膜反应器固定化米根霉发酵产富马酸的工艺研究

以膜反应器固定化米根霉发酵产富马酸为研究对象,以Na2CO3为中和剂,考察固定化米根霉在5L搅拌式发酵罐中的发酵特征,采用智能可视化软件(IVOS)优化发酵工艺条件。结果表明,在80g/L初始糖浓及最优工艺下,富马酸产量、生产速率及转化率分别为21.1g/L、0.25g/(L·h)和28%;采用40g/L初始糖浓及连续批次发酵工艺时,富马酸产量、生产速率及转化率最高分别为10.8 g/L、0.36g/(L·h)和27%。搅拌式反应器中,固定化米根霉的膜反应器比表面积有限,以及菌膜的空间阻隔效应对传质传氧的限制作用,显著影响了富马酸的生产强度和转化率。因此,亟需发掘新的固定化方法及反应器形式,达到既解决米根霉形态控制问题,又有助于生产性状提升的目标。     

基于智能可视化优化上的米根霉发酵生产富马酸过程的优化

为提高米根霉发酵产富马酸的效率,对米根霉发酵过程进行了优化。通过单因素实验考察不同氮源对富马酸合成的影响,确定了米根霉ME-F14发酵产富马酸的最佳氮源为(NH4)2SO4;在此基础上采用均匀实验设计法进行试验设计,并利用智能可视化优化软件对发酵培养基的组分和培养条件进行优化。当接种龄为12 h、葡萄糖87.5 g/L、(NH4)2SO40.55 g/L、接种量27.5%时,富马酸产量达43.8 g/L,比对照组提高了31.81%。此结果可以为发酵法制备富马酸的工业化生产奠定基础。     

L-Gln高产突变菌株发酵条件的初步优化

将诱变实验筛选出的遗传稳定性高产突变株C.glutamicum N-U-6作为研究对象,采用单次单因子非统计优化技术确定了它在培养温度为30℃下250 mL的摇瓶培养条件为:150 g.L-1葡萄糖,最佳无机氮源及其浓度为:40 g.L-1NH4Cl;最佳有机氮源及其浓度:14 g.L-1尿素;玉米浆浓度:10 g.L-1,初始pH为7.2,装液量为30 mL,种龄为12 h,接种量为10%。谷氨酰胺产量达到37.21 g.L-1,比优化前的突变株(33.54 g.L-1)提高10.9%。     

米根霉在氮源限制下的木糖代谢和关键酶特性北大核心CSCD

【目的】解析氮源浓度对米根霉木糖代谢途径及产物的影响,提高木糖利用率。【方法】以木糖为碳源,考察不同氮源浓度下米根霉的生物量、有机酸积累量、木糖代谢关键酶(木糖还原酶、葡萄糖-6-磷酸脱氢酶)活力以及胞内还原力(NADH/NAD+、NADPH/NADP+)的差异。【结果】富氮条件下(2.4 g/L尿素),木糖代谢速率达2.03 g/(L·h),木糖还原酶、葡萄糖-6-磷酸脱氢酶的活力以及胞内还原力较高,生物量达18.01g/L,几乎不积累有机酸;限氮条件下(0.15 g/L尿素),木糖还原酶、葡萄糖-6-磷酸脱氢酶的活力以及胞内还原力水平降低,生物量仅4.02 g/L,富马酸积累量为6.55 g/L,残余木糖量较高;氮源浓度为0.6 g/L时,木糖还原酶和葡萄糖-6-磷酸脱氢酶的活力以及NADPH/NADP+处于前二者之间,此时生物量9.11 g/L,有机酸积累量较大,其中富马酸为12.28 g/L。【结论】充足的氮源可使米根霉通过木糖代谢关键酶与胞内还原力的协同效应强化木糖代谢活力,通过优化氮源浓度后,米根霉可积累更多有机酸。     

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%。     

水产动物益生菌乳酸杆菌LH发酵工艺的研究

目的从生产实际出发,对1株高效乳酸杆菌（Lactobacillus spp）LH进行液体发酵培养基优化及发酵条件研究。方法通过碳源、氮源、无机盐、促生长素等单因子筛选及正交试验设计获得以下最佳培养基：糖蜜12 g/L,酵母膏5 g/L,蛋白胨1 g/L,葡萄糖4 g/L,玉米浆3 g/L,乙酸钠5 g/L,NaC l 5 g/L,K2HPO42.5 g/L,KH2PO42.5 g/L,MgSO40.5g/L,MnSO40.25 g/L。在此培养基上研究了该菌株最佳发酵条件。结果培养基初始pH 6.0,接种量2%（v/v,相对装液量）,500 m l三角瓶中装液量为500 m l,发酵温度为30～35℃,静置培养。在最佳培养条件下,LH活菌量达到1.74×10^9CFU/m l。结论通过活菌平板计数法测定了乳酸杆菌LH生长曲线,24 h为最佳种龄,生产收获时间是36 h。     

耐底物腈水合酶融合子的产酶条件优化

采用正交设计法对耐底物腈水合酶融合子的发酵条件进行优化,以发酵液起始pH,发酵周期,接种量,装料系数作为考察因素,最终确定最佳发酵条件为:起始pH8.0、发酵周期54h、接种量12％、装液系数12％.在此优化条件下融合子腈水合酶的活力达到1100万U/ml,较优化前提高了83.3％.通过响应面法对发酵培养基配方进行优化研究,采用Plackett-Burman法对8个因素进行了筛选,结果表明,葡萄糖、尿素、磷酸氢二钾、磷酸二氢钾是影响发酵液腈水合酶产量的主效应因子.用最陡爬坡试验及Central composite design设计进一步优化,利用Design-Expert软件进行二次回归分析,得到各因素的最佳浓度为:葡萄糖22.62g/L、尿素9.76g/L、K2HP04 1.22g/L、KH2PO41.268g/L.在此培养基优化配方下融合子腈水合酶的活力达到1280万U/ml,较原配方的酶活提高了16.4％.     

循环利用重组大肠杆菌细胞转化合成丁二酸

研究了回收丁二酸发酵液中的大肠杆菌进行细胞转化的可行性,以转化率和生产效率为指标,考察了不同菌体浓度、底物浓度、pH调节剂对细胞转化的影响。发酵结果表明大肠杆菌可以在仅含有葡萄糖和pH调节剂的水环境中转化生产丁二酸,并确定了最佳的转化条件为:细胞浓度(OD600)50,底物浓度40g/L,缓冲盐为MgCO3。基于优化好的条件,在7L发酵罐中进行重复批次转化,第1次转化的转化率和生产效率分别达到91%和3.22g/(L·h),第2次转化的生产效率和转化率达到了86%和2.04g/(L·h),第3次转化的转化率和生产效率分别达到了83%和1.82g/(L·h)。     

出芽短梗霉产聚苹果酸发酵条件的优化

【背景】出芽短梗霉可发酵葡萄糖生成聚苹果酸,但存在转化率和转化效率低等瓶颈,阻碍其实现商业化生产。【目的】通过优化发酵培养条件,提高出芽短梗霉的聚苹果酸产量、糖酸转化率和生产强度。【方法】采用单因素试验优化适宜出芽短梗霉BK-10菌株产生聚苹果酸的培养条件,通过Plackett-Burman法对培养基组分筛选显著性影响因素,并对其培养基中无机盐进行正交试验优化,最后进行5 L发酵罐验证。【结果】最优培养基配方和培养条件:100 g/L葡萄糖,1.5 g/L尿素,0.20 g/L KH_2PO_4,0.20 g/L ZnSO_4,0.05 g/L MgSO_4,0.75 g/L KCl,30 g/L CaCO_3,0.01%吐温-80,发酵温度26°C,250 mL摇瓶装液量50 mL。【结论】通过优化,聚苹果酸的糖酸转化率达到0.71 g/g,生产强度达到0.89 g/(L·h),较优化前分别提高了18.33%和71.15%,为发酵葡萄糖合成聚苹果酸进而生产L-苹果酸工艺的工业化生产奠定经济性基础。     

产琥珀酸重组大肠杆菌的发酵性能研究

研究了重组大肠杆菌JM001(△ppc)/pTrc99a-pck发酵产琥珀酸的性能,结果表明厌氧条件下其耗糖能力和产酸能力分别为对照菌株JM001的4.2倍和15.3倍。进一步优化发酵条件表明：采用接入菌泥的发酵方式比按照10%接种量转接厌氧发酵的效果要好,琥珀酸的对葡萄糖的质量收率提高了约10%,且副产物乙酸的量进一步降低。初始葡萄糖浓度高于60g/L时会对菌株的生长和产酸产生抑制,且浓度越高,抑制作用越明显。7L发酵罐放大实验中,整个厌氧发酵阶段葡萄糖的消耗速率为0.42g/(L.h),琥珀酸对葡萄糖的质量收率为67.75%,琥珀酸的生产强度为0.28g/(L.h)。     

Fumaric Acid Production by <Emphasis Type="Italic">Rhizopus oryzae</Emphasis> ATCC® 20344™ from Lignocellulosic Syrup

Powdered activated carbon-treated lignocellulosic syrup prepared from energy cane bagasse was evaluated as a potential feedstock in the production of fumaric acid by Rhizopus oryzae ATCC® 20344?. Energy cane bagasse was pretreated with dilute ammonia and enzymatically hydrolyzed with commercially available enzymes, Cellic® CTec2 and HTec2. The collected hydrolysate samples were subjected to powdered activated carbon adsorption for the removal of non-sugar compounds (i.e., organic acids, furaldehydes, total phenolic compounds) and concentrated to a final 65°Bx syrup (mostly xylose and glucose sugars). The use of lignocellulosic syrup, the effect of nitrogen source, medium additives, and initial pH in the seed culture medium on fungal morphology were investigated. The carbon to nitrogen (C/N) ratio in the acid production medium was also optimized for maximum yields in fumaric acid production. Optimum seed culture medium conditions (2.0 g/L urea, 3.0 pH) produced the desired compact, smooth, and uniform fungal pellets. Optimum acid production medium conditions (400 C/N ratio, 0.2 g/L urea) resulted in a fumaric acid production of 34.20 g/L, with a yield of 0.43 g/g and a productivity of 0.24 g/L/h. These results were comparable to those observed with the control medium (pure glucose and xylose). The present study demonstrated that lignocellulosic syrup processed from dilute ammonia pretreated energy cane bagasse has potential as a renewable carbon source for fumaric acid fermentation by Rhizopus oryzae ATCC® 20344?.     

Simultaneous Production and Recovery of Fumaric Acid from Immobilized Rhizopus oryzae with a Rotary Biofilm Contactor and an Adsorption Column

An integrated system of simultaneous fermentation-adsorption for the production and recovery of fumaric acid from glucose by Rhizopus oryzae was investigated. The system was constructed such that growing Rhizopus mycelia were self-immobilized on the plastic discs of a rotary biofilm contactor during the nitrogen-rich growth phase. During the nongrowth, production phase, the biofilm was alternately exposed to liquid medium and air upon rotation of the discs in the horizontal fermentation vessel. The product of fermentation, fumaric acid, was removed simultaneously and continuously by a coupled adsorption column, thereby moderating inhibition, enhancing the fermentation rate, and sustaining cell viability. Another beneficial effect of the removal of fumaric acid is release of hydroxyl ions from a polyvinyl pyridine adsorbent into the circulating fermentation broth. This moderates the decrease in pH that would otherwise occur. Polyvinyl pyridine and IRA-900 gave the highest loading for this type of fermentation. This fermentation system is capable of producing fumaric acid with an average yield of 85 g/liter from 100 g of glucose per liter within 20 h under repetitive fed-batch cycles. On a weight yield basis, 91% of the theoretical maximum was obtained with a productivity of 4.25 g/liter/h. This is in contrast to stirred-tank fermentation supplemented with calcium carbonate, whose average weight yield was 65% after 72 h with a productivity of 0.9 g/liter/h. The immobilized reactor was operated repetitively for 2 weeks without loss of biological activity.     

Continuous citric acid fermentation by <Emphasis Type="Italic">Candida oleophila</Emphasis> under nitrogen limitation at constant C/N ratio

Summary The central aspect of this work was to investigate the influence of nitrogen feed rate at constant C/N ratio on continuous citric acid fermentation by Candida oleophila ATCC 20177. Medium ammonia nitrogen and glucose concentrations influenced growth and production. Space-time yield (STY) meaning volumetric productivity, biomass specific productivity (BSP), product concentration, product selectivity and citrate/isocitrate ratio increased with increasing residence time (RT). BSP increased in an exponential mode lowering nitrogen feed rates. Highest BSP for citric acid of 0.13 g/(g h) was achieved at lowest NH₄Cl concentration of 1.5 g/l and highest STY (1.2 g/l h) with 3 g NH₄Cl/l at a RT of 25 h. Citric acid 74.2 g/l were produced at 58 h RT and 6 g NH₄Cl/l. Glucose uptake rate seems to be strictly controlled by growth rate of the yeast cells. Optimum nitrogen concentration and adapted C/N ratio are essential for successful continuous citric acid fermentation. The biomass-specific nitrogen feed rate is the most important factor influencing continuous citric acid production by yeasts. Numerous chemostat experiments showed the feasibility of continuous citrate production by yeasts.     

L-谷氨酸补料分批发酵的研究

对谷氨酸棒杆菌(Corynebacteriuin glutamicum)HCJ46产L-谷氨酸的补料分批发酵条件进行研究.结果表明:最适初糖质量浓度和最佳残糖维持质量浓度分别为100和(10～20)g/L;对发酵控温方式进行研究,确定了最佳温度控制策略为0～8h维持32℃,8～16h维持34℃、16～32h维持36℃,同时发现相对溶氧控制在30%左右时产酸最高.在以上的优化条件下,L-谷氨酸产量从72g/L提高到95g/L,提高了31.9%.     

大肠杆菌AFP111菌体回收连续转化生产丁二酸

在利用大肠杆菌AFP111厌氧发酵生产丁二酸过程中,随着产物丁二酸的不断积累,菌体活力和产酸能力逐渐降低,而通过回收菌体在新鲜培养基中重复发酵,可延长厌氧发酵时间,但是丁二酸生产效率较低。为了提高菌体回收丁二酸的转化效率,通过在回收菌体时有氧诱导 3 h,以纯水为培养基,进行丁二酸转化发酵。在连续进行 3 批次的发酵后,丁二酸的总产量和最终收率分别为 56.50 g/L和90%,生产速率达到了 0.81 g/(L·h),比未诱导情况下的生产速率提高了13%。     

Ethanol fermentation of acid-hydrolyzed cellulosic pyrolysate with Saccharomyces cerevisiae

The acid hydrolysis of cellulosic pyrolysate to glucose and its fermentation to ethanol were investigated. The maximum glucose yield (17.4%) was obtained by the hydrolysis with 0.2 mol sulfuric acid per liter pyrolysate using autoclaving at 121 degrees C for 20 min. The fermentation by Saccharomyces cerevisiae of a hydrolysate medium containing 31.6 g/l glucose gave 14.2 g/l ethanol in 24 h, whereas the fermentation of the medium containing 31.6 g/l pure glucose gave 13.7 g/l ethanol in 18 h. The results showed that the acid-hydrolyzed pyrolysate could be used for ethanol production. Different nitrogen sources were evaluated and the best ethanol concentration (15.1 g/l) was achieved by single urea. S. cerevisiae (R) was obtained by adaptation of S. cerevisiae to the hydrolysate medium for 12 times, and 40.2 g/l ethanol was produced by S. cerevisiae (R) in the fermentation with the hydrolysate medium containing 95.8 g/l glucose, which was about 47% increase in ethanol production compared to its parent strain.     

Production of lactic acid by Lactobacillus rhamnosus with vitamin-supplemented soybean hydrolysate

Batch fermentation studies were performed to evaluate the potentials of a complex nitrogen source, soybean, as an alternative to yeast extract for the economical production of lactic acid by Lactobacillus rhamnosus. An enzyme-hydrolysate of soybean meal, Soytone, with an adequate supplementation of vitamins was found to be highly effective in supporting lactic acid production from glucose and lactose. The effects of seven selected vitamins: d-biotin, pyridoxine, p-aminobenzoic acid, nicotinic acid, thiamine, pantothenic acid, and riboflavin, on cell growth and lactic acid production were investigated to provide the basis for the optimization of vitamin supplementation to minimize the cost. Pantothenic acid was the most required compound while the other six vitamins were also essential for high lactic acid productivity. As a result of the optimization, 15 g/l yeast extract could be successfully replaced with 19.3 g/l Soytone supplemented with the vitamins, resulting in a production of 125 g/l lactic acid from 150 g/l glucose. The volumetric productivity and lactate yield were 2.27 g/l/h and 92%, respectively, which were higher than those with 15 g/l yeast extract. The raw material cost was estimated to be 21.4 cent/kg lactic acid, which was only approximately 41% of that with yeast extract.     

Screening and characteristics of a butanol-tolerant strain and butanol production from enzymatic hydrolysate of NaOH-pretreated corn stover

As a gasoline substitute, butanol has advantages over traditional fuel ethanol in terms of energy density and hydroscopicity. However, solvent production appeared limited by butanol toxicity. The strain of Clostridium acetobutylicum was subjected to mutation by mutagen of N-methyl-N'-nitro-N-nitrosoguanidine for 0.5?h. Screening of mutants was done according to the individual resistance to butanol. A selected butanol-resistant mutant, strain 206, produced 50?% higher solvent concentrations than the wild-type strain when 60?g glucose/l was employed as substrate. The strain was also able to produce solvents of 23.47?g/l in 80?g/l glucose P2 medium after 70?h fermentation, including 5.41?g acetone/l, 15.05?g butanol/l and 3.02?g ethanol/l, resulting in an ABE yield and productivity of 0.32?g/g and 0.34?g/(l?h). Subsequently, Acetone-butanol-ethanol (ABE) production from enzymatic hydrolysate of NaOH-pretreated corn stover was investigated in this study. An ABE yield of 0.41 and a productivity of 0.21?g/(l?h) was obtained, compared to the yield of 0.33 and the productivity of 0.20?g/(l?h) in the control medium containing 52.47 mixed sugars. However, it is important to note that although strain 206 was able to utilize all the glucose rapidly in the hydrolysate, only 32.9?% xylose in the hydrolysate was used after fermentation stopped compared to 91.4?% xylose in the control medium. Strain 206 was shown to be a robust strain for ABE production from lignocellulosic materials and has a great potential for industrial application.