固定化嗜热脂肪芽孢杆菌合成低聚半乳糖

利用海藻酸钙、明胶和壳聚糖为固定化载体包埋嗜热脂肪芽孢杆菌细胞合成低聚半乳糖 (GOS)。通过比较三种方法的酶活力回收、最适反应条件、GOS的得率和和载体机械强度 ,选择明胶作为固定化细胞的载体。反应体系的温度、pH、乳糖浓度、乳糖的转化率和载体的传质阻力对GOS合成有明显影响。在CSTR反应器中水解 60 %乳糖 ,GOS最大得率为31 2 % ,经过 96h( 8批反应 ) ,产物得率为原来的 88%。在空速 0 0 9h- 1条件下 ,利用填充床反应器连续水解乳糖 ,GOS的得率和反应器生产能力分别为 31 5%和 1 7 4g (L·h) ,连续反应1 40h,GOS得率下降 2 0 %。产物经过活性炭柱层柱分离纯化 ,通过13C NMR鉴定四糖的化学结构为 β D Gal ( 1→ 3) D Gal ( 1→ 6) D G ( 1→ 4) D Glu。     

盐单胞菌S62 β-半乳糖苷酶合成低聚半乳糖的研究

以盐单胞菌S62 β-半乳糖苷酶为研究对象,探究其合成低聚半乳糖效率。为了提高低聚半乳糖产率,对反应条件进行了优化,并以反应温度、pH、加酶量、底物浓度为考察对象进行正交试验,得到最优反应条件:反应温度40℃,pH 7.0,加酶量50 U/mL,底物质量浓度300 g/L。反应6 h时可获得最大低聚半乳糖产率(41.91±0.27)%,乳糖消耗率为(82.47±0.38)%。反应4～8 h内低聚半乳糖产率都维持在40%以上,此时乳糖消耗率均在80%以上,在提高乳糖利用率的同时实现了低聚半乳糖的高产,有利于降低生产成本,为低温S62 β-半乳糖苷酶工业化应用奠定了基础。     

利用固定化重组大肠杆菌细胞生产D-塔格糖

利用经海藻酸钙包埋的重组大肠杆菌细胞催化D-半乳糖生产D-塔格糖,考察了细胞包埋量、反应条件对固定化细胞催化效率以及对D-塔格糖生产稳定性的影响。确定的最优转化条件为:温度65℃,pH 6.5,添加终浓度为1 mmol/L Mn²⁺,底物(D-半乳糖)浓度100 g/L,重组大肠杆菌细胞用量40 g/L。固定化小球在0.3%戊二醛溶液中交联30 min可以显著提高其在高温下的机械强度。考察了异构化反应体系中硼酸与底物间的摩尔比对产率的影响。研究结果表明,添加适量的硼酸可以改变原有的化学反应平衡,实现D-塔格糖的高产。利用D-半乳糖为底物在最优的反应条件下催化24 h,固定化细胞对D-半乳糖的转化率最高,可达65.8%,连续转化8批次的平均转化率为60.6%,为工业化生产D-塔格糖奠定了基础。     

β-半乳糖苷酶酶学性质及其在低聚半乳糖合成中的应用

研究乳酸克鲁维酵母所产β-半乳糖苷酶的酶学性质及低聚半乳糖(galactooligosaccharides,GOS)的酶法合成条件。利用高效液相色谱法进行检测,以GOS(聚合度n3)生成量为指标,考察温度、pH、金属离子种类和浓度对酶活性的影响,以及K+存在时,底物浓度、反应时间、加酶量对乳糖转化率及GOS生成浓度的影响。结果表明:一价离子对β-半乳糖苷酶转糖苷活性具有促进作用,其中K+、NH+4对水解活性同样起促进作用,而Na+起抑制作用;制备低聚半乳糖的最佳工艺条件为37℃、pH8.0、K+0.08mol/L、初始乳糖质量浓度500g/L、反应时间5h、加酶量10μL/g乳糖,此条件下低聚半乳糖的生成质量浓度达到94.74g/L。     

微生物酶法合成低聚半乳糖的新进展

低聚半乳糖(GOS)是目前国际上已开发的功能性低聚糖之一,其商业化产品是应用微生物β-半乳糖苷酶以乳糖为原料进行转糖基反应获得,不同来源的酶合成GOS的结构不同,转糖基效率也存在差异.天然酶合成GOS的产量一般为20%～45%,分子改造获得的人工酶能将90%的乳糖底物转化为GOS;采用两相体系或反相胶束可以在一定程度上提高GOS产量.应用填充床反应器、活塞流反应器、膜反应器可规模化合成GOS;采用色谱柱法、酶法、纳滤膜法和微生物发酵法可纯化GOS产品,去除单糖及乳糖组分,扩大其应用范围.     

耐高温β-糖苷酶的乳糖水解活性及转糖基活性

β-糖苷酶（ttβGLY）是Thermus thermophilus产生的一种耐高温酶,以乳糖为底物的酶反应研究表明：该酶具有较高的乳糖水解活性,其最适温度为70℃,最适pH为7．0,乳糖水解的Km=1．566mmol／L,Vmax=0．406mmol／min,在70℃有较好的热稳定性。该酶同时具有较强的转糖基活性,在以40％乳糖为底物,加酶量42．5U／mL、反应温度70℃、反应时间16h的条件下,低聚半乳糖的合成率达到35．3％。水解产物葡萄糖对乳糖水解反应和转糖基反应具有抑制作用,是影响GOS合成的重要因素。     

转糖基β-半乳糖苷酶产生菌Enterobacter agglomerans B1：筛选鉴定、发酵产酶及其合成低聚半乳糖的研究

从土壤中筛选获得一株具有转糖基活性的β-半乳糖苷酶产生菌,综合其形态学特征、生理生化特征及16S rDNA序列同源分析结果,将其鉴定为成团肠杆菌(Enterobacter agglomerans)B1.通过单因子试验和正交试验,对B1菌株产转糖基β-半乳糖苷酶的培养条件进行了优化.最佳培养基主要组份为:乳糖1%,酵母粉1%,蛋白胨0.5%;发酵条件为:初始pH7.5,发酵温度25℃,发酵时间26 h.在该培养条件下产酶量为9.7U/mL.利用薄层层析技术研究了pH、温度、底物浓度和反应时间对该菌株全细胞以乳糖为底物生成低聚半乳糖的影响,确定最适反应条件为:pH7.5缓冲液配制的30%乳糖溶液;50℃反应12h.最优化反应的转糖基产物经HPLC、TLC和MS分析,确定低聚半乳糖产量为40.7%,组分为转移二糖、三糖和四糖.     

β-半乳糖苷酶的筛选、克隆表达、酶学性质及其酶法合成低聚半乳糖

采用人工底物邻硝基苯酚-β-D-半乳糖苷(o NPG)为筛选标记,从耐有机溶剂微生物菌库中,筛选出具有较高水解活性的β-半乳糖苷酶产生菌,再以乳糖为底物考察菌株低聚半乳糖的合成性能,筛选得到1株产β-半乳糖苷酶的Erwinia billingiae WX1。根据Gen Bank中相同属种的基因组序列推测β-半乳糖苷酶基因,克隆得到β-半乳糖苷酶基因gal,并在大肠杆菌中实现了来源于Erwinia billingiae菌β-半乳糖苷酶的克隆表达。该基因的开放阅读框(ORF)为1 428 bp,编码475个氨基酸,理论相对分子质量为5.2×104。镍柱法分离纯化得到电泳纯的β-半乳糖苷酶GAL,其酶学性质研究表明最适催化温度55℃,最适p H 7.0;Mg~(2+)、Mn~(2+)对该酶起较强促进作用,EDTA对该酶抑制作用较强。利用β-半乳糖苷酶GAL的转糖基作用,以乳糖为底物合成低聚半乳糖,初步优化的反应条件:底物乳糖质量浓度400 g/L,每克乳糖添加酶量1.0 U,在40℃反应16 h后,低聚半乳糖合成率达到34%(质量分数),显示了较好的开发前景。     

重组大肠杆菌合成左旋多巴条件的优化

通过对合成体系各组分对产物形成的影响的研究。分别求得了底物邻苯二酚,丙酮酸及乙酸氨的表观米氏常数,表观底物抑制常数和最适底物浓度,并得出合成左旋多巴的最适反应体系为：1%丙酮酸,1.2%邻苯二酚,2%乙酸铵,0.1?TA,0.2%亚硫酸钠,用氨水调pH至8.0。加入从与合成体系等体积培养液中收获的重组大肠杆菌细胞,于15℃反应16h,L-DOPA的产量为15.36g/L。     

海藻酸钠-壳聚糖固定化木瓜蛋白酶催化内吗啡肽的合成

反应体系以乙腈作为有机介质,在微水有机溶剂体系中以Boc-Trp-OH和Phe-NH2为底物,用海藻酸钠 壳聚糖固定化木瓜蛋白酶催化合成Trp-Phe-NH2时,产率为27.8%．在这一合成反应中,对pH值、离子强度、溶液含量、反应温度、酶用量和反应时间进行正交试验,证明pH是本合成过程的最重要影响因素．反应体系以乙腈为有机介质,在微水有机溶剂体系中以 Boc-Tyr-Pro-OMe和Trp-Phe-NH2为底物,用IPSAC催化合成Tyr-Pro-Trp-Phe-NH2,产率为35~2%．     

Production of galacto-oligosaccharides by immobilized recombinant beta-galactosidase from Aspergillus candidus

The preparation of galacto-oligosaccharides (GOSs) was studied using the immobilized recombinant beta-galactosidase from Aspergillus candidus CGMCC3.2919. The optimal pH and temperature for the immobilized enzyme were observed at pH 6.5 and 40 degrees C, respectively. Increasing the initial lactose concentration increased the yield of GOSs. The dilution rate was found to be a key factor during the continuous production of GOSs. The maximum productivity, 87 g/L.h was reached when 400 g/L lactose was fed at dilution rate of 0.8/h. The maximum GOS yield reached 37% at dilution rate of 0.5/h. Continuous operation was maintained for 20 days in a packed-bed reactor without apparent decrease in GOS production. The average yield of GOSs was 32%, corresponding to the average productivity of 64 g/L.h, which implied that the immobilized recombinant beta-galactosidase has potential application for GOS production.     

Immobilization of beta-galactosidase on fibrous matrix by polyethyleneimine for production of galacto-oligosaccharides from lactose

The production of galacto-oligosaccharides (GOS) from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth was studied. A novel method of enzyme immobilization involving PEI-enzyme aggregate formation and growth of aggregates on individual fibrils of cotton cloth leading to multilayer immobilization of the enzyme was developed. A large amount of enzyme was immobilized (250 mg/g support) with about 90-95% efficiency. A maximum GOS production of 25-26% (w/w) was achieved at near 50% lactose conversion from 400 g/L of lactose at pH 4.5 and 40 degrees C. Tri- and tetrasaccharides were the major types of GOS formed, accounting for about 70% and 25% of the total GOS produced in the reactions, respectively. Temperature and pH affected not only the reaction rate but also GOS yield to some extend. A reaction pH of 6.0 increased GOS yield by as much as 10% compared with that of pH 4.5 while decreased the reaction rate of immobilized enzyme. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme under the same reaction conditions, suggesting diffusion limitation was negligible in the packed bed reactor and the enzyme carrier. Increase in the thermal stability of PEI-immobilized enzyme was also observed. The half-life for the immobilized enzyme on cotton cloth was close to 1 year at 40 degrees C and 21 days at 50 degrees C. Stable, continuous operation in a plug-flow reactor was demonstrated for about 3 days without any apparent problem. A maximum GOS production of 26% (w/w) of total sugars was attained at 50% lactose conversion with a feed containing 400 g/L of lactose at pH 4.5 and 40 degrees C. The corresponding reactor productivity was 6 kg/L/h, which is several-hundred-fold higher than those previously reported.     

Production of galacto-oligosaccharides from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth.

The production of galacto-oligosaccharides (GOS) from lactose by A. oryzae beta-galactosidase immobilized on cotton cloth was studied. The total amounts and types of GOS produced were mainly affected by the initial lactose concentration in the reaction media. In general, more and larger GOS can be produced with higher initial lactose concentrations. A maximum GOS production of 27% (w/w) of initial lactose was achieved at 50% lactose conversion with 500 g/L of initial lactose concentration. Tri-saccharides were the major types of GOS formed, accounting for more than 70% of the total GOS produced in the reactions. Temperature and pH affected the reaction rate, but did not result in any changes in GOS formation. The presence of galactose and glucose at the concentrations encountered near maximum GOS greatly inhibited the reactions and reduced GOS yield by as much as 15%. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme, suggesting no diffusion limitation in the enzyme carrier. The thermal stability of the enzyme increased approximately 25-fold upon immobilization on cotton cloth. The half-life for the immobilized enzyme on cotton cloth was more than 1 year at 40 degrees C and 48 days at 50 degrees C. Stable, continuous operation in a plugflow reactor was demonstrated for 2 weeks without any apparent problem. A maximum GOS production of 21 and 26% (w/w) of total sugars was attained with a feed solution containing 200 and 400 g/L of lactose, respectively, at pH 4.5 and 40 degrees C. The corresponding reactor productivities were 80 and 106 g/L/h, respectively, which are at least several-fold higher than those previously reported.     

Recycling of textile bleaching effluents for dyeing using immobilized catalase

Catalase was immobilized on alumina carrier and crosslinked with glutaraldehyde. Storing stability, temperature and pH profiles of enzyme activity were studied in a column reactor with recirculation and in a batch stirred-tank reactor. The immobilized enzyme retained 44% of its activity at pH 11, 30 °C and 90% at 80 °C, pH 7. The half-life time of the immobilized catalase was increased to 2 h at pH 12, and 60 °C. Acceptable results were achieved when the residual water from the washing process of H₂O₂-bleached fabrics was treated with the immobilized enzyme and then reused for dyeing.     

Continuous production of 4-ethylguaiacol by immobilized cells of salt-tolerant Candida versatilis in an airlift reactor

The effects of pH, temperature, aeration, and residence time on the continuous production of 4-ethyl-guaiacol (4-EG), which is one of the characteristic aroma components in soy sauce, by immobilized cells of the salt-tolerant yeast Candida versatilis were investigated using an airlift reactor. The optimum pH and temperature were about 4.0 and 30–33°C, respectively. The amount of 4-EG in the liquid was constant even during alterations of nitrogen/air ratio in the supplied gas. A large amount of 4-EG (over 20 ppm) was produced at a residence time from 5 to 28 h and 1–3 ppm of 4-EG, which was the optimum concentration in conventional soy souce, was produced at a shorter residence time of 0.5 h. The 4-EG production by immobilized C. versatilis cells using the airlift reactor was stable for 40 d. It was found that the immobilized cell method was effective for the production of 4-EG by C. versatilis cells.     

Bioconversion of D-galactose to D-tagatose: continuous packed bed reaction with an immobilized thermostable L-arabinose isomerase and efficient purification by selective microbial degradation

The continuous enzymatic conversion of D-galactose to D-tagatose with an immobilized thermostable L-arabinose isomerase in packed-bed reactor and a novel method for D-tagatose purification were studied. L-arabinose isomerase from Thermoanaerobacter mathranii (TMAI) was recombinantly overexpressed and immobilized in calcium alginate. The effects of pH and temperature on D-tagatose production reaction catalyzed by free and immobilized TMAI were investigated. The optimal condition for free enzyme was pH 8.0, 60°C, 5 mM MnCl(2). However, that for immobilized enzyme was pH 7.5, 75°C, 5 mM MnCl(2). In addition, the catalytic activity of immobilized enzyme at high temperature and low pH was significantly improved compared with free enzyme. The optimum reaction yield with immobilized TMAI increased by four percentage points to 43.9% compared with that of free TMAI. The highest productivity of 10 g/L h was achieved with the yield of 23.3%. Continuous production was performed at 70°C; after 168 h, the reaction yield was still above 30%. The resultant syrup was then incubated with Saccharomyces cerevisiae L1 cells. The selective degradation of D-galactose was achieved, obtaining D-tagatose with the purity above 95%. The established production and separation methods further potentiate the industrial production of D-tagatose via bioconversion and biopurification processes.     

Photochemical system for regenerating NADPH from NADP with use of immobilized chloroplasts

Spinach chloroplasts were immobilized in 2% agar gel. Crude ferredoxin and NADP–ferredoxin oxidoreductase isolated from spinach were used as electron carriers. The activity of the NADP reduction by immobilized chloroplasts increased with increasing ferredoxin concentration and the maximum activity was obtained at 8μM ferredoxin. The saturation of NADP reduction was observed at a light intensity of over 1000 lx. The optimum pH and temperature of NADP reduction were 8 and 25°C, respectively. The reduced NADP in a reaction medium increased linearly with increasing reaction time under illumination. NADP was continuously reduced for 2 hr with a hollow-fiber reactor containing immobilized chloroplasts. NADPH and NADP were separated with a hollow-fiber dialyzer from ferredoxin and NADP–ferredoxin oxidoreductase, which were reused. The conversion ratio of NADP to NADPH was from 40 to 80%.     

Enzyme, β-galactosidase immobilized on membrane surface for galacto-oligosaccharides formation from lactose: Kinetic study with feed flow under recirculation loop

The work focuses on producing galacto-oligosaccharides (GOS) through an enzymatic reaction with lactose under a partial recirculation loop by utilizing membrane-immobilized β-galactosidase. Cross-linking through covalent bonding, using gluteraldehyde, was employed to immobilize enzyme on a microporous polyvinylidene fluoride membrane. GOS synthesis was carried out in a laboratory fabricated reaction cell, whereby three immobilized membranes were housed in series. The reaction was conducted at varying initial lactose concentrations (ILCs) and feed flow rates at pH 6 and 40 °C. A maximum GOS of 30% (dry basis) was obtained after 60 h of reaction time, 50 g/L ILC, 241 U of enzyme (specific loading of 600 U/g-membrane), and 0.5 mL/min of feed flow rate at 56% lactose conversion. The GOS yield increased with increased ILC and decreased feed flow rate. The selectivity of GOS formation increased by increasing both the ILC and the feed flow rate, whereas the reverse was true for mono-saccharides. The immobilized enzyme retained ∼50% of its initial activity after 30 days of storage at 20 °C, while the native enzyme lost 100% of its activity within 21 days. Furthermore, a five-step, nine-parameter model was developed, and simulated results showed excellent agreement with the experimental data.