L-缬氨酸高产菌株的选育研究

以产L-缬氨酸的谷氨酸棒状杆菌(Corynebacterium glutamicum)为原始菌株,利用注入低能氮离子束进行一系列诱变,获得一株稳定的高产L-缬氨酸突变菌株。摇瓶培养96h后发酵能力可达38.0g·L-1,较出发菌株提高18.01%。通过对摇瓶中葡萄糖、玉米浆浓度及培养条件进行优化,发酵能力达到40.6g·L-1,50L发酵罐的发酵能力可达70g·L-1左右。     

结合缺陷型菌株显色法采用离子束诱变筛选高产L-精氨酸突变株

为快速高效筛选L-精氨酸高产突变株,建立一种缺陷菌株平板显色法并采用低能N+离子束对L-精氨酸生产用菌株钝齿棒杆菌SYPA5-5进行诱变处理,通过上述平板显色法筛选获得高产突变株.对突变株进行摇瓶发酵实验,最终选育出一株L-精氨酸产量较高且产酸性能比较稳定的突变菌株钝齿棒杆菌SYPA5-5-36.该菌株摇瓶发酵L-精氨酸产量可达35.85 g/L,比出发菌株提高了19.5％.因此,缺陷型菌株平板显色法可以用于快速、高效筛选高产L-精氨酸突变株.     

L-精氨酸高产菌株的选育

以谷氨酸高产菌种LH谷氨酸棒杆菌为出发菌株,用化学试剂亚硝基胍(NTG)诱变,经结构类似物磺胺胍和摇瓶产酸筛选,获得一株产L-精氨酸的菌株LH425,在摇瓶发酵中,培养96h,产酸率38g·L-1。     

耐温性L-谷氨酸发酵菌种的选育

应用基因组改组技术提高,L-谷氨酸生产菌在高温发酵条件下的谷氨酸产量。以天津短杆菌T6—13变异株SW07-1为原始亲株,分别经紫外线（UV）-硫酸二乙酯（DES）和X射线诱变,获得5株耐温性能略有提高的突变菌株。经2轮基因组改组,获得耐高温（能在44℃生长）的L-谷氨酸菌株F2-50。F2—50在38℃下,摇瓶发酵40h,发酵液中L-谷氨酸浓度比原始出发菌株提高了近41％,在41℃高温下,摇瓶发酵40h,L-谷氨酸浓度比原始出发菌株提高了近2倍。     

lysC定点突变及lysC、asdA串联表达对谷氨酸棒杆菌L-苏氨酸积累的影响

lysC、asdA基因分别编码的天冬氨酸激酶(Aspartate kinase,AK)和天冬氨酸半醛脱氢酶(Aspartate semi-aldehyde dehydrogenase,ASD)是L-苏氨酸合成途径中两个关键限速酶基因,其中AK受到代谢产物赖氨酸与苏氨酸的协同抑制。以选育获得的一株谷氨酸棒状杆菌T11(Corynebacterium glutamicum T11)为出发菌株,通过构建lysC-asdA串联表达盒,并对其关键限速酶基因lysC进行定点突变,突变位点为Ala279Thr,获得抗反馈抑制突变型编码基因lysCr-asdA,将其插入含强启动子tac的穿梭表达载体pZ8-1中成功构建串联表达质粒pZ8-1-lysCr-asdA转化出发菌株,筛选获得工程菌株T11/pZ8-1-lysCr-asdA。摇瓶发酵其L-苏氨酸产量达到7.18 g/L,较出发菌株提高27.8%。进一步的30 L发酵罐补料分批发酵结果显示,发酵60 h L-苏氨酸产量达65.5 g/L,糖酸转化率达到39.5%,较出发菌株分别提高29.5%和33.9%,为后续的进一步构建高产L-苏氨酸的谷氨酸棒杆菌工程菌株提供强有力的基础。     

紫外诱变原生质体选育赖氨酸高产菌株

以钝齿棒杆菌102S₂-58为出发菌株,在原生质体形成及再生的最佳条件下制备原生质体,并对原生质体进行紫外诱变处理,对大量的再生突变株进行发酵筛选．获得了高产稳定株102－100号,其发酵液经氨基酸自动分析仪测定L－赖氨酸积累量由出发菌株的5O．Omg／ml提高到80．8mg／ml,糖转化率达到63．88％．发酵液中主要副产酸——纈氨酸和蛋氨酸的量明显降低。     

双功能尿苷酰转移/去除酶GlnD在谷氨酸棒杆菌JNR中的功能

【目的】通过改造谷氨酸棒杆菌JNR中双功能尿苷酰转移/去除酶GlnD,减弱尿苷酰去除酶的活性,增强NH_4~+的转运和利用,提高L-精氨酸的合成。【方法】本文对来源于谷氨酸棒杆菌的突变菌株JNR中的双功能尿苷酰转移/去除酶GlnD进行整合突变,采用同源重组的方法将H_(414)和D_(415)位点突变为两个丙氨酸AA,在此菌株的基础上过量表达PII蛋白GlnK,并对其进行尿苷酰化研究,离子色谱检测摇瓶发酵过程中NH4+的浓度,并对最终的改造菌株进行连续流加发酵分析。【结果】该双功能尿苷酰转移/去除酶在谷氨酸棒杆菌中成功进行整合突变,有效减弱了尿苷酰去除酶的活性;同时过表达PII蛋白GlnK,其酰基化程度明显增强。摇瓶发酵结果表明菌株L4消耗NH_4~+增加,L-精氨酸产量为36.2±1.2 g/L,比对照菌株L3高出22.7%。5-L发酵罐实验结果显示改造菌株L4的L-精氨酸的产量为52.2 g/L,较野生型菌株L0提高了25.3%。【结论】谷氨酸棒杆菌合成L-精氨酸的过程中氮源是必不可少的。减弱GlnD尿苷酰去除酶的活性后,胞内尿苷酰化的GlnK-UMP增加,GlnK-UMP与氮转录调控因子AmtR结合,转运至胞内的NH_4~+浓度提高,促使L-精氨酸产量显著提高。     

利用紫外线、利福平、氯化锂诱变原生质体筛选L—亮氨酸高产菌株的研究

本实验是以黄色短杆菌T_(6—13)的诱变株L—亮氨酸产生菌D—R—4为出发菌株,经青霉素、甘氨酸、溶菌酶作用制备原生质体,形成率达91.30％,再生率达53.68％;然后对原生质体进行紫外线、利福平、氯化锂复合诱变处理;在再生培养基平皿上培养,获得再生突变株,从中挑取单独菌落,进行摇瓶发酵筛选,已选育出一株57—4S号高产稳定菌株;经氨基酸分析仪测定其发酵液L—亮氨酸产量由出发菌株的17.35mg/ml提高到23.45mg/ml提高了35％。发酵液中主要副酸——异亮氨酸含量很少。     

紫外线与亚硝酸钠复合诱变选育L-组氨酸产生菌

以1株谷氨酸棒杆菌(Corynebacterium glutamicum)S_6作为出发菌株,利用亚硝酸钠(NaNO_2)、紫外线(UV)进行诱变,通过实验证明亚硝酸钠诱变时间在180 s后致死率达到80%,紫外线在照射30 s后致死率达到80%。诱变后的突变菌株经6-巯基嘌呤结构类似物的抗性平板筛选,最终筛得3株菌,Y_1产L-组氨酸量达到331 mg/L,比出发菌株S_6高了5.08%,Z_2产L-组氨酸量达到325 mg/L,比出发菌株S_6高了1.9%,F_6产L-组氨酸量达到330 mg/L,比出发菌株S_6高了7.14%。结果显示,经紫外线与亚硝酸钠复合诱变后的菌株F_6产L-组氨酸的产量最高,比亚硝酸钠诱变后的菌株产L-组氨酸量提高2.06%,比紫外线诱变后的菌株产L-组氨酸量提高5.24%。     

谷氨酸棒杆菌metX、dapA基因敲除对苏氨酸合成的影响

谷氨酸棒杆菌中metX基因编码蛋氨酸合成途径关键酶高丝氨酸乙酰转移酶,dapA基因编码赖氨酸合成途径关键酶二氢吡啶二羧酸合成酶。为研究这两个基因缺失对苏氨酸积累的影响,以谷氨酸棒杆菌R102(AHVr)为出发菌株,通过重叠延伸PCR及同源重组技术分别构建了metX、dapA单基因缺失突变株R102ΔmetX、R102ΔdapA以及双基因缺失的突变株R102ΔmetXΔdapA。对出发菌以及上述3株重组菌进行初步摇瓶发酵试验,用HPLC法测定发酵液中苏氨酸含量。结果表明,发酵72 h后,3株重组菌的苏氨酸产量分别为2.58、2.38和3.01 g/L,比原始菌株分别提高了42.5%、31.5%和66.3%。     

L-色氨酸生产菌的选育及其发酵条件的研究

以代谢控制发酵理论为指导 ,对L -色氨酸产生菌的定向选育、摇瓶发酵条件、30L发酵罐发酵条件进行了研究。以谷氨酸棒杆菌Tx5 - 32 (Phe- +Tyr- )为出发菌株 ,经硫酸二乙酯 (DES)多次诱变处理 ,定向选育出一株L -色氨酸产生菌TQ2 2 2 3(Phe- +Tyr- +5 -MTr+5 -FTr+SGr+CINr)。以摇瓶分批发酵最优条件为基础 ,对菌株TQ2 2 2 3进行了 30L发酵罐分批发酵试验 ,该菌株发酵 6 4h ,产L -色氨酸 7.2 8g·L- 1 。     

Strain improvement and up scaling of phytase production by <Emphasis Type="Italic">Aspergillus niger</Emphasis> NCIM 563 under submerged fermentation conditions

Combination of physical and chemical mutagenesis was used to isolate hyper secretory strains of Aspergillus niger NCIM 563 for phytase production. Phytase activity of mutant N-1 and N-79 was about 17 and 47% higher than the parent strain. In shake flask the productivity of phytase in parent, mutant N-1 and N-79 was 6,181, 7,619 and 9,523 IU/L per day, respectively. Up scaling of the fermentation from shake flask to 3 and 14 L New Brunswick fermenter was studied. After optimizing various fermentation parameters like aeration, agitation and carbon source in fermentation medium the fermentation time to achieve highest phytase activity was reduced considerably from 14 days in shake flask to 8 days in 14 L fermenter. Highest phytase activity of 80 IU/ml was obtained in 1% rice bran–3.5% glucose containing medium with aeration 0.2 vvm and agitation 550 rpm at room temperature on 8th day of fermentation. Addition of either bavistin (0.1%), penicillin (0.1%), formalin (0.2%) and sodium chloride (10%) in fermented broth were effective in retaining 100% phytase activity for 8 days at room temperature while these reagents along with methanol (50%) and ethanol (50%) confer 100% stability of phytase activity at 4°C till 20 days. Among various carriers used for application of phytase in feed, wheat bran and rice bran were superior to silica and calcium carbonate. Thermo stabilization studies indicate 100% protection of phytase activity in presence of 12% skim milk at 70°C, which will be useful for its spray drying.     

Enhanced production of l‐lactic acid by Lactobacillus thermophilus SRZ50 mutant generated by high‐linear energy transfer heavy ion mutagenesis

The aim of this study was to improve l ‐lactic acid production of Lactobacillus thermophilus SRZ50. For this purpose, high efficient heavy‐ion mutagenesis technique was performed using SRZ50 as the original strain. To enhance the screening efficiency for high yield l ‐lactic acid producers, a scale‐down from shake flask to microtiter plate was developed. The results showed that 24‐well U‐bottom MTPs could well alternate shake flasks for L. thermophilus cultivation as a scale‐down tool due to its a very good comparability to the shake flasks. Based on this microtiter plate screening method, two high l ‐lactic acid productivity mutants, A59 and A69, were successfully screened out, which presented, respectively, 15.8 and 16.2% higher productivities than that of the original strain. Based on fed‐batch fermentation, the A69 mutant can accumulate 114.2 g/L l ‐lactic acid at 96 h. Hence, the proposed traditional microbial breeding method with efficient high‐throughput screening assay was proved to be an appropriate strategy to obtain lactic acid‐overproducing strain.     

常压室温等离子体诱变选育L-精氨酸生产菌及发酵条件优化

【目的】通过常压室温等离子体诱变技术选育L-精氨酸高产菌株,利用响应面设计探索突变菌株生产L-精氨酸的最佳发酵条件。【方法】采用常压室温等离子体生物诱变系统对实验室保藏的Corynebacterium glutamicum GUI089进行系列诱变,选育L-高精氨酸和8-氮鸟嘌呤抗性菌株。在单因子实验的基础上,应用Plackett-Burman设计从7个因素中筛选出对L-精氨酸合成具有显著效应的(NH4)2SO4、葡萄糖和尿素3个因素。基于上述结果,进一步采用响应面设计优化出主要影响因素的最佳参数水平。【结果】经过一系列的诱变和筛选,选育出一株L-高精氨酸(15 g/L)和8-氮鸟嘌呤(0.7 g/L)抗性菌株,并将此菌株命名为C.glutamicum ARG 3-16。此菌株的L-精氨酸产量比出发菌株提高了49.79%,且发酵液中杂酸的浓度明显降低,特别是L-脯氨酸、L-谷氨酸和L-缬氨酸。在经响应面优化后的最佳发酵条件下,L-精氨酸的产量达到39.72±0.75 g/L,比优化前提高了10.49%。【结论】通过常压室温等离子体诱变技术成功选育出一株L-精氨酸高产菌株,利用响应面法有效地优化了发酵条件,实验结果表明突变株ARG 3-16具有潜在的生产应用价值。     

Kinetics of kojic acid fermentation byAspergillus flavus link S44-1 using sucrose as a carbon source under different pH conditions

Kojic acid production byAspergillus flavus strain S44-1 using sucrose as a carbon source was carried out in a 250-mL shake flask and a 2-L stirred tank fermenter. For comparison, production of kojic acid using glucose, fructose and its mixture was also carried out. Kojic acid production in shake flask fermentation was 25.8 g/L using glucose as the sole carbon source, 23.6 g/L with sucrose, and 6.4 g/L from fructose. Reduced kojic acid production (13.5 g/L) was observed when a combination of glucose and fructose was used as a carbon source. The highest production of kojic acid (40.2 g/L) was obtained from 150 g/L sucrose in a 2 L fermenter, while the lowest kojic acid production (10.3 g/L) was seen in fermentation using fructose as the sole carbon source. The experimental data from batch fermentation and resuspended cell system was analysed in order to form the basis for a kinetic model of the process. An unstructured model based on logistic and Luedeking-Piret equations was found suitable to describe the growth, substrate consumption, and efficiency of kojic acid production byA. flavus in batch fermentation using sucrose. From this model, it was found that kojic acid production byA. flavus was not a growth-associated process. Fermentation without pH control (from an initial culture pH of 3.0) showed higher kojic acid production than single-phase pH-controlled fermentation (pH 2.5, 2.75, and 3.0).     

等离子体作用结合氧限制模型选育利福霉素SV高产菌株

利福霉素SV毒性低、疗效高、抗菌谱广,主要由地中海拟无枝酸菌发酵生产,其发酵过程属于耗氧发酵,供氧直接影响产物形成.为减少发酵过程氧限制影响,进一步提高利福霉素发酵产量,通过构建定向氧限制模型,将常温常压等离子体诱变和无水亚硫酸钠氧限制筛选模型相结合,建立了利福霉素生产菌株24孔板快速培养的高通量筛选方法,高效选育出能...     

阿维菌素生产菌的常压室温等离子体诱变育种及培养基优化

【目的】通过诱变筛选技术选育阿维菌素高产突变株,对其发酵培养基进行响应面优化,提高阿维菌素产量。【方法】采用常压室温等离子体(ARTP)诱变技术,结合链霉抗性和卡那霉素抗性筛选法及96深孔板高通量筛选法,筛选阿维菌素高产株。在单因素实验的基础上,应用响应面分析法对其发酵培养基进行优化,最后确定最佳培养基配方。【结果】获得一株遗传性状稳定的阿维菌素高产株K-1A6,其阿维菌素产量达到4.22 g/L,比出发菌株9-39提高了23.4%,在最佳培养基中阿维菌素产量达到5.36 g/L,较优化前提高了27.01%。【结论】通过对阿维链霉菌9-39菌株进行ARTP诱变筛选及发酵培养基优化研究能显著提高阿维菌素的产量。     

基于ARTP诱变和高通量筛选的绿针假单胞菌GP72育种方法

【目的】绿针假单胞菌GP72是一种植物根围促生细菌,其分泌的次级代谢产物2-羟基-吩嗪(2-OH-PHZ)具有广谱抗真菌活性,但其产量较低,不能满足农业生产的应用需求,因此需对GP72进行改造,从而提高产量。【方法】从GP72的野生株出发,首次将2-OH-PHZ合成途径的限制性因子Phz O用绿色荧光蛋白(GFP)替换,以一种新型的常压室温等离子体技术(Atmospheric and room temperature plasma,ARTP)进行诱变,通过酶标仪测定96孔板中突变株的荧光强度进行高通量筛选;最后将荧光强度高的菌株中绿色荧光蛋白(Green fluorescent protein,GFP)替换为Phz O以获得2-OH-PHZ高产突变株。【结果】经过五轮诱变后,获得一株荧光强度增加1.62倍的突变株,用phz O基因回替后,该突变株在KB培养基中摇瓶培养时2-OH-PHZ的产量为野生型的4.62倍。【结论】基于安全、高效ARTP诱变技术,并以GFP替换限制性因子作为标记进行高通量筛选,可以快速获得高产2-OH-PHZ的GP72突变株,克服了传统诱变育种方法筛选难度大、费时费力的不足,为其它微生物的育种提供了参考。