不同补料控制方式发酵生产头孢菌素C的性能比较

在7 L发酵罐下,对利用顶头孢霉菌(Cephalosporins acremonium)发酵生产头孢菌素C(CPC)过程的最优底物流加工艺进行了研究。提出了一种新式硫铵豆油耦联型的硫铵流加策略。该控制策略可将发酵液中的氨态氮浓度控制在3 6 g/L之间,同时满足了发酵前期细胞生长与CPC合成对氮源和硫源的需求,促进了顶头孢霉菌菌丝分化,为发酵后期的CPC高效生产奠定了前期基础。比较了CPC合成期内间歇、匀速和DO-Stat自动流加3种不同豆油流加方式的发酵性能。研究发现,耦联使用硫铵/后程通富氧空气DO-Stat法进行硫铵和豆油的同时补料和CPC发酵,可将碳源浓度与溶解氧浓度DO同时控制于适中水平,使CPC合成以高浓度和低副产物积累的方式进行,最终CPC浓度和得率分别达到35.77 g/L和13.3%。主代谢副产物脱乙酰氧头孢菌素C(DAOC)的积累量和DAOC/CPC分别仅有0.178 g/L和0.5%。     

C．shehatae TZ8耐乙醇菌株的筛选及发酵性能研究

以C.shehataeTZ8为出发茵株,利用1％溶壁酶和1％蜗牛酶酶解1．5h,制备成C.shehataeTZ8原生质体,并对原生质体进行紫外诱变,以含不同浓度乙醇的木糖液体培养基培养进行初筛和复筛,获得一株遗传性能稳定、耐乙醇能力达5．5％（v／v）的蕾株C．shehataeTZ8-4,比初始菌株耐乙醇能力提高了2％。对突变株C．shehataeTZ8-4发酵性能的研究结果表明：C．shehataeTZ8-4发酵糖能力从80g/L（葡糖糖和木糖比为2：1）提高到120g／L,最大乙醇产量从27．41g／L提高到43．12g／L。     

高效利用木糖产油的氮离子注入Mortierella alpina诱变选育研究

木糖的有效利用是木质纤维素全利用的基础。为了获得高效利用木糖产油的高山被孢霉菌株,通过多轮氮离子束诱变,筛选出一株有效利用木糖的产油高山被孢霉1502．8（MortiereUaalpina1502—8,MAIS02．8）,并研究了以葡萄糖／木糖（W／W,5／3）组成的混合糖为碳源,突变株生长和油脂积累的特性。采用单因子和正交实验对培养基组成和发酵条件进行了优化,结果表明,诱变菌在温度28oC,pH8．0,接种量8％,装液量30％,蛋白胨0．76％和豆粕1％,分批补糖的最优发酵条件下发酵9d,生物量和菌体油脂积累量分别达29．8g／L和11．7g／L,较出发菌提高了2．59倍和2．05倍,同时原料糖利用率达到99．4％。     

手性拆分环氧氯丙烷菌株的筛选、鉴定及产酶条件研究

从土壤中筛选到5株环氧化物水解酶生产菌,并通过ITS序列鉴定了其中的C375菌,结果为黑曲霉（Aspergillus nigerZJB-09103）。考察了培养基不同碳源、氮源、金属离子和pH等对产酶的影响,得到了较佳的培养基条件：淀粉16g／L,豆饼粉3g／L,蛋白胨3g／L,KH2PO4 0．4g／L,K2HPO4 0．8g／L,MgSO4 0．2g／L,ZnSO4 0．03g／L,pH6．5。采用优化后的培养基条件,酶活力达到156．1U／L,比优化前初始发酵培养条件下的酶活提高了252％,当环氧化物水解酶催化时间为10h时,（s）-环氧氯丙烷的对映体过量值（e．e．）可达99．0％。产率为18．6％。     

不同pH调节剂对补料批式发酵产1,3-丙二醇的影响

对肺炎克雷伯氏菌（Klebsiellapneumoniae）发酵生产1,3-丙二醇（1,3-Propanediol,1,3．PD）的补碱策略进行了研究。分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱。当采用混合碱调控发酵pH值为7．0时,1,3-丙二醇的产量达到了55dL,比无pH调控（对照）发酵过程发酵水平提高了10．6倍。     

丙酮酸钠对E．coli CCTCCM208088发酵生产聚唾液酸的影响

研究了丙酮酸钠对E．coliCCTCCM208088发酵生产聚唾液酸的影响。首先在摇瓶水平上优化了丙酮酸钠的添加策略：发酵初始培养基中添加6g／L丙酮酸钠,聚唾液酸的产量达到最高水平3．47g／L,相比空白相比提高了73％,聚唾液酸产率（YP／（x．s））提高了125％。在30L发酵罐中,添加丙酮酸钠使聚唾液酸产量达到了6．6g／L,相对照提高了53．5％。通过有机酸分析,添加丙酮酸钠增强了菌体内三羧酸循环．可能导致胞内能荷水平的提高．从而促进了聚唾液酸的合成。     

以玉米浆和木薯为原料机械搅拌发酵制备细菌纤维素的研究

本文以玉米浆和木薯为原料,用机械搅拌式发酵罐制备细菌纤维素（BC）,对发酵过程的纤维素产量、还原糖消耗、溶氧变化和茵浓变化进行了监测,并以葡萄糖一蛋白胨-酵母粉培养基为对照进行了比较。实验得出玉米浆作氮源时不溶BC的产量为9．2g／L,而氮源成本只是对照组的15％;木薯水解液作碳源时的不溶BC产量达到11．7g／L,比对照组（10．8g／L）高8％;而用玉米浆搭配木薯水解液发酵生产BC,产量也达到10．1g／L,验证了这两种天然原料的廉价高效性,用于工业生产细菌纤维素具有良好的前景。     

羊肚菌液态发酵的研究*

通过摇瓶正交试验研究了圆锥羊肚菌液体发酵的条件,选出最佳培养基配方、接种量、培养温度、pH、通气量,培养时间等参数。在此基础上,应用VIRTIS公司生产的2L－自控发酵罐进行了分批发酵,摸索到了羊肚菌液态深层发酵的基本规律,然后分别以淀粉和玉米粉为碳源进行了补料分批发酵,获得其干细胞产量为25．4g／L和27．4g／L,生长速率为0．45g／（L·h）和0．51g／（L·h）,以碳源为基准的产量得率系数（yx／s）为0.72（g／g）和0.75（g／g）等数据。实验结果表明,羊肚菌的液态深层发酵已达到了真菌菌丝液态发酵的正常水平。     

羊肚菌液态发酵的研究

通过摇瓶正交试验研究了圆锥羊肚菌液体发酵的条件,选出最佳培养基配方、接种量、培养温度、pH、通气量,培养时间等参数。在此基础上,应用VIRTIS公司生产的2L－自控发酵罐进行了分批发酵,摸索到了羊肚菌液态深层发酵的基本规律,然后分别以淀粉和玉米粉为碳源进行了补料分批发酵,获得其干细胞产量为25．4g／L和27．4g／L,生长速率为0．45g／（L·h）和0．51g／（L·h）,以碳源为基准的产量得率系数（yx／s）为0.72（g／g）和0.75（g／g）等数据。实验结果表明,羊肚菌的液态深层发酵已达到了真菌菌丝液态发酵的正常水平。     

氮源种类及溶氧水平对锁掷酵母产类胡萝卜素组分的影响

在锁掷酵母（Sporidioboluspararoseus）发酵产类胡萝卜紊的过程中,发酵产物中类胡萝卜紊种类繁多,而且性质相似,加大了不同色素分离纯化的难度。为定向积累不同种类的类胡萝卜素,以本实验室保藏锁挪酵母JD-2为出发菌,研究了氮源种类和浓度及溶氧对锁掷酵母产类胡萝卜素的影响,并在7L发酵罐中进行了补料分批发酵试验。发现培养基中同时添加有机氮源和无机氮源且溶氧控制较低（5％）时有利于β-胡萝卜素的大量积累,最佳有机氮源和无机氮源分别为玉米浆（20g／L）、硫酸铵（5g／L）。补料分批发酵时β-胡萝卜素产量达到31．28mg／L,红酵母烯12．38mg／L。培养基中只添加有机氮源且相对溶氧控制相对较高（30％）时有利于红酵母烯的大量积累,最佳有机氮源为酵母膏（20g／L）。补料分批发酵时红酵母烯产量达到38．96mg／L,8．胡萝卜素12．36mg／L。     

Performance improvement of cephalosporin C fermentation by Acremonium chrysogenum with DO-Stat based strategy of co-feeding soybean oil and glucose

Cephalosporin C (CPC) fermentation by Acremonium chrysogenum featured with two major problems: (1) high raw materials cost (low CPC yield from soybean oil) and (2) low oxygen transfer rate between gaseous/aqueous phases leading to low CPC productivity and quality instability of CPC fermentation product due to the accumulation of deacetoxycephalosporin C (DAOC). To solve the problems, in this study, we proposed a novel DO-Stat based co-substrates feeding strategy by simultaneously supplementing soybean oil and glucose, and testified the effectiveness of the strategy in a 7 L bioreactor. The CPC fermentation performance were significantly improved when co-feeding soybean oil and glucose at a weight ratio of 1:0.7, as compared with those when feeding pure soybean oil: (1) final CPC concentration and yield reached higher levels of 37 g/L and 23.5%, the increments were 46% and 82%, respectively; (2) oxygen transfer rate was largely improved, oil consumption rate and CPC productivity were enhanced by 31% and 136%, respectively; and (3) DO could be controlled at adequately high levels so that DAOC accumulation could be minimized and the quality of CPC fermentation product be ensured. The proposed strategy showed application potential in improving the economics of industrial CPC productions.     

甲醇／山梨醇共混诱导改善重组毕赤酵母表达猪a干扰素发酵过程和NADH再生效率

在10L发酵罐中利用重组毕赤酵母诱导表达猪a干扰素（pIFN-a）,考察甲醇／山梨醇共混诱导策略对pIFN-a表达水平提高和能量（NADH）再生效率的影响。结果表明：在诱导稳定期,甲醇／山梨醇共混诱导可弱化细胞的甲醇代谢,有利于缓解毒副中间产物（过氧化氢、甲醛等）的生成积累;以0．785g／（L·h）的速率缓慢共混流加山梨醇时,pIFN-a抗病毒活性最大,最高活性可达1．8×107IU／mL,与30℃常温甲醇单独诱导（最高活性1．0X10。IU／mL）和20℃低温甲醇单独诱导（最高活性1．4×lO6IU／mL）相比,活性均大幅提高,且胞外pIFN-a的降解减缓;发酵体系的抗高甲醇浓度冲击能力有效提高,发酵生产的稳定性增强;能量利用效率大幅提高,NADH的再生利用效率提高了29％-84％。     

甲醇/山梨醇共混流加控制溶氧改善毕赤酵母表达猪圆环病毒Cap蛋白的发酵性能

研究在重组毕赤酵母(GS115,Mut+)表达猪圆环病毒Cap蛋白的发酵过程中,甲醇毒害作用以及溶氧波动影响目的蛋白的正常表达。基于对甲醇和山梨醇代谢途径的分析,将C源流加的手动调节与反馈控制相结合,提出了1种新型的甲醇/山梨醇共混诱导策略,能够将溶氧稳定地控制于某一设定值,同时避免甲醇毒害作用。使用该策略将溶氧控制于20%的批次,C源(甲醇和山梨醇)添加过少,导致Cap蛋白表达量较低(54 mg/L);而将溶氧控制于10%的批次,C源流加速率适宜,Cap蛋白表达量达到198 mg/L,表达水平明显高于采用传统甲醇诱导策略(0 mg/L)和DO-stat诱导策略的批次(121 mg/L)。     

甲醇-山梨醇混合碳源诱导提高抗HER2抗体在糖基工程毕赤酵母中的表达

目的：以抗HER2抗体为模型,研究抗体在糖基工程酵母菌中的表达及工程菌发酵技术。方法：首先通过摇瓶试验分析诱导用甲醇浓度对抗体表达的影响,并用高表达HER2的SK-BR-3细胞分析抗HER2抗体的抗原结合活性。以此为基础,在5 L发酵罐中研究甲醇-山梨醇混合碳源流加诱导对抗HER2抗体表达水平的影响;收集发酵培养液,采用阳离子交换层析对目标产物进行纯化;利用SDS-PAGE、Western印迹、Lowry法对抗体的相对分子质量、浓度等进行分析。结果：摇瓶试验结果表明,甲醇浓度为0.5%时抗体表达量最高,且糖基工程毕赤酵母菌表达的抗HER2抗体具有与SK-BR-3细胞抗原结合的活性;在5 L发酵罐中,利用甲醇和山梨醇混合诱导方式发酵表达抗体,其表达量可提高至0.6 g/L,比摇瓶诱导表达的抗体产量提高了近10倍;非还原SDS-PAGE及Western印迹表明抗体相对分子质量为1.5×105,与商业化抗体Herceptin的大小一致;经过一步阳离子交换层析纯化,纯化后抗体浓度为0.365 g/L。结论：采用甲醇-山梨醇混合碳源诱导方式在5 L发酵罐中进行发酵表达,能够提高抗HER2抗体在糖基工程酵母菌中的表达量,本研究可为抗体在酵母中的规模发酵技术提供重要参考。     

The utilization of beet molasses as a novel carbon source for cephalosporin C production by Acremonium chrysogenum: Optimization of process parameters through statistical experimental designs

In this work, cephalosporin C (CPC) production on pilot scale fermenters of 600l capacity with 350l working volume by Acremonium chrysogenum EMCC 904 was performed. The effects of fermentation medium composition, inoculum concentration, initial pH and aeration rate on CPC production by A. chrysogenum strain was investigated by using response surface methodology (RSM). The Plackett-Burman design which involves two concentrations of each nutrient was effective in searching for the major medium components promoting CPC production. Under our experimental conditions; Soya oil, beet molasses and corn steep liquor were found to be the major factors contributing to the antibiotic production. Subsequently, a Box-Behnken design was used for outlining the concentration of the most effective medium constituents. Estimated optimum composition for the production of CPC was as follows: soya oil, 40g/l; beet molasses, 180g/l; and corn steep liquor, 330g/l. The central composite design was used for outlining the optimum values of the fermentation parameters. Estimated optimum values for the production of CPC are as follows: inoculum level, 10(5.5)spores/ml; initial pH, 4.3; and aeration rate, 9364ml/min.     

响应面法优化多杀菌素发酵培养基的研究

采用响应面分析方法,对刺糖多孢茵（Saccharopolyspora spinosa）H-2产多杀菌素的发酵培养基进行优化研究。运用单因子试验筛选出葡萄糖和棉籽粉为最适碳源和氮源,通过Plack—ett—Burman设计试验,对影响发酵培养基的8个相关因子进行评估并筛选出具有显著效应的4个因子：葡萄糖、棉籽粉、黄豆饼粉及玉米浆。通过最陡爬坡实验逼近以上4个因子的最大响应区域后,采用Box-Behnken响应面分析法,确定发酵产多杀菌素最佳培养基为葡萄糖64．5g,麦芽糖20g,玉米浆2g,大豆油40g,棉籽粉25g,黄豆饼粉2．4g,蛋白胨25g,CaCO35g,定容至1L,pH7．0。培养基优化后多杀菌素产量由278．1mg／L提高到508．7mg／L,比初始多杀茵素产量提高了1．83倍。     

高产γ-氨基丁酸的谷氨酸棒杆菌工程菌的构建和发酵条件优化

为了实现γ-氨基丁酸(GABA)在微生物中"一步法"高效生产,本研究构建出一株高产GABA的谷氨酸棒杆茵工程菌ATCC 13032/pDXW10-gadB1-gadB2,可以直接将自身合成的L-谷氨酸转变成GABA,并对该工程茵的发酵培养基和发酵条件进行了初步优化。结果表明:培养7 h~8 h的种子液按发酵起始OD_(562)=1.6转接至发酵培养基(葡萄糖、玉米浆分别100 g/L、4 g/L),10 h添加PLP至O.1 mmol/L,发酵结束后胞外GABA可达(26.39±1.68)g/L。为工业化"一步法"生产GABA提供理论和实验基础。     

Expression of cefF significantly decreased deacetoxycephalosporin C formation during cephalosporin C production in Acremonium chrysogenum

Deacetoxycephalosporin C (DAOC) is not only the precursor but also one of the by-products during cephalosporin C (CPC) biosynthesis. One enzyme (DAOC/DAC synthase) is responsible for the two-step conversion of penicillin N into deacetylcephalosporin C (DAC) in Acremonium chrysogenum, while two enzymes (DAOC synthase and DAOC hydroxylase) were involved in this reaction in Streptomyces clavuligerus and Amycolatopsis lactamdurans (Nocardia lactamdurans). In this study, the DAOC hydroxylase gene cefF was cloned from Streptomyces clavuligerus and introduced into Acremonium chrysogenum through Agrobacterium tumefaciens-mediated transformation. When cefF was expressed under the promoter of pcbC, the ratio of DAOC/CPC in the fermentation broth significantly decreased. These results suggested that introduction of cefF could function quite well in Acremonium chrysogenum and successfully reduce the content of DAOC in the CPC fermentation broth. This work offered a practical way to improve the CPC purification and reduce its production cost.     

Environmentally safe production of 7-aminodeacetoxycephalosporanic acid (7-ADCA) using recombinant strains of Acremonium chrysogenum

Medically useful semisynthetic cephalosporins are made from 7-aminodeacetoxycephalosporanic acid (7-ADCA) or 7-aminocephalosporanic acid (7-ACA). Here we describe a new industrially amenable bioprocess for the production of the important intermediate 7-ADCA that can replace the expensive and environmentally unfriendly chemical method classically used. The method is based on the disruption and one-step replacement of the cefEF gene, encoding the bifunctional expandase/hydroxylase activity, of an actual industrial cephalosporin C production strain of Acremonium chrysogenum. Subsequent cloning and expression of the cefE gene from Streptomyces clavuligerus in A. chrysogenum yield recombinant strains producing high titers of deacetoxycephalosporin C (DAOC). Production level of DAOC is nearly equivalent (75-80%) to the total beta-lactams biosynthesized by the parental overproducing strain. DAOC deacylation is carried out by two final enzymatic bioconversions catalyzed by D-amino acid oxidase (DAO) and glutaryl acylase (GLA) yielding 7-ADCA. In contrast to the data reported for recombinant strains of Penicillium chrysogenum expressing ring expansion activity, no detectable contamination with other cephalosporin intermediates occurred.