VC二步发酵产酸菌氧化葡萄糖酸杆菌的选育

实验通过紫外线两轮诱变的方法诱变选育氧化葡萄糖酸杆菌（Gluconobacter oxydans）,以实现提高2-酮基-L-古龙酸（2-KLG）产量的目的,获得1株高产2-KLG的菌株G5。结果证明该突变菌株在pH6．5—6．7的发酵培养基中与蜡质芽孢杆菌（Bcillus cereus）混合发酵,G5的平均糖酸转化率提高了13．49％,酸量达到83．6mg／mL,发酵周期缩短了2—3h。经连续10代转接发酵实验,证明其产酸稳定性较好。结论：氧化葡萄糖酸杆菌（Gluconobacter oxydans）的突变体G5提高了糖酸转化率,缩短了发酵周期。     

新组合菌系SCB329—SCB933利用L—山梨糖发酵产生维生素C前体2—酮基—L—…

在分析了新组合菌系ＳＣＢ３２９－ＳＣＢ９３３发酵过程特征的基础上,对流加发酵工艺中的种子培养、ｐＨ、溶氧的控制,以及发酵液初始培养基中的Ｌ－山梨糖浓度和流加起始点进行了优化,获得了比分批发酵更为满意的结果：发酵最终总糖达１３％（ｗ／ｖ）左右,发酵周期４０￣５０ｈ,产２－酮基－Ｌ－古龙酸达１１５－１３０ｍｇ／ｍｌ,克分子转化率达８８ｍｏｌ％左右。     

新组合菌系SCB329-SCB933利用L-山梨糖发酵产生维生素C前体2-酮基-L-古龙酸的研究Ⅲ.发酵过程的特征和条件控制

在分析了新组合菌系ＳＣＢ３２９－ＳＣＢ９３３发酵过程特征的基础上,对流加发酵工艺中的种子培养、ｐＨ、溶氧的控制,以及发酵液初始培养基中的Ｌ－山梨糖浓度和流加起始点进行了优化,获得了比分批发酵更为满意的结果：发酵最终总糖达１３％（ｗ／ｖ）左右,发酵周期４０～５０ｈ,产２－酮基－Ｌ－古龙酸达１１５－１３０ｍｇ／ｍｌ,克分子转化率达８８ｍｏｌ％左右。     

新组合菌系SCB329-SCB933利用L-山梨糖发酵生产维生素C前体——2-酮基-L-古龙酸的研究 Ⅱ.利用L-山梨糖批加技术实现高糖发酵

新组合菌系氧化葡萄糖酸杆菌SCB329-苏芸金芽孢杆菌SCB933能在较长时间内保持高的转化活力且具有极强的抗杂菌污染的特性。在一次投糖分批发酵的基础上,探索在控制溶氧、pH、温度等条件下,分批加入L-山梨糖发酵生产2-酮基-L-古龙酸新工艺。采用新工艺,既充分利用了菌系的优良特性,又避免了高糖浓度可能对菌系造成的不良影响。L-山梨糖最终浓度达到14%（w/v）,产酸120—135g/l,转化率90％左右,发酵周期40—65h。     

一株芽孢杆菌在维生素C二步发酵中对小菌的促进作用

从土壤中分离到1株能更好促使小菌生长和产酸的芽孢杆菌B601,作为伴生菌与巨大芽孢杆菌相比,在生长过程中,发酵液中B601活菌数小于巨大芽孢杆菌,而其芽孢数则多于巨大芽孢杆菌。对B601组成菌系的发酵条件进行优化,得到如下结果：100g／L L-山梨糖、6g／L尿素、10g/L玉米浆、培养温度30℃和发酵周期44h。与巨大芽孢杆菌组成菌系相比其底物,L-山梨糖质量浓度提高了25％,尿素下降了50％．玉米浆质量浓度下降了33％,温度提高了2℃,发酵周期缩短了4h。结果表明：B601作为伴生菌,与巨大芽孢杆菌相比,该菌株明显提高了发酵效率。     

高渗条件下利用蔗糖提升2-酮基-L-古龙酸生产效率

旨在进一步提升维生素C前体2-酮基-L-古龙酸(2-KLG)的生产效率。在详细考察了2-KLG工业化生产过程中渗透压变化规律的基础上,研究了高渗对混合菌系细胞生长和2-KLG合成的影响,提出蔗糖促进伴生菌巨大芽胞杆菌Bacillus megaterium生长,进而促进普通生酮古龙酸菌Ketogulonigenium vulgare生长和产酸的策略。结果表明,2-KLG的积累和碱性物质的流加使渗透压上升了832mOsmol/kg;高渗抑制了巨大芽胞杆菌的生长(15.4%),从而抑制普通生酮古龙酸菌(31.7%)的生长,导致2-KLG产量和生产强度分别下降67.5%和69.3%(以1250mOsmol/kg为例);蔗糖的添加则显著促进巨大芽胞杆菌的生长,使高渗条件下(摇瓶,1250 mOsmol/kg)2-KLG产量(40.6g/L)提高87%;在3L发酵罐中,补加10mmol/L蔗糖使2-KLG发酵周期缩短10.8%,2-KLG生产强度提高10.4%。研究成果为在环境胁迫下提高混菌生产目标代谢产物的产量提供了潜在的策略。     

VC二步发酵新组合菌系的研究

选用苏云金芽孢杆菌与氧化葡萄糖酸杆菌组成一新组合菌系 ,其摇瓶发酵转化率较原菌系提高 4 .83% ,且具有耐受高浓度 (10 % )山梨糖的特性。在 4m3 发酵罐中 ,连续 4批发酵平均转化率较对照菌系提高 8.16 % ,周期缩短 2 3.7%。新菌组合系的发酵转化率与玉米浆浓度成正相关性 ,尿素浓度x2 =1.4 5 % (g/ 10 0mL)时 ,转化率达最大。     

新组合菌系SCB329—SCB933利用L—山梨糖发酵生产维生素C前体—2—酮基…

新组合菌系氧化葡萄糖酸杆菌ＳＣＢ３２９－苏芸金芽杆菌ＳＣＢ９３３能在较长时间内保持高的转化活力且具有极强的抗杂菌污染的特性。在一次投糖分批发酵的基础上,探索在控制溶氧、ＰＨ,温度等条件下,分批加入Ｌ－山梨糖发酵生产２－酮基－Ｌ－古龙酸新工艺。采用新工艺,既充分利用了菌系的优良特性,又避免了高糖浓度可能对菌系造成的不良影响。Ｌ－山梨糖最终浓度达到１４％（Ｗ／Ｖ）,产酸１２０－１３５ｇ／ｌ,转化率９０     

醇醛脱氢酶的分离纯化及其基因文库的构建和筛选

在维生素C的发酵生产过程中,普通生酮基古龙酸菌S2(Ketogulonigenium vulgare)能产生醇醛脱氢酶,将L-山梨糖转化为VC的前体2-酮基-L-古龙酸(2-KLG)。通过超声波破碎菌体、硫酸铵分级沉淀、DEAE Sepharose Fast Flow阴离子交换层析,QSepharose High Performance柱层析等过程,从普通生酮基古龙酸菌S2发酵液中分离纯化了醇醛脱氢酶,并用该纯化酶免疫新西兰兔制备出了合格抗血清。同时,普通生酮基古龙酸菌S2基因组DNA经Sau3AⅠ部分酶切后,与黏粒载体pKC505连接,用包装蛋白进行包装,转染大肠杆菌DH5浕,构建了基因组文库。最后应用免疫酶斑点技术(Dot-ELISA)从12000个克隆子中筛选得到一个阳性克隆K719#。通过检测该基因工程菌的活性,表明K719#具有使L-山梨糖转化为2-KLG的功能,从而使醇醛脱氢酶在大肠杆菌中获得了高效表达,这为简化VC的生产工艺奠定了基础。     

响应面法优化Vc二步发酵新菌系产2-酮基-L-古龙酸的培养基

以短小芽胞杆菌(Bacillus pumilus)HJ-04作为维生素C二步发酵第2步中的伴生菌,促进产酸菌产维生素C(Vitamin C,Vc)前体2-酮基-L-古龙酸(2-keto-L-gulonic acid,2-KGA)的能力强于工业生产用菌株巨大芽胞杆菌(Bacillus megaterium) B2980.采用单因素试验、Plackett-Burman(PB)试验及Box-Behnken试验对影响新菌系发酵产2-KGA的6个因素进行分析优化.结果表明,L-山梨糖、尿素、玉米浆为显著影响因子.最佳产酸条件为L-山梨糖94.95 g/L,尿素11.99 g/L,玉米浆14.13g/L.优化后产酸量提高12.31 mg/mL,产酸周期缩短6h.     

生黑醋酸杆菌在高浓度山梨醇下的半连续发酵特性

目的：调节生黑醋酸杆菌生物和代谢特性,以提高发酵效率。方法：通过改变种液特性,采用半连续培养的方式,对生黑醋酸杆菌在高醇浓度下的生长特性进行了研究。结果：通过优化可以提高VC一步发酵底物山梨醇浓度达38%,32h左右发酵率达95%,山梨糖产量达360mg/ml,半连续培养连续5批之间产糖稳定,没有明显差别。结论：通过优化,有效地提高了山梨糖的产率。     

羊毛生物整理复合酶L86发酵工艺优化研究

采用L9（34）正交试验对L86复合酶生产菌的发酵培养基进行优化、并通过溶氧浓度调节和中期补加蛋白水解液对发酵过程进行调控。结果表明较优的培养基组成为（g/100ml）：黄豆粉4.0、玉米粉1.0、鱼粉0.6、蚕蛹粉0.6、CaCl20.5、NH4Cl1.0、Na2HPO4·2H2O 0.4;通气量控制30h前1:0.5、30-50h1:1.0、50h后1:1.2 v/v/m。在上述条件下摇瓶,酸性蛋白酶酶活10000u/ml、纤维素CMC酶3600u/ml;在0.5m3搅拌罐中扩大中试平均发酵单位酸性蛋白酶5500u/ml、纤维素CMC酶2200u/ml。     

Vc生产菌“神舟七号”搭载育种

选取3株性状不同的Vc二步发酵生产菌搭载于"神舟七号"飞船进行空间诱变,返回地面后,经富集培养和分离,获得近12000株诱变菌株。采用试管微量培养并监测pH值法作3次初筛,获300余株优良株,再经摇瓶发酵定酸、糖法作3次复筛,选出12株优良菌株。新菌株摇瓶发酵转化率提高了5%～7%。研究了新菌株生产的最适发酵条件,调整了部分工艺过程,应用于大生产,转化率提高4%～5%。     

过量表达自身hemA基因的重组大肠杆菌发酵生产5-氨基乙酰丙酸的研究

研究了优化重组大肠杆菌产5-氨基乙酰丙酸（ALA）的条件,提高大肠杆菌发酵生产AL气的产量。在测定重组大肠杆菌GT48的生长曲线的基础上,确定诱导时间,优化摇瓶发酵条件。然后,进一步在5L发酵罐上进行间歇和流加发酵研究。摇瓶实验表明,细胞培养最佳初始pH为6．5,最佳诱导时间为稳定期前期,最佳接种量为2％,过高的葡萄糖浓度对细胞生长和产物合成均有一定的抑制作用。在5L发酵罐间歇发酵中,重组菌产ALA能力达到47．8mg／L。采用流加发酵可以进一步将产物产量提高到63．8mg／L。构建的过量表达自身的hemA基因的大肠杆菌具有较高的产ALA能力,通过发酵条件优化和采用流加发酵可以提高AL气产量。     

Optimized synthesis of L-sorbose by C(5)-dehydrogenation of D-sorbitol with Gluconobacter oxydans

The optimization of L-sorbose synthesis by regiospecific dehydrogenation of D-sorbitol using Gluconobacter oxydans is reported. The current L-sorbose production processes that are based on G. oxydans and other bacterial strains are suboptimal as to yield and rate of L-sorbose synthesis. One reason for these problems is the toxicity that is induced by the substrate D-sorbitol when used in concentrations of >10% (w/v). This phenomenon significantly limits the potentials of L-sorbose production from an industrial point of view. The goal of this study was to develop a fast production process that yields L-sorbose in stoichiometric amounts starting from D-sorbitol concentrations that exceed 10% (w/v). A gradual improvement of the inoculum build-up procedure, culture medium composition, and process parameters ultimately led to a theoretically maximal L-sorbose productivity (200 g L(-1) of L-sorbose from 200 g L(-1) of D-sorbitol in 28 h of fermentation) using a Gluconobacter oxydans mutant strain that was selected under conditions of substrate inhibition. Because the D-sorbitol/L‐sorbose bioconversion is used to mass-produce vitamin C, the procedure reported here will contribute to a more efficient and more economic synthesis of vitamin C.     

Effects of environmental conditions and methanol feeding strategy on lipase-mediated biodiesel production using soybean oil

Methanol is a commonly used acyl acceptor for lipase-driven biodiesel production, but a high concentration of methanol is detrimental for lipase activity. To overcome this drawback, a simple fed-batch process was developed by optimization of the methanol feeding strategy and reaction conditions. For the feeding strategy, an equal volume of pure methanol was fed twice with specified time intervals into a reactor initially containing a 1:1 molar ratio of soybean oil to methanol in order to adjust the net molar ratio of the oil to methanol to 1:3. In contrast with the batch reaction, a higher agitation speed in the fed-batch process elevated the conversion yield of soybean oil to biodiesel. An agitation speed of 600 rpm and a reaction temperature of 70°C were chosen as the optimal environmental conditions. Residual lipase activities for the fed-batch operation at 40 ∼ 70°C and 600 rpm were 7.1 ± 1.4 times higher than that of the batch method at 40°C with the same agitation speed, indicating that methanol feeding can prevent significant deactivation of lipase. Finally, two times feeding methanol at 2 and 6 hr resulted in a biodiesel productivity of 10.7%/h and 94.9% final conversion yield under the optimal conditions.     

L-缬氨酸的发酵工艺研究

目的:以黄色短杆菌XV0505为生产菌株,探讨发酵培养基和发酵控制条件对L-缬氨酸的产量和糖酸转化率的影响。方法:应用单因素实验确定发酵的工艺条件;利用纸层析-色斑洗脱比色法测定发酵液中L-缬氨酸的含量。结果:在最优发酵条件下,通过10L罐流加发酵72h,产酸量可达53.4g/L,糖酸转化率为26.7%,分别比补料分批发酵提高11.9%和3.5%。结论:环境因子和发酵控制工艺对发酵生产L-缬氨酸具有重要影响。     

Cloning and nucleotide sequencing of the membrane-bound L-sorbosone dehydrogenase gene of Acetobacter liquefaciens IFO 12258 and its expression in Gluconobacter oxydans.

Cloning and expression of the gene encoding Acetobacter liquefaciens IFO 12258 membrane-bound L-sorbosone dehydrogenase (SNDH) were studied. A genomic library of A. liquefaciens IFO 12258 was constructed with the mobilizable cosmid vector pVK102 (mob+) in Escherichia coli S17-1 (Tra+). The library was transferred by conjugal mating into Gluconobacter oxydans OX4, a mutant of G. oxydans IFO 3293 that accumulates L-sorbosone in the presence of L-sorbose. The transconjugants were screened for SNDH activity by performing a direct expression assay. One clone harboring plasmid p7A6 converted L-sorbosone to 2-keto-L-gulonic acid (2KGA) more rapidly than its host did and also converted L-sorbose to 2KGA with no accumulation of L-sorbosone. The insert (25 kb) of p7A6 was shortened to a 3.1-kb fragment, in which one open reading frame (1,347 bp) was found and was shown to encode a polypeptide with a molecular weight of 48,222. The SNDH gene was introduced into the 2KGA-producing strain G. oxydans IFO 3293 and its derivatives, which contained membrane-bound L-sorbose dehydrogenase. The cloned SNDH was correctly located in the membrane of the host. The membrane fraction of the clone exhibited almost stoichiometric formation of 2KGA from L-sorbosone and L-sorbose. Resting cells of the clones produced 2KGA very efficiently from L-sorbosone and L-sorbose, but not from D-sorbitol; the conversion yield from L-sorbosone was improved from approximately 25 to 83%, whereas the yield from L-sorbose was increased from 68 to 81%. Under fermentation conditions, cloning did not obviously improve the yield of 2KGA from L-sorbose.