L-山梨糖流加发酵高效生产2-酮基-L-古龙酸

实验充分利用混合菌系氧化葡萄糖酸杆菌(Gluconobacter oxydans)和蜡状芽孢杆菌(Bacillus cereus)混合发酵的优良特性,通过在发酵过程中间歇流加L-山梨糖的方法,实现了在自动控制温度、pH和溶氧的条件下,高效发酵L-山梨糖生成2-酮基-L-古龙酸(2-KLG)的目的。结果表明：当将L-山梨糖的终浓度调高到14％(w／v)时,2-KLG产量为130mg／mL左右,转化率达90％,发酵周期40—60h之间。结论：发酵过程中间歇流加L-山梨糖可以解除高浓度糖对产酸的抑制作用,提高了糖的转化率,但是发酵周期略有延长。     

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.     

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。     

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 Ⅰ.新组合菌系SCB329-SCB933的生物学特性

采用紫外照射、化学诱变和原生质融合等方法选育到一株性状更优良的突变株SCB329,并与新筛选的一株芽孢杆菌SCB933搭配组成新的组合菌系。产酸小菌SCB329与其亲本菌株氧化葡萄糖酸杆菌性状相似。伴生大菌SCB933属苏芸金芽孢杆菌（B.thuringiensis）。新组合菌系利用L-山梨糖的发酵液提取后经纸层析,元素分析和红外吸收光谱等项鉴定,其发酵产物确系2-酮基-L-古龙酸,对新组合菌系的生物学特性也进行了研究。     

巨大芽孢杆菌B．m2980产孢对氧化葡萄糖酸杆菌产酸的影响

为确定维生素C二步发酵中巨大芽孢杆菌（伴生菌）芽孢形成对氧化葡萄酸杆菌（产酸菌）产酸的影响,本研究通过对巨大芽孢杆菌生长特性分析,选取培养12h（未形成芽孢）和36h（芽孢大量形成）巨大芽孢杆菌B．m2980,检测其胞外液、胞内液以及混合液对产酸菌生成2-酮基-L-古龙酸的影响。结果表明,在未开始形成芽孢时,伴生菌胞外液、胞内液及混合液对产酸菌的生长和产酸有较低的促进作用,其中胞内液的促进能力大于胞外液;在芽孢生成后,胞外液以及混合液对产酸菌生长和产酸的促进能力显著提高。     

VC三菌种一步发酵方法的构建与研究

就维生素C微生物一步发酵方法进行了探索,构建了酮古龙酸杆菌、氧化葡萄糖酸杆菌和芽孢杆菌三菌混菌一步发酵的方法。研究发现,植物内生芽孢杆菌可以与酮古龙酸杆菌配合,促进酮古龙酸杆菌生长和产酸。在有山梨醇存在的条件下酮古龙酸杆菌及其伴生菌能够快速地生长增殖,植物内生芽孢杆菌在发酵的10h中不断消耗山梨醇。5L的发酵罐中,酮古龙酸杆菌、氧化葡萄糖酸杆菌和植物内生芽孢杆菌三菌混菌一步发酵在恒定的30℃温度,600r/min搅拌速度和1.5vvm通气条件下,补料发酵过程中醇酸质量转化率达到了81.89%,在分批发酵过程中,醇酸质量转化率达到了87.90%,进一步优化了维生素C生产工艺。     

混合菌发酵L-山梨糖生产Vc前体2-酮基-L-古龙酸研究进展

利用混合菌发酵L-山梨糖生产2-酮基-L-古龙酸(2-KCA),再经化学转化合成维生素C(Vc),是我国工业生产Vc的主要途径,具有简化工艺,减少污染,降低能耗等诸多优点.从菌系组合、菌种选育、代谢途径与酶学特性、工程菌构建、伴生作用机制及发酵工艺等方面出发,综述混合菌发酵L-山梨糖生产Vc前体2-KGA的研究现状和最新进展,并提出进一步研究和探索的方向.     

维生素C二步发酵中巨大芽孢杆菌对氧化葡萄糖酸杆菌生长和产酸的影响

通过测定氧化葡萄糖酸杆菌转化L－山梨糖中成ZKGA的细胞酶活性、摇瓶发酵及中长变化,研究了Vc:步发酵中巨大茅孢杆菌对氧化葡萄糖酸杆菌生长和产酸作用的影响。结果显示：巨大芽孢杆菌胞外液和胞内液均可促进氧化葡萄糖酸杆菌的增殖,主要表现为缩短其中长周期中的延迟期;巨大芽孢杆菌通过所产生的部分生物活性物质增强氧化葡萄糖酸杆菌产酸的细胞酶活性,促进氧化葡萄糖酸杆菌转化L一山梨糖生成2KGA.     

分阶段pH调控提高2-酮基-L-古龙酸生产

为了提高酮古龙酸菌Ketogulonicigenium vulgare和巨大芽胞杆菌Bacillus megaterium生产2-酮基-L-古龙酸(2-KLG)的生产效率,分析了pH对K.vulgare和B.megaterium生长和产酸的影响,发现K.vulgare和B.megaterium的最适生长pH值分别为6.0和8.0,但是K.vulgare的糖酸转化活力在pH7.0时达到最大值,因此提出了三阶段pH控制策略(第一阶段:0～8h,pH8.0;第二阶段:8～20h,pH6.0;第三阶段:20h至发酵结束,pH7.0)以促进K.vulgare生长和2-KLG生产。结果表明,三阶段pH控制策略的实施进一步提高了2-KLG的产量(77.3g/L)、生产强度(1.38g/(L·h))和L-山梨糖消耗速率(1.42g/(L·h)),分别比恒定pH7.0时提高了9.7%、33.2%和25.7%。     

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…

采用紫外照射,化学诱变和原生质融合等方法选育到一株性状更优良的突变株ＳＣＢ３２９,并与新筛选的一株芽孢杆菌ＳＣＢ９３３搭配组成新的组合菌系,产酸小菌ＳＣＢ３２９与其亲本菌株氧化葡萄糖酸杆菌性状相似,伴生大菌ＳＣＢ９３３属苏芸金芽孢杆菌（Ｂ．ｔｈｕｒｎｇｉｅｎｓｉｓ）,新组合菌系列Ｌ－山梨糖的发酵液提取后经纸层析,元素分析和红外吸收光谱等项鉴定,其发酵产物克系２－酮基－Ｌ－古龙酸,对新组合菌系的生物     

一株产D-海因酶菌株的鉴定及离子束诱变选育

首次报道了产D-海因酶的巨大芽孢杆菌,通过对该菌进行离子束诱变,获得酶活最高增加3倍的突变株M5,对M5的产酶条件进行优化,得到最佳的发酵条件为玉米浆1.5%,葡萄糖1%,油酸1.5%,氯化钠0.5%,并添加50 mg.L-1的Mn2+、Zn2+及500 mg.L-1的Mg2+,pH8.0,30℃发酵24 h,酶活力可达到每毫升2.119 U,比优化前突变株提高了300%,比出发菌株提高了850%。     

Galactomyces geotrichum Y25产脂肪酶条件的优化

应用响应面法对Galactomyces geotrichumY25液体发酵产脂肪酶的条件进行了优化。首先采用Plackett-Burman设计对影响产酶因素的效应进行评价,筛选出黄豆粉、玉米浆和发酵时间3个对产酶影响显著的因素。用最陡爬坡路径逼近最大产酶区域后,利用响应面设计对显著因素进行优化,得出黄豆粉、玉米浆最佳质量分数分别为2.51%、2.12%,最佳发酵时间101.95 h。优化后液体发酵液中脂肪酶活力提高到34.65 U/mL,比初始酶活力9.6 U/mL提高了3.61倍。表明响应面法可显著优化Galactomyces geotrichumY25液体发酵产脂肪酶条件。     

Citric acid production by a novel Aspergillus niger isolate: II. Optimization of process parameters through statistical experimental designs

In this work, sequential optimization strategy, based on statistical designs, was employed to enhance the production of citric acid in submerged culture. For screening of fermentation medium composition significantly influencing citric acid production, the two-level Plackett-Burman design was used. Under our experimental conditions, beet molasses and corn steep liquor were found to be the major factors of the acid production. A near optimum medium formulation was obtained using this method with increased citric acid yield by five-folds. Response surface methodology (RSM) was adopted to acquire the best process conditions. In this respect, the three-level Box-Behnken design was applied. A polynomial model was created to correlate the relationship between the three variables (beet molasses, corn steep liquor and inoculum concentration) and citric acid yield. Estimated optimum composition for the production of citric acid is as follows pretreated beet molasses, 240.1g/l; corn steep liquor, 10.5g/l; and spores concentration, 10(8)spores/ml. The optimum citric acid yield was 87.81% which is 14 times than the basal medium. The five level central composite design was used for outlining the optimum values of the fermentation factors initial pH, aeration rate and temperature on citric acid production. Estimated optimum values for the production of citric acid are as follows initial pH 4.0; aeration rate, 6500ml/min and fermentation temperature, 31.5 degrees C.     

响应面分析法优化黑根霉胞外多糖发酵工艺

实验以商品化的马铃薯葡萄糖液体培养基为基础培养基,以胞外粗多糖产量为考察指标,运用响应面分析法考察玉米浆浓度、KH₂PO₄浓度和发酵时间3个因素对胞外多糖发酵产量的影响,以获得黑根霉胞外多糖发酵最优工艺,建立高产、稳定、可控的胞外多糖发酵生产工艺技术方案。经响应面分析,各因素按照对响应值的影响顺序为：玉米浆浓度>发酵时间> KH₂PO₄浓度,且玉米浆浓度、发酵时间对胞外多糖产量的影响极显著,KH₂PO₄浓度对胞外多糖产量的影响不显著。胞外多糖发酵最优工艺为：玉米浆3.2mg/mL、KH₂PO₄ 1.5mg/mL和发酵时间132h,在此条件下胞外多糖的最大预测产量为0.824mg/mL。实验重复性好,是一个高产、稳定、可控的胞外多糖发酵生产工艺技术方案,可以指导黑根霉胞外多糖发酵。     

玉米浆对玉米粉和木薯淀粉发酵甘油的影响及二者的比较

以玉米粉和木薯淀粉为原料 ,比较了二者的液化和糖化 ,结果表明 :在相同条件下 ,木薯淀粉液化时间较短 ,玉米粉液化时间较长 ,但二者的液化液均较易糖化。然后分别以玉米粉和木薯淀粉糖化液为原料 ,用耐高渗酵母发酵生产甘油 ,研究了玉米浆对二者甘油发酵的影响并对二者进行了比较 ,结果表明 :当玉米粉和木薯淀粉糖化液还原糖含量分别为 2 5 % ,尿素为 0 .2 % ,pH为 4 .5时 ,用玉米粉糖化液发酵甘油时可不添加玉米浆 ,甘油产量最高可达 2 % ,而用木薯淀粉糖化液发酵甘油时 ,适宜的玉米浆为 0 .15 % ,甘油产量最高可达 4 .9%。对二者的比较结果表明 :用玉米粉糖化液为发酵原料时 ,发酵时间较短 ,残糖降低较快 ,甘油产量较低 ,在 36h之后 ,甘油开始反耗。而用木薯淀粉糖化液发酵时 ,发酵时间较长 ,残糖降低较慢 ,甘油产量较高 ,在 72h之后 ,甘油开始反耗。     

产琥珀酸工程菌株的发酵工艺条件优化

对实验室构建的产琥珀酸大肠杆菌工程菌株(E.coliQZ1111)进行发酵工艺条件研究。以AM1低盐培养基为基础,研究不同C、N源及其质量浓度,培养基初始pH和发酵温度等因素对琥珀酸的影响,并在5L发酵罐中进行了补料-分批发酵实验。优化后的发酵条件为葡萄糖20g/L,玉米浆10g/L,pH6.4,发酵温度37℃。在5L发酵罐中培养,琥珀酸产量达到47.9g/L。     

Production of a novel polygalacturonic acid bioflocculant REA-11 by Corynebacterium glutamicum

The production of a novel polygalacturonic acid bioflocculant REA-11 from a newly isolated strain, Corynebacterium glutamicum CCTCC M201005, was investigated. Sucrose was chosen as a carbon source for REA-11 production. Complex nitrogen sources containing urea and an organic nitrogen compound enhanced both bacterial growth and REA-11 production, among which urea plus corn steep liquor was shown to be the most efficient combination. A cost-effective medium for REA-11 production mainly comprised 17 g/l sucrose, 0.45 g/l urea, and 5 ml/l corn steep liquor, under which conditions the flocculating activity reached 390 U/ml. The molar ratio of carbon to nitrogen (C/N) significantly affected REA-11 production, where a C/N ratio of 20:1 was shown to be the best. Interestingly, by simultaneously feeding sucrose and urea at a C/N ratio of 20:1 at 24 h of fermentation, REA-11 production (458 U/ml) was enhanced by 17% compared to the control. In a 10 l jar fermentor, lower dissolved oxygen tension was favorable for REA-11 production: a flocculating activity of 520 U/ml was achieved at a kappaLa of 100 h(-1). REA-11 raw product is relatively thermo-stable at acidic pH ranges of 3.0-6.5. Preliminary application studies showed that REA-11 had stronger flocculating activity to Kaolin clay suspension compared to chemical flocculants. In addition, the capability of decolorizing molasses wastewater indicates the industrial potential of this novel bioflocculant.     

菊糖芽孢乳杆菌DS2-18中试规模的D-乳酸发酵研究

研究了菊糖芽孢乳杆茵DS2的突变株DS2-18在中试规模的D-乳酸发酵.在容积为300L自控发酵罐中,DS2-18茵在合适的发酵条件下,即培养基组成(g/L):葡萄糖120,玉米浆8,蛋白胨6,豆粕水解液100,接种量8%(v/v),发酵温度40℃,以轻质碳酸钙作为中和剂调pH 5～6,发酵期间交替不通气和通气,发酵6...     

Solid-state fermentation-supported enhanced production of α-galactosidase by a deoxyglucose-resistant mutant of <Emphasis Type="Italic">Aspergillus niger</Emphasis> and thermostabilization of the production process

The aim of the present investigation was to comparatively evaluate the behaviour of A. niger and its derepressed mutant in production of α-galactosidase in submerged (SmF) and solid state fermentation (SSF) using basal Vogel’s medium or corn steep liquor as nitrogen source and observe the response of latter source under both cultural techniques under different temperature regimes, and determine if SSF can be exploited in a wide range of temperature expected to vary in this fermentation system. All studies were performed in both systems under pre-optimized cultural conditions. Higher melting temperature and negative values of entropy of activation in SSF indicated that the genetic system of both organisms was thermodynamically resistant in the presence of corn steep liquor but sensitive to inactivation in the presence of Vogel’s nitrogen sources in submerged fermentation. This was reflected as the organisms demanded higher magnitudes of energy for product formation in the presence of ammonium salts. Studies on influence of corn steep liquor revealed that it had stabilizing effect too in both fermentation systems but the mutant strain was more stable in both fermentation systems. Because of these properties, the mutant organism may be exploited for bulk production of α-galactosidase in SSF under condition where temperature may fluctuate during fermentation.