米根霉发酵产富马酸的最适替代中和剂及pH调控策略研究

针对米根霉发酵产富马酸使用的不同中和剂(CaCO3,Na2CO3,NH3·H2O,NaOH)进行了研究,结果表明发酵过程中使用Na2CO3作为中和剂时富马酸产率和生产强度最接近传统中和剂CaCO3.此后考察了不同pH值(3.5,4.5,5.5和6.5)对Na2CO3作为中和剂的富马酸发酵过程的影响.基于对3个动力学参数的分析,提出了一个旨在同时获得富马酸高产物浓度、高产率和高生产强度的双阶段pH调控策略,在初始的24 h内pH控制在5.5,然后将pH调到4.5直至发酵结束.最终富马酸的终浓度达到40.5 g/L,产率为0.55 g/g,生产强度为0.61 g/L/h,比恒定pH时的最优结果分别提高了8.3％,10.0％和17.3％,其中生产强度甚至比使用CaCO3时还高了3.4％.故以Na2CO3作为中和剂,采用双阶段pH调控策略具有降低能耗和简化下游步骤的优势,可以成功取代CaCO3.     

氨水中和Lactobacillus delbrueckii subsp.lactis BME5-18M发酵生成L-乳酸铵的研究

实验确定了Lactobacillus delbrueckiisubsp.lactis BME5-18M接种的最佳种龄为24h.以氨水取代传统的中和剂碳酸钙中和发酵生成的乳酸、调控发酵液的pH,考察了不同pH值对菌体生长和产酸的影响,确定了菌种生长和产酸的较适pH值为6.5.考察了底物流加速度对菌种生长和产酸的影响,对间歇和流加发酵时菌体的生长量和产酸量进行了动力学关联.在较适pH值6.5和较佳流加速度25mL/h条件下,乳酸的产量可达到136.8g/L,产率为1.71 g/(L·h).     

氨水中和Lactobacillus delbrueckiisubsp. lactis BME5-18M发酵生成L-乳酸铵的研究*

实验确定了Lactobacillusdelbrueckiisubsp lactisBME5-18M接种的最佳种龄为24h。以氨水取代传统的中和剂碳酸钙中和发酵生成的乳酸、调控发酵液的pH ,考察了不同pH值对菌体生长和产酸的影响 ,确定了菌种生长和产酸的较适pH值为 6.5。考察了底物流加速度对菌种生长和产酸的影响 ,对间歇和流加发酵时菌体的生长量和产酸量进行了动力学关联。在较适pH值 6.5和较佳流加速度 25mL/h条件下 ,乳酸的产量可达到 136.8g/L ,产率为1.     

氨水中和Lactobacillus delbrueckii subsp．1actis BME5-18M发酵生成L-乳酸铵的研究

实验确定了Lacobacillus delbrueckii subsp．lactis BME5-18M接种的最佳种龄为24h。以氨水取代传统的中和剂碳酸钙中和发酵生成的乳酸、调控发酵液的pH,考察了不同pH值对菌体生长和产酸的影响,确定了菌种生长和产酸的较适pH值为6．5。考察了底物流加速度对菌种生长和产酸的影响,对间歇和流加发酵时菌体的生长量和产酸量进行了动力学关联。在较适pH值6．5和较佳流加速度25mL／h条件下,乳酸的产量可达到136．8g／L,产率为1．71g/(L．h)。     

Effects of different pH regulators on 1,3-propanediol production by Klebsiella pneumoniae in fed-batch culture

对肺炎克雷伯氏菌(Klebsiella pneumoniae)发酵生产1,3-丙二醇(1,3-Propanediol,1,3-PD)的补碱策略进行了研究.分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱.当采用混合碱调控发酵pH值为7.0时,1,3-丙二醇的产量达到了55 g/L,比无pH调控(对照)发酵过程发酵水平提高了10.6倍.     

芽孢乳杆菌发酵葡萄糖制备D(-)-乳酸的研究

在国内首次报道了发酵法制备D(-)-乳酸,采用芽孢乳杆菌(Sporolactobacillus sp．)从葡萄糖发酵制备D-乳酸。该发酵为微需氧,发酵培养基组成(g/L):葡萄糖60,酵母膏6,玉米浆5,NH4NO3l,麸皮2,NaH2PO4 4,CaCO340。发酵液的初始pH为7．0.在最佳条件下,37℃发酵72h可产40．7g/L的D-乳酸,葡萄糖转化率67．83％。通过离子配位色谱分析,产物的D-乳酸光学纯度为96．04％e．e．。     

耐氨米根霉发酵生产L-乳酸的研究

传统的L-乳酸发酵法生产以CaCO3为酸中和剂,在乳酸后提取中产生的大量石膏废渣不仅在过滤时造成较大的乳酸损失,而且由于废渣不易处理,对L-乳酸万吨级规模的生产将形成巨大的环保压力和废渣处理成本。为此,为了降低L-乳酸生产成本,该文采用氨水为酸中和剂,用筛选得到的一株米根霉RhizopusoryzaeJS-N02-02进行以氨水为中和剂的L-乳酸摇瓶、15L自动发酵罐的发酵试验。以玉米粉双酶水解糖为碳源,接种孢子浓度1×105个ml,以0.01%(NH4)2SO4为氮源,30℃,15L自动发酵罐连续5批发酵,平均总糖浓度为136.8gL,平均产酸达100.6gL,L-乳酸纯度达95.3%,糖酸转化率达71.6%。     

酸奶菌群发酵糖蜜产复合有机酸化剂的研究

【背景】开发安全、有效、稳定、适口性好、对环境无危害的无抗饲料添加剂是我国畜牧业的重中之重,酸化剂作为功能性饲料添加剂在众多替抗产品中有较大的优势。【目的】通过酸奶菌群发酵甜菜糖蜜制备低成本乳酸型复合液态酸化剂。【方法】以11种不同的新疆农牧民传统发酵酸奶菌群为出发菌,经MRS培养基富集乳酸菌群,选择产酸量高的菌群进行甜菜糖蜜发酵试验,并对菌群发酵时间、发酵条件、糖蜜浓度、氮源及中和剂进行优化。【结果】在糖蜜浓度为100 g/L、培养基未灭菌且37℃静置发酵48 h时,B2菌群发酵乳酸产量为34.52 g/L,总酸为83.42 g/L,加入中和剂Na₂CO₃后其乳酸产量达73.42 g/L,总酸达到169.37 g/L;B5菌群发酵乳酸产量可达61.12 g/L,总酸可达112.50 g/L,加入中和剂Ca（OH）₂后其乳酸产量达74.37 g/L,总酸为137.26 g/L。B2菌群发酵原液对沙门氏菌、金黄色葡萄球菌及产气荚膜杆菌均有较强的抑制作用;B5菌群发酵原液则对产气荚膜杆菌、沙门氏菌、金黄色葡萄球菌、大肠杆菌O...     

过表达氨基葡萄糖脱氨酶对大肠杆菌氨基葡萄糖合成及中心碳代谢的影响

考察过表达氨基葡萄糖脱氨酶对氨基葡萄糖合成及大肠杆菌（Escherichia coli）中心碳代谢的影响。实验结果表明：过表达氨基葡萄糖脱氨酶使得在36 g/L葡萄糖,pH为9.0的发酵条件下,发酵24 h后,重组菌发酵液中氨基葡萄糖、丙酮酸和乙酸的量分别是对照菌Rosetta的2.1、1.48和1.74倍;而乳酸的量为2.53 g/L,对照菌Rosetta发酵液中的乳酸含量未检测到,重组菌发酵液中柠檬酸及α-酮戊二酸的含量分别是Rosetta的2.99和2.73倍。     

乳杆菌Lactobacillus sp.lxp发酵高产L-乳酸研究

筛选得到一株乳杆菌Laetobaeillus sp．,进行发酵生产高浓度L-乳酸的研究。考察了种龄、接种量、温度和不同pH调节剂对乳酸发酵的影响。结果表明：最佳种子培养时间为15h;最佳接种量为15％;最适培养温度为42℃;与氨水和氢氧化钠相比,碳酸钙更适于作为发酵过程的pH调节刺;以葡萄糖为碳源,添加豆粕水解液和玉米浆作为辅料,2L罐培养120h,L-乳酸质量浓度可达202 g/L,糖转化率91．3％,L-乳酸占发酵液中总酸含量98％以上。     

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)。     

Improvement of lactic acid production from cellulose with the addition of Zn/Ni/C under alkaline hydrothermal conditions

The effect of Zn, Ni and activated carbon on the yield of lactic acid from cellulose was investigated to improve the lactic acid yield under alkaline hydrothermal conditions. The results showed that the lactic acid yield increased greatly in the presence of Zn, Ni and activated carbon. Central composite response surface method (RSM) design experimentation was used to find the optimal concentrations of Zn, Ni, activated carbon and NaOH, which indicated that 0.02 g Zn, 0.03 g Ni, 0.07 g activated carbon and 2.5 mol/L NaOH were the optimal concentrations. Under this condition, the highest lactic acid yield was 42%, which was much higher than previous results using only NaOH (15%). The confirmatory experiments on lactic acid yield proved that the proposed model of lactic acid yield can accurately predict the lactic acid yield from cellulose.     

Co-culturing of Lactobacillus paracasei subsp. paracasei with a Lactobacillus delbrueckii subsp. delbrueckii Mutant to Make High Cell Density for Increased Lactate Productivity from Cassava Bagasse Hydrolysate

To increase the productivity of lactic acid, a co-culture of lactobacilli was made by mixing 1:1 ratio of Lactobacillus paracasei subsp. paracasei and a fast growing L. delbrueckii subsp. delbrueckii mutant. The culture was embedded on to polyurethane foam (PUF) cubes as a biofilm and used for fermentation. In order to prevent the cell leakage, the PUF cubes were further entrapped in calcium cross-linked alginate. The maximum lactic acid production using a high cell density free culture was >38 g l(-1) from ~40 g l(-1) of reducing sugar within 12 h of fermentation. Using PUF biofilms, the same yield of lactic acid attained after 24 h. When the cubes were further coated with alginate it took 36 h for the maximum yield. Even though, the productivity is slightly lesser with the alginate coating, cell leakage was decreased and cubes were reused without much decrease in production in repeated batches. Using a conventional control inoculum (3%, w/v), it took 120 h to yield same amount of lactic acid.     

Genome shuffling of Lactobacillus delbrueckii mutant and Bacillus amyloliquefaciens through protoplasmic fusion for L-lactic acid production from starchy wastes

Current study was focused on the development of a non-fastidious lactic acid producing strain having better growth rate, low pH tolerance and good productivity by genome shuffling of a mutant strain of Lactobacillus delbrueckii NCIM 2025 and an amylase producing non-fastidious Bacillus amyloliquefaciens ATCC 23842. After the third cycle of the protoplast fusion, lactic acid production by few fusants was monitored and the best fusant was selected for further studies. Optimization of the important process parameters for lactic acid production was conducted using Plackett-Burman design and response surface methodology. Selected fusant could utilize the liquefied cassava bagasse starch directly with minimum nutrient supplementation for lactic acid production. During validation, 40g/L of lactic acid was obtained ( approximately 96% conversion of starch to lactic acid) by using fusant inoculum (3%, v/v) from 83g/L cassava bagasse (starch content 50% w/w) supplemented with yeast extract and peptone (0.2% each, w/v) and the buffering agent (2% CaCO(3), w/v).     

An economic approach for L-(+) lactic acid fermentation by Lactobacillus amylophilus GV6 using inexpensive carbon and nitrogen sources

AIMS: Development of cost-effective production medium by applying statistical designs for single-step fermentation of starch (corn flour - CF) to L-(+) lactic acid, using inexpensive nitrogen sources as substitutes for peptone and yeast extract in MRS medium by amylolytic Lactobacillus amylophilus GV6. METHODS AND RESULTS: A two-level Plackett-Burman design was employed for screening various available crude starches (flours) for L-(+) lactic acid production by Lact. amylophilus GV6 using red lentil flour (RL) and bakers yeast cells (YC) as substitutes for commercial peptone and yeast extract in MRS medium in anaerobic submerged fermentation. Of all the tested flours, CF was found to be the most significant. Central composite rotatable design was employed to determine maximum production of L-(+) lactic acid at optimum values of process variables, CF, RL, YC, CaCO(3) and incubation period (IP). minitab analyses showed that lactic acid production was significantly affected by the linear terms CF, RL, CaCO(3) and IP. The interactions of CF-RL, CF-YC, CF-CaCO(3), RL-YC and RL-CaCO(3) and the square terms CF and IP were significant. The maximum lactic acid production of 29 g/37 g of starch present in 50 g of CF was obtained at optimized concentrations of CF 5%, RL 0.7%, YC 0.8%, CaCO(3) 0.8% and IP 2.9 days. CONCLUSIONS: Successful application of Plackett-Burman design helped in identifying CF as the best carbon source among the tested flours for L-(+) lactic acid production using inexpensive nitrogen sources. Further optimization of the process variables by response surface methods (RSMs) led to maximum production of lactic acid (29 g lactic acid from 37 g of starch present in 50 g of flour). SIGNIFICANCE AND IMPACT OF THE STUDY: Lactobacillus amylophilus GV6 showed 78.4% lactic acid production efficiency (g lactic acid produced/g starch taken) and 96% lactic acid yield efficiency (g lactic acid produced/g starch utilized). Information from the present studies provides a better understanding on production of L-(+) lactic acid on fermentation of CF using inexpensive nitrogen sources and on changes in the production as a response from interaction of factors. Use of inexpensive nitrogen sources and starch as substrate in MRS medium for single-step fermentation of lactic acid can become an efficient, economic and viable process. This report is on optimization of inexpensive nitrogen sources completely replacing peptone and yeast extract in single-step submerged fermentation of starch (present in CF) to lactic acid with high production efficiency.     

不同pH调节剂对产琥珀酸放线杆菌NJ113发酵产丁二酸的影响

在3L发酵罐中分别采用不同的碱性物质作为pH调节剂,考察其对产琥珀酸放线杆菌Actinobacillus succinogenes NJ113厌氧发酵制备丁二酸的影响。结果表明:Ca2+、NH4+调节剂对菌体生长代谢有较大阻碍作用,丁二酸产量较低;采用含Na+调节剂,在发酵中后期菌体出现絮凝现象严重,且产丁二酸能力骤降;采用含Mg2+调节剂,整个发酵过程菌体代谢旺盛,发酵效果较佳。根据各碱性物质的调节能力以及对菌体生长代谢的影响,选择NaOH、Mg(OH)2和Na2CO3、Mg(OH)2分别作为混合碱组分调节pH,并对两组混合碱中各物质的质量比例进行优化。结果表明,以NaOH、Mg(OH)2混合,两者质量比为1:1时,发酵效果最好,丁二酸质量浓度高达到69.8g/L,质量收率74.5%。该种混合碱配比可有效替代碱式MgCO3调节pH,既达到高产丁二酸的目的,又可降低生物制备丁二酸的成本。     

Effects of neutralizing agents on lactic acid production by Rhizopus oryzae using sweet potato starch

A neutralizing agent is usually employed to counteract the pH reduction during lactic acid fermentation by Rhizopus oryzae. Calcium carbonate (CaCO₃) is used as such a pH controlling agent. The low solubility of CaCO₃ in the fermentation broth could however lead to low efficiency in pH control and cause problems in the subsequent purification process. Therefore, an alternative agent in place of CaCO₃ was examined in this study. The effect of four different neutralizing agents, including CaCO₃, sodium hydroxide (NaOH), ammoniacal solution and sodium bicarbonate (NaHCO₃) on lactic acid production and the morphology of the pellets were investigated. Results indicated that CaCO₃ was still the preferred choice, because of the pellet morphology and the highest lactic acid concentration (43.3 g/L) obtained in the batch using 60 g/L of sweet potato starch as feedstock. It is noteworthy that the lactic acid purification is relatively easier when using NaHCO₃ instead of CaCO₃, due to the higher solubility of sodium lactate than calcium lactate. Therefore, even the batch with CaCO₃ had a slightly higher productivity (1.23 g/L/h) than the batch with NaHCO₃ (1.14 g/L/h), NaHCO₃ might be the first choice for process designers whenever recovery is vital.     

不同pH调节剂对补料批式发酵产1,3-丙二醇的影响

对肺炎克雷伯氏菌（Klebsiellapneumoniae）发酵生产1,3-丙二醇（1,3-Propanediol,1,3．PD）的补碱策略进行了研究。分别利用NaOH、氨水、KOH三种溶液作为pH调节剂,优化三种pH调节剂并得到按一定比例混合的混合碱。当采用混合碱调控发酵pH值为7．0时,1,3-丙二醇的产量达到了55dL,比无pH调控（对照）发酵过程发酵水平提高了10．6倍。     

米根霉发酵生产L-乳酸

报道了Ｌ－乳酸菌株的分离与筛选,探讨了不同碳源、氮源、通气量、温度等发酵条件对产Ｌ－乳酸的影响,从７８株米根霉中筛选出１３株产Ｌ－乳酸较高的菌株,其中米根霉（Ｒｈｉｚｏｐｕｓ ｏｒｙｚａｅ）Ｒｓ９２８产Ｌ－乳酸最高,产酸最稳定。试验结果表明,该菌株最适发酵培养组成（％）：淀粉水解糖１６,ＭｇＳＯ４ ０．０８,ＫＨ２ＰＯ４ ０．０５,ＺｎＳＯ４ ０．０１,ＣａＣＯ３ ７,ｐＨ自然。在６０ｔ发酵罐中,     

代谢甘油高产乳酸的菌种选育及培养基优化

分离出一株可高效利用甘油生产乳酸的菌株, 经过生理生化和16S rDNA分子鉴定, 确定其属于大肠埃希氏菌, 命名为Escherichia coli AC-521。通过五因素四水平正交试验, 优化了其最佳发酵培养基成分为初始甘油70 g/L, 酵母粉4 g/L, 蛋白胨7 g/L, (NH4)2SO4 10 g/L, K2HPO4 2.5 g/L。利用该最佳条件的5 L发酵罐批式补料发酵实验表明: 该菌株发酵80 h后, 乳酸产量可达到74.5 g/L, 得率为0.87 mol/mol甘油。