色氨酸合成酶酶法合成S-苯基-L-半胱氨酸

利用重组色氨酸合成酶催化合成S-苯基-L-半胱氨酸,考察了反应温度、pH、底物摩尔比和底物浓度对色氨酸合成酶酶活的影响。最佳转化条件为:反应温度为37℃,pH=8,苯硫酚与L-丝氨酸的适宜底物摩尔比为1.2∶1,底物最适合浓度为400 mmol/L,反应达到平衡时间为16 h,底物L-丝氨酸摩尔转化率达到91%,苯硫酚与色氨酸合成酶活性位点Ser 235和Gly 233形成稳定的氢键。     

重组色氨酸合成酶催化合成5-羟基色氨酸

利用重组色氨酸合成酶催化合成5-羟基色氨酸,考察了pH、反应温度、底物摩尔比和底物浓度对色氨酸合成酶酶活的影响。最佳转化条件为：反应温度为35 篊,pH为9,5-羟基吲哚与工业角蛋白水解氨基酸液中L-丝氨酸的适宜底物摩尔比为1.1: 1,底物工业角蛋白水解氨基酸液中L-丝氨酸最适合浓度为200 mmol/L,反应达到平衡时间为18 h,底物L-丝氨酸摩尔转化率达到86%。     

重组色氨酸合成酶催化合成L-5-羟基色氨酸

利用重组色氨酸合成酶催化合成L-5-羟基色氨酸,采用单因素以及响应面分析方法考察了p H、反应温度、底物浓度和底物摩尔比对L-5-羟基色氨酸合成的影响。最佳转化条件为:反应温度为32℃,p H=8.6,5-羟基吲哚与工业角蛋白水解氨基酸液中L-丝氨酸的适宜底物摩尔比为1.1∶1,底物工业角蛋白水解氨基酸液中L-丝氨酸最适合浓度为180 mmol/L,反应平衡时间为18 h,工业角蛋白水解氨基酸液中L-丝氨酸摩尔转化率达到86.5%。     

基于改性玉米秸秆纤维固定色氨酸合成酶基因工程菌合成L-2-甲基-色氨酸

摘要：利用固定化色氨酸合成酶细胞合成L-2-甲基-色氨酸。采用戊二醛作为交联剂、海藻酸钠作为包埋剂和改性玉米秸秆纤维作为填充剂固定色氨酸合成酶基因工程菌,探究并建立最优固定因素水平条件,提高该固定化菌的酶活力以及其稳定性,响应面法优化固定化色氨酸合成酶基因工程菌合成L-2-甲基-色氨酸。研究结果表明,底物L-丝氨酸浓度为10 g/L,温度为35℃,pH为8.0,L-2-甲基-色氨酸合成量达到5.3 g/L,底物L-丝氨酸转化率为41.6%,产物L-2-甲基-色氨酸收率为25.3%,固定化色氨酸合成酶基因工程菌可连续使用12批次。     

固定化色氨酸合成酶细胞合成L-2-甲基色氨酸

利用固定化色氨酸合成酶细胞合成了L-2-甲基色氨酸,采用戊二醛作为交联剂、海藻酸钠作为包埋剂和改性玉米秸秆纤维作为填充剂固定色氨酸合成酶基因工程菌,并利用响应面法建立了最优固定因素水平条件,并考察了最佳条件下该固定化菌的酶活力以及其稳定性。实验结果表明:底物L-丝氨酸质量浓度为30 g/L、温度为35℃、pH=8.0时,L-2-甲基色氨酸质量浓度达到5.3 g/L,底物L-丝氨酸转化率为41.6%,产物L-2-甲基色氨酸收率为25.3%,固定化色氨酸合成酶基因工程菌可连续使用12批次。     

色氨酸酶重组基因表达及其酶法合成L-色氨酸

为实现色氨酸酶高效、低成本催化合成L-色氨酸,利用p ET30a为载体在宿主细胞E.coli BL21(DE3)中重组表达了产气肠杆菌(Enterobacter aerogenes)来源的色氨酸酶,以丙酮酸、吲哚和氨为底物,探究其酶学性质,考察了反应温度、起始p H、底物摩尔比对酶促反应的影响,并利用丙酮酸发酵液为底物酶法合成L-色氨酸。结果表明,色氨酸酶重组表达成功,色氨酸酶最佳反应条件为:温度35℃,起始p H=9.0,底物摩尔比n(吲哚)∶n(丙酮酸)=0.6∶1,底物丙酮酸浓度为0.17 mol/L。利用重组色氨酸酶全细胞催化100 m L浓度为0.57 mol/L丙酮酸发酵液,流加浓度为4.27 mol/L吲哚酒精溶液6.5 m L,反应28 h后,L-色氨酸浓度达0.25 mol/L,吲哚摩尔转化率达91.8%。     

重组L-苏氨酸醛缩酶催化合成L-4-硝基苯基丝氨酸

利用pGEX-KG载体在大肠杆菌BL21(DE3)中重组表达了L-苏氨酸醛缩酶,以4-硝基苯甲醛、甘氨酸为底物酶法合成了L-4-硝基苯基丝氨酸,考察了反应温度、pH、底物摩尔比和甘氨酸浓度对酶活的影响。最佳转化条件为：反应温度45℃,pH=8.0,甘氨酸与4-硝基苯甲醛底物摩尔比5:1,底物甘氨酸最适浓度为500 mmol/L;0.1 g湿细胞菌体在10 mL反应体系中在最佳反应条件下反应24 h,底物4-硝基苯甲醛转化率为43%,产物L-4-硝基苯基丝氨酸达到9.72g/L,总收率为35%。     

利用色氨酸酶酶法拆分D,L-丝氨酸制备D-丝氨酸

以D,L-丝氨酸为底物,采用色氨酸酶将L-丝氨酸转化为L-色氨酸,并进一步分离纯化拆分得到D-丝氨酸。该文对色氨酸酶酶法拆分条件进行了响应面优化,酶促反应最佳条件为:温度45℃,pH=8.0,反应时间18 h,底物D,L-丝氨酸质量浓度30 g/L,色氨酸酶用量为6 g/L,经过两次转化,L-丝氨酸的总转化率可达95.4%。酶促反应液经NKA-Ⅱ型大孔吸附树脂与001×7强酸性阳离子交换树脂纯化,重结晶后得到D-丝氨酸,化学纯度99.4%,α2D0=-15.3°(ρ=0.1 kg/L,2 mol/L HCl),总回收率为66.6%。     

丝氨酸脱氨酶酶法拆分DL-丝氨酸

利用pET28a为载体在宿主细胞BL21(DE3)中重组表达了大肠杆菌丝氨酸脱氨酶,以L-丝氨酸为底物,研究了其酶学性质,考察了温度、起始pH、底物质量浓度等因素对酶促反应的影响,并利用丝氨酸脱氨酶酶法拆分了DL-丝氨酸。结果表明,丝氨酸脱氨酶重组表达成功;丝氨酸脱氨酶最佳反应条件为37℃,pH=9.0,底物质量浓度40 g/L;0.3 g菌体细胞酶法拆分100 mLρ(DL-丝氨酸)=80 g/L反应液需8 h,其中,L-丝氨酸摩尔转化率达98%。     

固定化色氨酸合成酶基因工程菌合成L-色氨酸的研究

以海藻酸钠作为包埋剂、戊二醛作为交联剂和氯化钙作为填充剂对色氨酸合成酶基因工程菌进行固定化,同时探究三种物质和菌体负载量对固定化菌影响,响应面法优化色氨酸合成酶基因工程菌合成L-色氨酸。固定化色氨酸合成酶基因工程菌最优制备条件为：海藻酸钠28.92 g/l、戊二醛0.95%、氯化钙19.82 g/l、菌体负载量25 g/l。底物L-丝氨酸浓度为1%、固定化菌8g, L-色氨酸转化率为28.16%。固定化菌可连续使用15批次。     

有机相中脂肪酶催化转酯化反应动力学拆分左旋帕罗醇

研究了在有机相中脂肪酶催化转酯化反应动力学拆分左旋帕罗醇,考察了酶种类、溶剂、酰基供体、温度、底物与酰基供体摩尔比等因素对反应的影响。结果表明:以Novozym 435为催化剂,在30℃下,以乙腈为反应溶剂,乙酸乙烯酯为酰基供体,底物浓度40mmol/L及其与酰基供体摩尔比为1:8时,反应8h后,底物转化率为48.1%,ee_s为53.3%,E值为6.20。     

Effects of Polyhydroxy Compounds on Enzymatic Synthesis of <Emphasis Type="SmallCaps">L</Emphasis>-Tryptophan Catalyzed by Tryptophan Synthase

Abstract  

The effects of polyethylene glycol (PEG) of different molecular (1000, 2000), glycerol, ethylene glycol on the catalytic activity of tryptophan synthase were studied. The results indicated that the addition of PEG 2000 increased the enzymatic activity of tryptophan synthase. The enzymatic activity of tryptophan synthase was enhanced 25.2% by 10 g L⁻¹ PEG 2000. Reaction conditions were optimized by using 10 g L⁻¹ PEG 2000 at pH 9 and 40 °C. L-Serine conversion rate reach 89.9% under the optimal conditions. The kinetic parameters indicated the specificity of TSase to substrate was improved.     

Lipase‐catalyzed production of medium‐chain triacylglycerols from palm kernel oil distillate: Optimization using response surface methodology

Optimization of lipase‐catalyzed esterification for the production of medium‐chain triacylglycerols (MCT) from palm kernel oil distillate and glycerol was carried out in order to determine the factors that have significant effects on the reaction system and MCT yield. Novozyme 435 from Candida antarctica lipase was found to have the highest activity at 52.87 ± 0.03 U/g. This lipase also produced the highest MCT yield, which is 56.67%. The effect of different variables on MCT synthesis was studied with a two‐level five‐factor fractional factorial design. The various variables include (1) reaction temperature, (2) enzyme load, (3) molecular sieves concentration, (4) reaction time and (5) molar substrate ratio. Reaction temperature, reaction time and molar substrate ratio strongly affect MCT synthesis (p <0.05). However, enzyme load and molecular sieve concentration did not have a significant (p >0.05) influence on MCT yield. Therefore, the significant variables such as reaction temperature, reaction time and molar substrate ratio were further optimized through central composite rotatable design (CCRD). Comparisons between predicted and experimental values from the CCRD optimization procedures revealed good correlation, implying that the quadric response model satisfactorily expressed the percentage yield of MCT in the lipase‐catalyzed esterification. The optimum MCT yield is 73.3% by using 2 wt‐% enzyme dosage, a molecular sieves concentration of 1 wt‐%, a reaction temperature of 90 °C, a reaction time of 10 h and a molar substrate ratio of 4 : 1 (medium‐chain fatty acid/glycerol). Experiments to confirm the predicted results using the optimal parameters were conducted and an MCT yield of 70.21 ± 0.18% (n = 3) was obtained.     

Five-factor response surface optimization of the enzymatic synthesis of citronellyl butyrate by lipase IM77 from Mucor miehei

Response surface methodology (RSM) and a five-level-five-factor central composite rotatable design (CCRD) were used to evaluate the effects of synthetic variables, such as reaction time (3 to 27 h), temperature (25 to 65 °C), enzyme amount (10 to 50%), substrate molar ratio of citronellol to butyric acid (1∶1 to 1∶3), and added water amount (0 to 20%) on molar percent yield of citronellyl butyrate by direct esterification, using lipase IM77 from Mucor miehei. Reaction time and temperature were the most important variables. Substrate molar ratio had no effect on percent molar conversion. Based on contour plots, optimal synthetic conditions were these: reaction time 24 h, temperature 60°C, enzyme amount 20%, substrate molar ratio 1∶1.5, and added water 0%. The predicted molar conversion value was 100%. An actual experimental value of 98% molar conversion was obtained.     

Preparation of D-lysine by chemical reaction and microbial asymmetric transformation

The DL-lysine crystals from the racemization of L-lysine was treated as substrate with Hafnia alvei AS1.1009 intact cells as biocatalysts to produce crystalline D-lysine with a yield of 56.6% from the reaction mixture after simple purification. In the presence of 0.10 molar equivalent of salicylaldehyde, L-lysine racemization can be completed within 4 h in 1.0 mol/L of NaOH at 100°C. The activation energy of the processes was 62187.86 J/mol. The characteristics of Hafnia alvei AS1.1009 decarboxylase were studied. Under the conditions of pH 8.0, temperature 37°C, cell concentration 10 g/L, tween-80 0.5 g/L, substrate concentration 30 g/L, and the specific activity of up to 3840 U, L-lysine can be completely degraded by the decarboxylase for 12 h under the optimal conditions.