealed a U-shaped relationship between ambient temperature and PSA in 2007 and 2009 (P?<?0.001 and P?=?0.004, respectively), but not in 2008 (P?=?0.779). In 2007, PSA was 13.5 % higher at 5 °C and 10.0 % higher at 30 °C than that at 18.4 °C (nadir). In 2009, PSA was 7.3 % higher at 5 °C and 6.8 % at 30 °C compared with the level at 17.7 °C (nadir). In logistic regression analysis, a U-shaped relationship was found for the prevalence of a higher PSA (> 2.5 ng/mL) by ambient temperature, with the lowest likelihood of having a high PSA at 17.8 °C in 2007 (P?=?0.038) and 15.5 °C in 2009 (P?=?0.033). When tested at 30 °C, there was a 57 % excess risk of having a high PSA in 2007 and a 61 % higher risk in 2009 compared with those at each nadir temperature. We found a U-shaped relationship between PSA and ambient temperature with the lowest level of PSA at 15–20 °C.     

Synthesis of cyclopropane fatty acid and its effect on freeze-drying survival of Lactobacillus bulgaricus L2 at different growth conditions

In order to correlate cyclopropane fatty acid of the membrane of Lactobacillus bulgaricus L2 with freeze-drying survival at different growth conditions, fatty acid methyl esters (FAME) from extracts grown at difference fermentation pH (5.0, 5.5, 6.0, 6.5) and temperature (30, 35, 37, 39°C) were obtained and analyzed. Results showed that cultures grown at 30°C and pH 5.0, 35°C and pH 5.0, 39°C and pH 6.0 exhibited more resistance to the freeze-drying process than cultures grown in other conditions, cells cultured at 30°C and pH 5.0 had a highest survival rate. On the other hand, cells grown at 37°C displayed poor resistance to adverse conditions possible because of the lower cycC19:0 content. It was concluded that the improved cryotolerance observed during freeze-drying would be associated with an increase in cycC19:0 content and cycC19:0/SFA ratio and vice versa.     

3′-Azido-3′-deoxy-5′-O-isonicotinoylthymidine: A Novel Antiretroviral Analog of Zidovudine. II. Stability in Aqueous Media and Experimental and Theoretical Ionization Constants

Abstract

Degradation of 3′-azido-3′-deoxy-5′-O-isonicotinoylthymidine (AZT-Iso), an antiretroviral derivative of zidovudine, was investigated in buffer pH 7.4, µ = 300 mOsm at 37, 50 and 60°C, and in water (pH 6.6, 37°C), giving zidovudine (AZT) and isonicotinic acid (INA) as products. The rate constants were determined by reversed-phase HPLC showing pseudo-first-order kinetics related to the residual amount of AZT-Iso. In this way, the studied compound was demonstrated to be 153 times more stable in water than in buffer solution at 37°C. The analytical method was conveniently validated demonstrating to be a rapid and accurate stability-indicating technique. In addition, experimental and theoretical values of pKa were determined.     

Production, purification and characterization of cholesterol oxidase from a newly isolated Streptomyces sp.

Cholesterol oxidase production (COD) by a new isolate characterized as Streptomyces sp. was studied in different production media and fermentation conditions. Individual supplementation of 1 % maltose, lactose, sucrose, peptone, soybean meal and yeast extract enhanced COD production by 80–110 % in comparison to the basal production medium (2.4 U/ml). Supplementation of 0.05 % cholesterol (inducer) enhanced COD production by 150 %. COD was purified 14.3-fold and its molecular weight was found to be 62 kDa. V_max (21.93 μM/min mg) and substrate affinity K_m (101.3 μM) suggested high affinity of the COD for cholesterol. In presence of Ba²⁺ and Hg²⁺ the enzyme activity was inhibited while Cu²⁺ enhanced the activity nearly threefold. Relative activity of the enzyme was found maximum in triton X-100 whereas sodium dodecyl sulfate inactivated the enzyme. The enzyme activity was also inhibited by the thiol-reducing reagents like Dithiothreitol and β-mercaptoethanol. The COD showed moderate stability towards all organic solvents except acetone, benzene and chloroform. The activity increased in presence of isopropanol and ethanol. The enzyme was most active at pH 7 and 37 °C temperature. This organism is not reported to produce COD.     

EFFECT OF FERMENTATION PARAMETERS ON BIO-ALCOHOLS PRODUCTION FROM GLYCEROL USING IMMOBILIZED Clostridium pasteurianum: AN OPTIMIZATION STUDY

This article addresses the issue of effect of fermentation parameters for conversion of glycerol (in both pure and crude form) into three value-added products, namely, ethanol, butanol, and 1,3-propanediol (1,3-PDO), by immobilized Clostridium pasteurianum and thereby addresses the statistical optimization of this process. The analysis of effect of different process parameters such as agitation rate, fermentation temperature, medium pH, and initial glycerol concentration indicated that medium pH was the most critical factor for total alcohols production in case of pure glycerol as fermentation substrate. On the other hand, initial glycerol concentration was the most significant factor for fermentation with crude glycerol. An interesting observation was that the optimized set of fermentation parameters was found to be independent of the type of glycerol (either pure or crude) used. At optimum conditions of agitation rate (200 rpm), initial glycerol concentration (25 g/L), fermentation temperature (30°C), and medium pH (7.0), the total alcohols production was almost equal in anaerobic shake flasks and 2-L bioreactor. This essentially means that at optimum process parameters, the scale of operation does not affect the output of the process. The immobilized cells could be reused for multiple cycles for both pure and crude glycerol fermentation.