利用发酵促进剂提高红酵母β-胡萝卜素产率

为提高红酵母生物合成β-胡萝卜素的产量,分别研究了几种添加物对发酵过程的促进效应。试验结果表明：分别添加硫胺素、核黄素、大豆油和番茄汁可以显著促进红酵母合成β-胡萝卜素。当按单因素试验确定的最优添加量联合添加硫胺素1.5mg/L、核黄素3mg/L、大豆油5mg/L、番茄汁6mg/L时,试验证实β-胡萝卜素发酵产率可比对照提高80%以上,值得进一步研究。     

黄色短杆菌TK0303的L-亮氨酸生物合成途径分析

应用途径分析方法分析了在拟稳态时黄色短杆菌(Brevibacterium flavum)TK0303由葡萄糖发酵生产L-亮氨酸的代谢途径,确定了L-亮氨酸合成的最佳途径和最大理论产率。通过比较途径分析所获得的反应模型,确定了丙酮酸和乙酰辅酶A是L-亮氨酸合成途径的关键节点。在此基础上改变外界环境因子,强化L-亮氨酸生物合成途径中丙酮酸和乙酰辅酶A两个关键节点的代谢流,以期进一步提高L-亮氨酸产率。结果表明,经过谷氨酸以及醋酸铵的调节,代谢途径流量发生显著变化,L-亮氨酸产量有明显提高。     

用b-紫罗兰酮筛选虾青素高产菌株

用β-紫罗兰酮作为筛选剂选择性分离海洋红酵母虾青素高产突变菌株。实验结果表明, 在β-紫罗兰酮存在的情况下, 由于类胡萝卜素合成受到抑制, 海洋红酵母的生物量和虾青素合成量都减少; 当平板培养基中β-紫罗兰酮浓度达到370 mg/L时, 海洋红酵母的致死率为92.3%; 在这种平板培养基上涂布经甲基磺酸乙酯诱变的海洋红酵母, 随机筛选200个菌落, 结果表明生物量、虾青素体积产率和细胞产率均有所提高的正突变株占18%, 生物量、虾青素体积产率和细胞产率的单项指标有所提高的正突变株分别占22.5%、45%和46%。该实验结果表明在分离培养基中添加β-紫罗兰酮可选择性地分离海洋红酵母虾青素高产菌株, 提高虾青素高产突变株的筛选效率。     

用β-紫罗兰酮筛选虾青素高产菌株

用β-紫罗兰酮作为筛选剂选择性分离海洋红酵母虾青素高产突变菌株.实验结果表明,在β-紫罗兰酮存在的情况下,由于类胡萝卜素合成受到抑制,海洋红酵母的生物量和虾青素合成量都减少;当平板培养基中β-紫罗兰酮浓度达到370 mg/L时,海洋红酵母的致死率为92.3%:在这种平板培养基上涂布经甲基磺酸乙酯诱变的海洋红酵母,随机筛选200个菌落,结果表明生物量、虾青素体积产率和细胞产率均有所提高的正突变株占18%,生物量、虾青素体积产率和细胞产率的单项指标有所提高的正突变株分别占22.5%、45%和46%.该实验结果表明在分离培养基中添加β-紫罗兰酮可选择性地分离海洋红酵母虾青素高产菌株,提高虾青素高产突变株的筛选效率.     

铵离子对必特螺旋霉素组分生物合成的调控作用

通过考察铵离子浓度对必特螺旋霉素组分的影响,证实低浓度铵离子的培养条件可以有效提高必特螺旋霉素中异戊酰螺旋霉素Ⅲ的比例。在此基础上进一步测定了高铵(62·5mmol/L)和低铵(2·5mmol/L)培养条件下的糖、铵离子、相关有机酸、缬氨酸脱氢酶酶活等中间代谢数据,结果表明高浓度铵离子培养条件下,必特螺旋霉素产生菌中亮氨酸分解代谢途径的关键酶——缬氨酸脱氢酶的活性低于低铵对照试验,造成异戊酰螺旋霉素合成过程中酰基转移反应的底物——异戊酰CoA的相对不足,从而导致异戊酰螺旋霉素组分的降低。大幅度降低铵离子浓度至2·5mmol/L,使异戊酰螺旋霉素Ⅲ的比例从5·43%提高至28·59%。但氮源的不足影响了必特螺旋霉素的产量,低铵条件下的效价为107μg/mL,相对高铵条件下降了14·4%。在低铵培养条件的基础上添加亮氨酸,可以进一步改善必特螺旋霉素的组分,异戊酰螺旋霉素Ⅲ的比例增至37·84%。     

偶联基于酮还原酶的NADH再生系统一锅法酶催化合成L-2-氨基丁酸

以廉价易得的L-苏氨酸为原料,利用在大肠杆菌中重组表达的苏氨酸脱氨酶和亮氨酸脱氢酶,并偶联基于酮还原酶的NADH再生系统一锅法制备L-2-氨基丁酸。以L-2-氨基丁酸的产率为指标,考察了一锅法酶催化制备L-2-氨基丁酸的最适p H、L-苏氨酸浓度及异丙醇浓度。在最适p H 7.5~8.0,L-苏氨酸浓度50g/L,添加5%的异丙醇及0.5g/L NAD+,分别加入0.6g/L苏氨酸脱氨酶、2g/L亮氨酸脱氢酶及2g/L酮还原酶,反应20h,可实现L-2-氨基丁酸的摩尔产率为99%,产量为43g/L。该结果为L-2-氨基丁酸的制备提供了一种新的思路。     

一株高产脯氨酸的嗜醋酸棒杆菌的选育及发酵条件优化

以嗜醋酸棒杆菌为出发菌株,经过片段化全基因组体外诱变、重组和连续的磺胺胍抗性筛选,获得一株L-脯氨酸的高产菌株。摇瓶发酵优化结果表明,葡萄糖、生物素和硫胺素的最适用量分别为16%、300μg/L、400μg/L,最适pH为6.8~7.0,装液量为25ml/500ml摇瓶,发酵培养72h后L-脯氨酸产率高达到75.6g/L,与对照相比提高了5%。考察了50L发酵罐中细胞生长对L-脯氨酸产量的影响,补料分批发酵结果表明(比生长速率分别为0.06/h、0.08/h和0.1/h),比生长速率在0.08/h左右时L-脯氨酸的产率最高,L-脯氨酸的比生产速率Q_P达到0.091 g/(g.h),产率高达82.1 g/L,比优化前提高了14%。     

液态烷烃氧载体对粘红酵母发酵产番茄红素的影响

研究正己烷、正十二烷、正十六烷3种液态烷烃作为氧载体对粘红酵母生长和番茄红素合成的影响,发现氧载体不仅使菌体生物量提高,同时使单位细胞的番茄红素产率增大,从而提高粘红酵母合成番茄红素的能力。3种液态烷烃中正十二烷作为氧载体效果较好,试验结果表明,在发酵第0 h时添加4%的正十二烷,细胞生物量达到16.49 g/L,番茄红素合成量达到42.32 mg/L分别比对照组提高了26.2%和50.17%。     

Pgk和ilvN基因对谷氨酸棒杆菌产L-丝氨酸的影响

为增加谷氨酸棒杆菌A36的L-丝氨酸合成途径的碳流,首先过表达磷酸甘油酸激酶(pgk),以增加前体物质3-磷酸甘油酸的积累,但经发酵分析发现其对菌株A36的L-丝氨酸产量无显著影响。进一步敲除副产物L-缬氨酸合成途径的乙酰羟酸合酶(AHAS)基因ilvN,敲除该基因后L-缬氨酸只有微量积累,但重组菌并未形成营养缺陷型菌株,L-丝氨酸的产量反而下降,分析发现L-缬氨酸的存在在一定程度上有助于L-丝氨酸的生成。在培养基中分别添加不同质量浓度的L-缬氨酸,在L-缬氨酸添加量为750 mg/L时,重组菌L-丝氨酸产量达到34.19 g/L,糖酸转化率为0.34 g/g,生产强度为0.28 g/(L·h),相比出发菌株A36分别提高了11.8%、13.3%和12.0%。     

β-胡萝卜素对阿魏蘑菌体形态及其产漆酶的影响

前期研究发现β-胡萝卜素为阿魏蘑和胶红酵母共培养过程中提高漆酶活性的关键因子。本文研究β-胡萝卜素的最佳添加量、添加时间和消耗情况,以及胶红酵母和β-胡萝卜素对阿魏蘑的形态的影响。结果表明,在阿魏蘑单培养中β-胡萝卜素的最佳添加量为10 mg(0.067%),最优添加时间为48 h,漆酶酶活达到7 083 U/L,为单培养的2.9倍。在形态研究中发现中小型菌球和粗糙型菌球都有利于产漆酶。结果显示通过添加β-胡萝卜素和控制阿魏蘑的菌体形态均可提高漆酶的产量,为漆酶的工业化生产提供了新的尝试和方法。     

Carotene production from waste cooking oil by Blakeslea trispora in a bubble column reactor: The role of oxidative stress

The oxidative stress induced by hydroperoxides and reactive oxygen species (ROS) during carotene production from waste cooking oil (WCO) and corn steep liquor (CSL) by the fungus Blakeslea trispora in a bubble column reactor was investigated. The specific activities of the intracellular enzymes superoxide dismutase (SOD) and catalase (CAT) as well as the micromorphology of the fungus were measured in order to study the response of the fungus to oxidative stress. The changes of the morphology of microorganism leaded to pellets formation and documented using a computerized image analysis system. As a consequence of the mild oxidative stress induced by hydroperoxides of WCO and ROS a significant increase in carotene production was obtained. The highest carotene concentration (980.0 mg/l or 51.5 mg/g dry biomass) was achieved in a medium consisted of CSL (80.0 g/L) and WCO (50.0 g/L) at an aeration rate of 5 vvm after 6 days of fermentation. In this case the carotenes produced consisted of β‐carotene (71%), γ‐carotene (26%), and lycopene (3%). The strong oxidative stress in the fungus caused a significant increase of γ‐carotene concentration. Bubble column reactor is a useful fermentation system for carotene production in industrial scale.     

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。     

红豆杉细胞培养产物提取策略及其对紫杉醇的影响

研究了硫酸铈铵及原位提取对红豆杉细胞悬浮培养过程中细胞生长、紫杉醇合成及释放的影响。红豆杉细胞悬浮培养过程中培养第12d添加2mg/L硫酸铈铵能获得最大紫杉醇产量8．3mg/L,其中2．4mg/L释放到细胞外,分别为对照组的4倍及12倍。同时添加2mg/L硫酸铈铵、5％油酸(v/v)时胞外紫杉醇产量达到9mg/L,为对照组的45倍。将硫酸铈铵及原位提取与补料培养相结合,最高紫杉醇产量可达24．5mg/L,其中60％释放到胞外。     

Use of soybean oil and ammonium sulfate additions to optimize secondary metabolite production

A valine-overproducing mutant (MA7040, Streptomyces hygroscopicus) was found to produce 1.5 to 2.0 g/L of the immunoregulant, L-683,590, at the 0.6 m3 fermentation scale in a simple batch process using soybean oil and ammonium sulfate-based GYG5 medium. Levels of both lower (L-683,795) and higher (HH1 and HH2) undesirable homolog levels were controlled adequately. This batch process was utilized to produce broth economically at the 19 m3 fermentation scale. Material of acceptable purity was obtained without the multiple pure crystallizations previously required for an earlier culture, MA6678, requiring valine supplementation for impurity control. Investigations at the 0.6 m3 fermentation scale were conducted, varying agitation, pH, initial soybean oil/ammonium sulfate charges, and initial aeration rate to further improve growth and productivity. Mid-cycle ammonia levels and lipase activity appeared to have an important role. Using mid-cycle soybean oil additions, a titer of 2.3 g/L of L-683,590 was obtained, while titers reached 2.7 g/L using mid-cycle soybean oil and ammonium sulfate additions. Both higher and lower homolog levels remained acceptable during this fed-batch process. Optimal timing of mid-cycle oil and ammonium sulfate additions was considered a critical factor to further titer improvements.     

营养条件对兽疫链球菌发酵生产透明质酸的影响

透明质酸 (Ｈｙａｌｕｒｏｎｉｃａｃｉｄ ,简称ＨＡ)是Ｎ 乙酰氨基葡萄糖胺和葡萄糖醛酸以 β 1 3糖苷键和 β 1 4糖苷键连接而成的二糖单体重复构建而成的杂多糖 ,广泛存在于高等动物的结缔组织内。由于结构上的特点 ,ＨＡ具有很高的粘弹性和极强的保水性等特征 ,已被大量用于医学医药、化妆品工业[1,2 ] 。1937年Ｋｅｎｄａｌｌ[3 ] 等发现用溶血性链球菌 (Ｓｔｒｅｐｔｏｃｏｃｃｕｓｈａｅｍｏｌｙｔｉｃｕｓ)可以产生ＨＡ。其后 ,陆续发现许多能产生ＨＡ的微生物菌种 ,逐渐开发出一条可替代传统的动物组织提取法[4 ] 生产ＨＡ的新途径…     

氨茶碱与柠檬酸盐协同作用促进环磷酸腺苷发酵生产

目的: 探究通过抑制磷酸二酯酶活性促进cAMP发酵合成的工艺方法。方法: 在7 L发酵罐上进行添加氨茶碱的发酵实验,通过对发酵主要参数、关键酶活性、能量代谢水平等进行分析,针对性提出了氨茶碱与柠檬酸盐协同作用促进cAMP合成的发酵工艺。结果: 与对照相比,添加5 mg/L氨茶碱批次的cAMP产量提高25.9%,副产物腺苷浓度减少41.6%,两批次中腺苷酸环化酶和琥珀腺苷酸脱氢酶活性无显著改变,而磷酸二酯酶和5'-核苷酸酶活性明显下降。能量代谢分析结果表明,两批次的胞内ATP/AMP相比于对照批次明显降低,而AMP水平却显著上升,ATP合成水平成为限制产物积累的主要因素。氨茶碱与柠檬酸盐协同添加的cAMP发酵工艺中,cAMP产量达到4.48 g/L,比单独添加柠檬酸钠和氨茶碱分别提高22.1%和13.8%,副产物腺苷浓度仅为0.98 g/L,分别降低51.7%和25.3%。结论: 氨茶碱抑制了磷酸二酯酶和5'-核苷酸酶活性,减少cAMP分解和副产物合成,显著提高cAMP产量,然而ATP合成水平成为产物积累的限制因素。氨茶碱与柠檬酸盐协同添加工艺将抑制磷酸二酯酶活性和提高能量代谢水平相结合,进一步促进了产物发酵合成。     

Effect of nutritional factors on cellulase enzyme and microbial protein production by Aspergillus terreus and its evaluation

The biomass yield, cellulolytic activity, and protein recovery using Aspergillus terreus GN1 with alkali-treated sugarcane bagasse was studied using different levels (250-600 mg of N/L of broth) of organic and inorganic nitrogen sources. e.g., cattle urine, urea, cornsteep liquor, ammonium sulfate, ammonium nitrate, ammonium iron sulfate, ammonium chloride, and sodium nitrate. Among different levels of alkali-treated bagasse substrate concentrations (0.5-4.0% w/v) tested, 1.0% substrate yielded the highest crude protein content, protein recovery, and cellulolytic activity. The biomass recovery with 1.0% substrate ranged from 290-380 mg/500 mg bagasse substrate in a 50-mL broth with a nitrogen level of 250-600 mg of N/L in all the sources except ammonium iron sulfate, which yielded 402-439 mg/500 mg bagasse substrate. However, crude protein content of biomass obtained with an ammonium iron sulfate nitrogen source was the lowest. Cornsteep liquor nitrogen source at the rate of 600 mg of N/L yielded the maximum crude protein of 32.9%, protein recovery of 22.2 g/100 g of bagasse, and carboxymethyl cellulase and filter paper enzyme activities of 1.1 and 0.09 units/mL, among the organic and inorganic nitrogen sources studied. In general, the organic nitrogen sources and inorganic nonammonium nitrogen sources were utilized preferentially for protein production over the inorganic ammonium nitrogen sources. The fermentation time required under optimum cultural and nutritional conditions for A. terreus GN1 was also evaluated. The crude protein content of the biomass increased gradually up to the seventh day of fermentation, but the protein recovery rate was high up to two or three days. It was observed that the cellulose utilization rate increased after an initial lag of one day up to the third day and gradually increased further, which corresponded positively with protein content, biomass protein recovery, and cellulase enzyme activity. On the seventh day of fermentation, the crude protein content, biomass protein recovery, water-soluble carbohydrate, bagasse cellulose utilization, CMCase, and FPase activities were 32.8%, 20.1 g/100 g of bagasse, 6.2%, 82.7%, 1.0. and 0.08 U/mL, respectively. The final biomass recovered contained 32.8% crude protein content and had an in vitro rumen digestibility (IVRD) coefficient of 68.8%. The biomass contained almost all the essential and nonessential amino acids and was comparable with FAO reference protein. It is concluded that a fermentation time of 72 h gave a faster rate of protein production of 16.9 g/100 g of bagasse with 69.8% bagasse cellulose utilization with 76.0% IVRD. and contained almost all the essential and nonessential amino acids.     

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。