烷烃发酵产生1，13-十三碳二元酸及其诱导作用的研究

从能利用正十二烷产生1,12-十二碳二元酸的热带假丝酵母突变株D28出发,经两次紫外线照射诱变,选育到一株从正十三烷产生1,13-十三碳二元酸较高的突变株2—23号菌。该突变株较出发菌株提高产酸率20％,达40．4g／L。突变株2—23也能将一定链长的长链烷烃以较高的产率转变成相应的单一二元酸。此外,在产酸摇瓶条件试验中观察到烷烃的诱导作用,使突变株产酸能力得以提高。用烷烃预培养的种子发酵正十三烷,其产生1,13一十三碳二元酸的量较糖质碳源培养的种子发酵时要提高30％。     

烷烃发酵产生1，13-十三碳二元酸及其诱导作用的研究

从能利用正十二烷产生1,12-十二碳二元酸的热带假丝酵母突变株D28出发,经两次紫外线照射诱变,选育到一株从正十三烷产生1,13-十三碳二元酸较高的突变株2—23号菌。该突变株较出发菌株提高产酸率20％,达40．4g／L。突变株2—23也能将一定链长的长链烷烃以较高的产率转变成相应的单一二元酸。此外,在产酸摇瓶条件试验中观察到烷烃的诱导作用,使突变株产酸能力得以提高。用烷烃预培养的种子发酵正十三烷,其产生1,13一十三碳二元酸的量较糖质碳源培养的种子发酵时要提高30％。     

抗药性突变肌苷高产菌的选育

以枯草芽孢杆菌(Bacillur subtilis)22为出发菌株,经紫外线诱变,分别获得对链霉素(Sm)、盐酸羟胺(Hc)、叠氮化钠(Sa)有抗性的突变株,产肌苷均明显高于出发株。其中链霉素抗性突变株Sm-37-18产肌苷最高,在最佳发酵条件下,产肌苷达19.49g/L,较出发株提高38.4%,发酵周期由60小时缩短至48小时。     

利用微生物混合培养技术生产聚羟基烷酸(PHA)研究

研究了圆褐固氮菌(Azotobacter chroococcum)突变株G3与巨大芽孢杆菌(Bacillus megaterium)G6发酵生产聚羟基烷酸(PHA)的人工可配伍性,确定了它们混合培养的适宜条件,先将G3菌株发酵培养24～28 h后,再以15%(v/v)接种量接入G6菌株并同时补加05%(g/g)蛋白胨(FP)和0.5%(g/g)NH4NO3,继续混合培养42～46h,细胞干重达32 g/L,PHA含量为80%,再结合补料技术最终生物量可达53 g/L,PHA产生量达42.4 g/L。糖对PHA的转化率为0.32。人工混合培养成功地解决了固氮菌发酵生产PHA过程中,发酵液粘度过高,传质较差,补糖总量上不去等技术问题。     

十二碳二元酸的发酵研究

热带假丝酵母(Candidatropicalis)UH248菌株在单因子实验的基础上经过正交实验后,以正十二烷发酵生成十二碳二元酸的产酸量从817g/L提高到1082g/L。而其二元酸产品的纯度(>97%)满足工业生产的需要。吐温60010%、尿素012%、维生素B2150μg/L、青霉素150μ/mL、丙氨酸050%的浓度时也对十二碳二元酸产量有促进作用。用一株以UH248为母株诱变筛选的新的优良突变株HP12菌株,在最佳条件下,20m³罐中发酵151h,十二碳二元酸的平均产量达2021g/L。     

复合诱变对米曲霉产曲酸的影响

发酵法生产曲酸还未实现大规模工业化生产的原因之一是曲酸菌种产酸率较低,本文以平展米曲霉（Aspergillus oryzae effusus)AS32为出现菌株,经UV和^60Co诱变处理,筛选获得一株高产曲酸变异株AUR163,以葡萄糖为碳源,酵母膏为氮源,32℃摇瓶和30L罐发酵培养4天,产酸达6．8g/100mL。平均生产效率为17．0g/L.d最高可达30．5g/L.d比出发菌AS32提高190％以上,这表明UV和^60Co作诱剂,可以大幅度提高米曲霉的曲酸生产效率。     

L－缬氨酸发酵供氧与补料过程控制的研究

高产缬氨酸的北京棒杆菌(corynebacterium pekinense)突变株125菌株,在2．6L自控发酵罐上分批培养结果表明,当发酵中后期DO为零时,产酸量较多。也可用kL。值为指标来调节过程的供氧强度,Kla=90．75h^-1时,产酸量最高。同时比较了恒速连续补加葡萄糖液,当F=3．75g／b时,产酸较高。由此获得了该菌株L一缅氨酸发酵的低供氧与恒速补糖的控制模式。总糖量为16．85％的发酵,可使产酸量达38．2g／L,转化率为22．67％。本文对有关试验结果,进行了发酵动力学的分析和讨论。     

E.aero高产13-丙二醇菌株选育及发酵培养基研究(Ⅰ)

以淡水湖泊泥土中分离出的 30 0多株肠杆菌 (Enterobacter)为出发菌株 ,利用常规筛选方法选出 2株 1 3 丙二醇产生菌 (Enterobacteraerogenes)。经UV、DES、NTG、EMS、LiCl单独及复合诱变 ,选育出一株 (E aero N 56) 1 3 PD高产突变株。通过单因素实验 ,确定了E aero N 56菌株 1 3 PD发酵培养基为 :甘油 90g L ,NH4Cl₁ 50g L     

ε-聚赖氨酸高产菌株选育及分批发酵的研究

以北里孢菌(Kitasatospora sp.)PL6-3为出发菌株,经硫酸二乙酯诱变,获得遗传性能稳定的AECr突变株MY5-36。MY5-36摇瓶发酵产ε-聚赖氨酸达1.17 g/L,是出发株PL6-3的3倍;5 L发酵罐批式发酵产酸达7.72 g/L,较出发菌株提高了7倍以上。与PL6-3相比,MY5-36菌株形态发生了很大变化,菌丝和孢子颜色都发生了改变。     

积累L-苹果酸的米根霉突变株酶活性初探

对富马酸产生菌株—米根霉ME-F10进行诱变育种的过程中, 得到一株性能稳定的高效积累L-苹果酸的突变株ME-M15。该菌株发酵96 h平均L-苹果酸产量达16.3 g/L, 较出发菌株L-苹果酸积累量平均提高3倍, 而富马酸和乙醇的积累量大幅下降。对突变株代谢途径关键酶活研究表明, 突变株富马酸酶胞质途径同功酶和乙醇脱氢酶活力较之出发菌株酶活力明显减弱, 而丙酮酸羧化酶活力无明显差别。     

采用玉米秸秆水解糖和玉米浆发酵生产丁二酸

研究了以玉米秸秆水解糖为碳源,不同氮源条件下琥珀酸放线杆菌Actinobacillus succinogenesSF-9的丁二酸发酵产酸能力。结果表明玉米浆可以替代酵母膏作为丁二酸发酵的廉价氮源。厌氧摇瓶丁二酸发酵单因素试验,得到在初糖浓度50 g/L时,玉米浆的较佳用量为20 g/L。在5 L搅拌罐上,考察了不同初始玉米秸秆水解糖浓度对A.succinogenes SF-9发酵生产丁二酸的影响,结果显示高初始秸秆糖浓度对琥珀酸放线杆菌的生长有抑制作用。采用补料分批发酵,发酵60 h丁二酸的产量达到42.7g/L,丁二酸产率82.7%,生产强度0.81 g/(L·h)。丁二酸的产量和生产强度较分批发酵有明显提高。     

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).     

Enhanced production of periplasmic interferon alpha-2b by Escherichia coli using ion-exchange resin for in situ removal of acetate in the culture

The possibility of using in situ addition of anion-exchange resin for the removal of acetate in the culture aimed at improving growth of E. coli and expression of periplasmic human interferon-α2b (PrIFN-α2b) was studied in shake flask culture and stirred tank bioreactor. Different types of anion-exchange resin were evaluated and the concentration of anion-exchange resin was optimized using response surface methodology. The addition of anion-exchange resins reduced acetate accumulation in the culture, which in turn, improved growth of E. coli and enhanced PrIFN-α2b expression. The presence of anion-exchange resins did not influence the physiology of the cells. The weak base anion-exchange resins, which have higher affinity towards acetate, yielded higher PrIFN-α2b expression as compared to strong anion-exchange resins. High concentrations of anion-exchange resin showed inhibitory effect towards growth of E. coli as well as the expression of PrIFN-α2b. The maximum yield of PrIFN-α2b in shake flask culture (501.8 μg/L) and stirred tank bioreactor (578.8 μg/L) was obtained at ion exchange resin (WA 30) concentration of 12.2 g/L. The production of PrIFN-α2b in stirred tank bioreactor with the addition of ion exchange resin was about 1.8-fold higher than that obtained in fermentation without ion exchange resin (318.4 μg/L).     

Microbial degradation of quinoline: Kinetic studies with Comamonas acidovorans DSM 6426

The microbial degradation of quinoline by Comamonas acidovorans was studied in a laboratory scale stirred tank reactor. In continuous culture experiments using quinoline as a sole source of carbon and nitrogen, it was shown by means of mass balances that quinoline was converted completely to biomass, carbon dioxide, and ammonia. Degradation rates up to 0.7 g/L h were obtained. Measured yield coefficients Y(x/s) for quinoline were about 0.7 g/g, which is in agreement with the theoretical value for complete mineralization. Kinetic constants based on Haldane substrate inhibition were evaluated. The values were mu(max) = 0.48 h(-1), K(i) = 69 mg/L, and K(s) < 1.45 mg/L. (c) 1993 John Wiley & Sons, Inc.     

Selectivity in citric acid production by Yarrowia lipolytica

This experimental study reports about production selectivity in the fermentation of glucose to citric acid by Yarrowia lipolytica as a function of substrate concentration. Batch runs featuring biomass growth and one or two citric acid production phases were carried out in a 15-l stirred tank fermentor. The presented results demonstrate that working at high initial substrate concentration in the production phase is beneficial both in terms of a higher production rate of citric acid, the desired metabolite (reaching 0.077 h(-1)) and of a higher utilization degree of the employed carbon source (yield up to 0.384 g(c.a.)/g(glucose)). The production rate of isocitric acid, the major undesired metabolite, was found to be practically constant over the tested initial substrate concentration range.     

提高光滑球拟酵母乙酰辅酶A水平促进a-酮戊二酸合成

【目的】为了了解光滑球拟酵母中乙酰辅酶A含量对其碳代谢及其通量的影响。【方法】将来源于酿酒酵母中编码乙酰辅酶A合成酶ACS2基因过量表达于发酵法生产丙酮酸的生产菌株Torulopsis glabrata中,获得了一株乙酰辅酶A合成酶活性提高9.2倍(1.20 U/mg protein)的重组菌T. glabrata ACS2-1。【结果】与出发菌株WSH-IP303相比,重组菌T. glabrata ACS2-1：(1)能以乙酸为唯一碳源在胞内积累0.94 mmol/(L·g DCW)的乙酰辅酶A;(2)以葡萄糖为唯一碳源时胞内乙酰辅酶A浓度、a-酮戊二酸产量和Ca-KG/Cpyr是出发菌株WSH-IP303 的3.22、2.05和2.52倍;(3)在葡萄糖培养基中添加4 g/L乙酸,使乙酰辅酶A浓度、a-酮戊二酸产量和Ca-KG/Cpyr是出发菌株WSH-IP303的4.55、2.47和3.75倍,a-酮戊二酸浓度达到17.8 g/L。【结论】这一结果表明,改变细胞内关键辅因子的浓度能使碳代谢流的流向与通量发生改变,从积累丙酮酸转向过量积累a-酮戊二酸。     

液蜡发酵制取混合二元酸的研究

A mutant of Candida tropicalis FYD-2 was obtained from its parental strain SFP-1186 by ultraviolet treatments.On shaking flask,the yield of mixed dicarboxylic acid(DCA) by the mutant was 21.4% higher than that by its ancestor.The amount of mixed DCA reached 156g/L for 120h incubation in a 10 L autoconrolled fermentor where the culture medium contained 25% n-paraffin.The process of induced and screening mutant was introduced and the time course of fermentation in 10 L fermentor was discussed.     

Whole-cell bio-oxidation of n-dodecane using the alkane hydroxylase system of P. putida GPo1 expressed in E. coli

The alkane-1-monoxygenase (alkB) complex of Pseudomonas putida GPo1 has been extensively studied in the past and shown to be capable of oxidising aliphatic C(5)-C(12) alkanes to primary alcohols both in the wild-type organism by growth on C(5)-C(12) alkanes as sole carbon source and in vitro. Despite this, successful n-dodecane oxidation for the production of 1-dodecanol or dodecanoic acid has proven elusive in the past when using alkB-expressing recombinants. This article demonstrates, for the first time in vivo, by using the Escherichia coli GEC137 pGEc47ΔJ strain, that n-dodecane oxidation using this enzyme for the production of primary alcohols and carboxylic acids is feasible and in fact potentially more promising than n-octane oxidation due to lower product and substrate toxicity. Yields are reported of 1-dodecanol of up to 2 g/L(organic) and dodecanoic acid up to 19.7 g/L(organic) in a 2 L stirred tank reactor with 1L aqueous phase and 200 mL of n-dodecane as a second phase. The maximum volumetric rate of combined alcohol and acid production achieved was 1.9 g/L(organic)/h (0.35 g/L(total)/h). The maximum specific activity of combined alcohol and acid production was 7-fold lower on n-dodecane (3.5 μmol/min/g(dcw)) than on n-octane (21 μmol/min/g(dcw)); similar to the 5-fold difference observed between wild-type growth rates using the two respective alkanes as sole carbon source. Despite this, both total volumetric rate and final yield exceeded n-octane oxidation by 3.5-fold under the same conditions, due to the lower toxicity of n-dodecane and its oxidation products to E. coli compared to the 8-carbon equivalents. Substrate access limitations and the overoxidation of 1-dodecanol to dodecanoic acid were identified as the most important limitations to be addressed.     

Unstable steady state operations of substrate inhibited cultures by dissolved oxygen control

Microorganism kinetic growth characterized by substrate inhibition was investigated by means of a continuous stirred tank reactor equipped with a feedback controller of the medium feeding flow rate. The aerobic growth of Pseudomonas sp. OX1 with phenol as carbon/energy source was adopted as a case study to test a new control strategy using dissolved oxygen concentration as a state variable. The controller was successful in steadily operating bioconversion under intrinsically unstable conditions. A simple model of the controlled system was proposed to set the feedback controller. The specific growth rate of Pseudomonas sp. OX1 was successfully described by means of the Haldane model. The regression of the experimental data yielded μ(M)=0.26 h(-1), K(Ph)=5×10(-3)g/L and K(I)=0.2g/L. The biomass-to-substrate fractional yield as a function of the specific growth rate did not change moving from substrate-inhibited to substrate-deficient state. The data was modelled according to the Pirt model: m=1.7×10(-2)g/(gh), Y(X/Ph)(Th)=1.3g/g. The specific growth rates calculated for batch and continuous growth were compared.     

添加TCA循环中间产物加速光滑球拟酵母积累丙酮酸

在维生素限制的条件下,研究了添加TCA循环中间产物对光滑球拟酵母多重维生素营养缺陷型菌株CCTCC M202019生长和积累丙酮酸的影响。该菌株能以TCA循环中间产物为唯一碳源进行生长,且在以葡萄糖、乙酸和TCA循环中间产物为复合碳源的平板上菌落数高于分别以葡萄糖和乙酸或TCA循环中间产物为唯一碳源时的菌落数。与其它TCA循环中间产物相比,草酰乙酸更能促进细胞的生长、提高丙酮酸产量和对葡萄糖的得率。草酰乙酸能够促进细胞生长,是因为T. glabrata CCTCC M202019菌株能够利用乙酸作为乙酰辅酶A供体。在含有100 g/L葡萄糖和6 g/L乙酸钠的培养基中再添加10 g/L草酰乙酸进行分批发酵实验,可使菌体浓度从11.8 g/L提高到 13.6 g/L,增长幅度为15%;丙酮酸对葡萄糖的得率(0.66 g/g)以及生产强度(1.19 g·L^{-1<、sup>·h-1<、sup>)分别高出6%和24%,使发酵结束时间提前8～12h。}