大肠杆菌利用木糖发酵产琥珀酸的研究

目的:研究大肠杆菌以木糖为碳源发酵产琥珀酸。方法:首先比较了实验室保藏的7种野生型大肠杆菌利用木糖发酵产琥珀酸的产量和得率,结果:表明野生型菌株琥珀酸对木糖的得率集中在0.34g/g~0.53g/g之间,得率较低,副产物主要为乳酸、乙酸。然后选取其中2株菌(E.coli MG1655与E.coli C-1)进行基因敲除,构建了ldhA和pflB双基因缺失的MLB和CLB菌株,以减少副产物的积累。两阶段摇瓶发酵结果表明,琥珀酸得率从0.40g/g分别提高到了0.89g/g及0.90g/g,而产量分别从4.92g/L、5.58g/L提高到11.52g/L、11.81g/L。结论:通过基因敲除后,大肠杆菌能够利用木糖发酵产琥珀酸,琥珀酸得率可以达到0.90g/g。     

常压室温等离子体诱变高效利用木糖产丁二酸菌株

大肠杆菌Escherichia coli AFP111是E. coli NZN111 (△pflAB△ldhA) 的ptsG自发突变株,其转化1 mol的木糖合成丁二酸的过程中净产生1.67 mol ATP,但是转化1 mol的木糖合成丁二酸的过程中实际需要2.67 mol ATP,因此在厌氧条件下,ATP的供给不足导致E. coli AFP111不能代谢木糖。采用常压室温等离子体射流诱变产丁二酸大肠杆菌菌株,在厌氧条件下,利用以木糖为碳源的M9培养基,筛选得到一株可以代谢木糖并积累丁二酸的突变株DC111。该突变菌株在发酵培养基中,72 h内可以消耗10.52 g/L木糖产6.46 g/L的丁二酸,丁二酸的得率达到了0.78 mol/mol。而且突变株中伴有ATP产生的磷酸烯醇式丙酮酸羧激酶 (PCK) 途径得到加强,PCK的比酶活相对于出发菌株提高了19.33倍,使得其在厌氧条件下能够有足够的ATP供给来代谢木糖发酵产丁二酸。     

产D-乳酸重组大肠杆菌ptsG基因的敲除及其混合糖同步发酵

为构建能够同时高效利用五碳糖和六碳糖发酵产D-乳酸的重组大肠杆菌工程菌,以能高效利用五碳糖发酵产D-乳酸的大肠杆菌工程菌E.coli JH13为出发菌株,通过Red同源重组技术敲除葡萄糖跨膜转运基因pts G。实验结果表明,pts G缺陷菌株E.coli JH15在10%混合糖(5%葡萄糖和5%木糖)培养基中发酵,可同时利用五碳糖和六碳糖以完成发酵;而对照菌葡萄糖消耗完才利用木糖,发酵结束还有18 g/L木糖残留;JH15乳酸产量为83.04 g/L,相比于对照菌株提高了25.86%;在稻草秸秆水解液中发酵,JH15同时利用葡萄糖、木糖和L-阿拉伯糖,乳酸产量为25.15 g/L,转化率为86.42%。JH15作为能利用混合糖同步发酵产D-乳酸的大肠杆菌工程菌,它的成功构建为利用廉价的木质纤维素水解物为原料发酵生产D-乳酸提供参考依据。     

大肠杆菌突变株QQS101发酵生产琥珀酸初步研究

琥珀酸是一种具有重要应用价值的生物基平台化合物。对大肠杆菌focA-pflB ldhA突变株QQS101在严格厌氧条件下生长和葡萄糖代谢能力进行了考察,比较分析了葡萄糖与大肠杆菌混合酸发酵产物的单位碳的还原程度,认为非严格厌氧条件有利于QQS101发酵葡萄糖积累琥珀酸,进一步对有氧生长碳源进行了对比试验的结果表明,以木糖支持有氧生长,QQS101摇瓶发酵39 h消耗葡萄糖37.6 g/L,琥珀酸的产量达到31.01 g/L,摩尔产率为1.258 mol Succinate/mol Glucose。发酵过程中,丙氨酸的添加能够提高琥珀酸的摩尔产率。     

代谢木糖重组谷氨酸棒杆菌的构建

为了使谷氨酸棒杆菌较好地利用木糖生产有机酸,将来自Escherichia coli K-12的木糖异构酶基因xylA构建到表达载体pXMJ19中,导入Corynebacterium glutamicum ATCC13032Δldh中,成功表达了该酶基因。结果表明:重组菌株在以木糖为唯一C源进行发酵时,木糖的消耗速率为0.54 g/(L·h),木糖异构酶比酶活约为0.54 U/mL;在以木糖和葡萄糖的混合糖为C源进行发酵时,菌株优先利用葡萄糖,在葡萄糖完全消耗后,菌株开始有效利用木糖;以木糖为唯一C源进行两阶段发酵时,琥珀酸的收率可达(0.62±0.003)g/g。     

共表达烟酸转磷酸核糖激酶和丙酮酸羧化酶对大肠杆菌NZN111产丁二酸的影响

构建了共表达烟酸转磷酸核糖激酶(NAPRTase)和丙酮酸羧化酶(PYC)的重组质粒pTrc99a-pncB-pyc,并考察了重组菌E.coli NZN111/pTrc99a-pncB-pyc生产丁二酸的能力。结果表明:重组菌NZN111/pTrc99a-pncB-pyc的NAPRTase和PYC的比酶活达到最高,分别为20.75和1.04 U/mg,同时,辅酶NADH、NAD+及NAD(H)总量达到最高。厌氧摇瓶发酵结果:48 h能够消耗17.5 g/L的葡萄糖生成14.08 g/L的丁二酸,而丙酮酸的产量大幅度降低,仅为0.11 g/L。本研究为基因工程菌大肠杆菌厌氧条件下发酵生产丁二酸提供了一定的基础。     

果糖和麦芽糖作为有氧碳源对大肠杆菌NZN111两阶段发酵中厌氧发酵的影响

为了了解磷酸转移酶转运系统 (PTS) 依赖和非PTS依赖代谢的糖类对大肠杆菌生产琥珀酸的影响,进行了两阶段培养,有氧阶段采用PTS依赖型的果糖或非PTS依赖型的麦芽糖作为丙酮酸甲酸裂解酶 (PFL) 和乳酸脱氢酶 (LDH) 双突变株NZN111的碳源,研究其对NZN111厌氧阶段代谢葡萄糖的影响。5 L罐发酵结果表明,以果糖和麦芽糖为碳源有氧培养的细胞恢复了在厌氧条件下快速代谢葡萄糖的能力,琥珀酸和丙酮酸成为主要代谢产物,最终琥珀酸得率分别为0.84和0.75 mol/mol,丙酮酸得率分别达到了0.65和0.83 mol/mol,琥珀酸和丙酮酸终浓度比分别为1.73∶1和1.21∶1。果糖和麦芽糖培养的NZN111与葡萄糖培养的菌体代谢的明显差异推测是cyclic AMP (cAMP) 依赖型和非cAMP依赖型的分解代谢物阻遏调控这两种机制共同作用的结果。     

玉米秸秆水解液发酵联产氢气与2,3-丁二醇的初步研究

选用实验室自行筛选的Klebsiella pneumoniae ECU-15,进行了玉米秸秆水解液发酵联产氢气和2,3-丁二醇的初步研究。结果表明:以葡萄糖为碳源时,两目标产物随培养条件的改变呈现相同的变化趋势,且最佳发酵温度为37℃,最佳pH为6.0,最佳初始糖浓度为30 g/L;不同比例葡萄糖/木糖为混合碳源时,均能实现氢气和2,3-丁二醇的联产过程,但随着木糖含量的增加,细胞产量、氢气产量和2,3-丁二醇的产量都有所下降,并且木糖的存在会降低葡萄糖的消耗速率;实验最后以玉米秸秆水解液和同比例模拟合成培养基为底物,初步探明了该菌株利用水解液发酵联产氢气和2,3-丁二醇的可行性,最终氢气产量为0.65 v/v,产氢得率为0.43 mol/mol sugar;2,3-丁二醇产量为5.05 g/L,得率为0.82 mol/mol sugar。     

过量表达NADH氧化酶加速光滑球拟酵母合成丙酮酸

[目的]进一步提高光滑球拟酵母(Torulopsis glabrata)发酵生产丙酮酸的生产强度.[方法]将来源于乳酸乳球菌(Lactococcus lactis)中编码形成水的NADH氧化酶noxE基因过量表达于丙酮酸工业生产菌株T. glabrata CCTCC M202019中,获得了一株NADH氧化酶活性为34.8 U/mg蛋白的重组菌T. glabrata-PDnoxE.[结果]与出发菌株T. glabrata CCTCC M202019相比,细胞浓度、葡萄糖消耗速率和丙酮酸生产强度分别提高了168%、44.9%和12%,发酵进行到36 h葡萄糖消耗完毕.补加50 g/L葡萄糖继续发酵20 h,则使丙酮酸浓度提高到67.2 g/L.葡萄糖消耗速度和丙酮酸生产强度增加的原因在于形成水的NADH氧化酶过量表达,导致NADH和ATP含量分别降低了18.1%和15.8%.而NAD<' 增加了11.1%.[结论]增加细胞内NAD<' 含量能有效地提高酵母细胞葡萄糖的代谢速度及目标代谢产物的生产强度.     

代谢改造热带假丝酵母发酵木糖母液生产木糖醇

木糖醇是一种在食品、医药、轻工等领域具有广泛用途的多元醇,目前主要通过酸水解木聚糖获得木糖并进一步化学催化加氢方法制备。提取木糖过程中会产生大量的木糖母液副产物,其中含有一定浓度的葡萄糖、木糖、阿拉伯糖等碳源,以及少量的糠醛、四氢呋喃等物质。研究微生物转化木糖母液生产高附加值化学品不仅能够提高木糖母液的利用价值,而且能够减少环境污染。热带假丝酵母不仅能够利用葡萄糖,也具有高效的木糖代谢途径。首先利用代谢工程技术删除了热带假丝酵母菌株的木糖醇脱氢酶基因,获得能够转化木糖积累木糖醇的突变株。在此基础上,评价了突变株在木糖母液培养基中的发酵性能。通过单因素优化实验确定了突变株发酵生产木糖醇较优的发酵工艺:培养基组成为木糖母液300g/L,玉米浆5g/L;最佳发酵条件为:发酵温度35℃,初始p H为5.0,接种量15%,200r/min摇床培养140h。利用优化后的发酵工艺,木糖醇产量达到83.01g/L。初步建立了转化木糖母液生产木糖醇的工艺,为进一步利用木糖母液奠定了基础。     

Effect of different carbon sources on the production of succinic acid using metabolically engineered Escherichia coli

Succinic acid (SA) is an important platform molecule in the synthesis of a number of commodity and specialty chemicals. In the present work, dual-phase batch fermentations with the E. coli strain AFP184 were performed using a medium suited for large-scale industrial production of SA. The ability of the strain to ferment different sugars was investigated. The sugars studied were sucrose, glucose, fructose, xylose, and equal mixtures of glucose and fructose and glucose and xylose at a total initial sugar concentration of 100 g L-1. AFP184 was able to utilize all sugars and sugar combinations except sucrose for biomass generation and succinate production. For sucrose as a substrate no succinic acid was produced and none of the sucrose was metabolized. The succinic acid yield from glucose (0.83 g succinic acid per gram glucose consumed anaerobically) was higher than the yield from fructose (0.66 g g-1). When using xylose as a carbon source, a yield of 0.50 g g-1 was obtained. In the mixed-sugar fermentations no catabolite repression was detected. Mixtures of glucose and xylose resulted in higher yields (0.60 g g-1) than use of xylose alone. Fermenting glucose mixed with fructose gave a lower yield (0.58 g g-1) than fructose used as the sole carbon source. The reason is an increased pyruvate production. The pyruvate concentration decreased later in the fermentation. Final succinic acid concentrations were in the range of 25-40 g L-1. Acetic and pyruvic acid were the only other products detected and accumulated to concentrations of 2.7-6.7 and 0-2.7 g L-1. Production of succinic acid decreased when organic acid concentrations reached approximately 30 g L-1. This study demonstrates that E. coli strain AFP184 is able to produce succinic acid in a low cost medium from a variety of sugars with only small amounts of byproducts formed.     

Proteomics analysis of Bifidobacterium longum NCC2705 growing on glucose, fructose, mannose, xylose, ribose, and galactose

To investigate the molecular mechanisms underlying carbohydrate uptake and connected metabolic pathways of Bifidobacterium longum NCC2705, the proteomic profiles of bacteria grown on different carbon sources including glucose, fructose, mannose, xylose, ribose, and galactose were analyzed. Our results show that all sugars tested were catabolized via the bifid shunt. Sixty-eight proteins that exhibited changes in abundance of threefold or greater were identified by MS. A striking observation was the differential expression of proteins related to the pyruvate metabolism. Further analysis of acetic acid and lactic acid in the culture supernatants by HPLC at the end of fermentation showed that more lactic acid was produced during growth on fructose, ribose, xylose, galactose and more acetic acid was produced during the fermentation of glucose and mannose. Growth experiments revealed that B. longum NCC2705 preferentially used fructose, ribose, xylose, and galactose with higher growth rates over glucose and mannose. Furthermore, five proteins (GroEL, Eno, Tal, Pgm, and BL0033) exhibited clear phosphorylation modifications at serine and/or tyrosine residues. BL0033, a component of an ATP-binding cassette (ABC) transporter, was significantly more abundant in bacteria grown on fructose and, to a lesser extent, ribose and xylose. RT-PCR analysis revealed that all genes of the ABC transporter are induced in the presence of these sugars suggesting that BL0033, BL0034, BL0035, and BL0036 constitute an ABC transporter with fructose as preferred substrate.     

Succinic acid production by <Emphasis Type="Italic">Actinobacillus succinogenes</Emphasis> from batch fermentation of mixed sugars

Succinic acid production from the monosaccharides xylose, arabinose, glucose, mannose and galactose was studied using the bacterium Actinobacillus succinogenes. In Duran bottle cultures, containing 10 g/L of each of sugar, succinic acid was produced from all sugars except for galactose. The highest succinate yield, 0.56 g/g, was obtained with glucose, whereas the succinate yield was 0.42, 0.38 and 0.44 g/g for xylose, mannose and arabinose, respectively. The specific succinate productivity was 0.7 g/g h for glucose, but below 0.2 g/g h for the other sugars. Batch bioreactor fermentations were carried out using a sugar mixture of the five sugars giving a total concentration of 50 g/L, mimicking the distribution of sugars in spent sulfite liquor (SSL) from Eucalyptus which is rich in xylose. In this mixture, an almost complete conversion of all sugars (except galactose) was achieved resulting in a final succinate concentration of 21.8–26.8 g/L and a total yield of 0.59–0.68 g/g. There was evidence of co-consumption of glucose and xylose, whereas mannose was consumed after glucose. The main by-products were acetate 0.14–0.20 g/g and formate 0.08–0.13 g/g. NADH balance calculations suggested that NADH required for succinate production was not met solely from formate and acetate production, but other means of NADH production was necessary. Results from mixed sugar fermentations were verified using SSL as substrate resulting in a succinate yield of 0.60 g/g. In addition, it was found that CO₂ sparging could replace carbonate supply in the form of MgCO₃ without affecting the succinate yield.     

The influence of aeration and hemicellulosic sugars on xylitol production by Candida tropicalis

The influence of other hemicellulosic sugars (arabinose, galactose, mannose and glucose), oxygen limitation, and initial xylose concentration on the fermentation of xylose to xylitol was investigated using experimental design methodology. Oxygen limitation and initial xylose concentration had considerable influences on xylitol production by Canadida tropicalis ATCC 96745. Under semiaerobic conditions, the maximum xylitol yield was 0.62 g/g substrate, while under aerobic conditions, the maximum volumetric productivity was 0.90 g/l h. In the presence of glucose, xylose utilization was strongly repressed and sequential sugar utilization was observed. Ethanol produced from the glucose caused 50% reduction in xylitol yield when its concentration exceeded 30 g/l. When complex synthetic hemicellulosic sugars were fermented, glucose was initially consumed followed by a simultaneous uptake of the other sugars. The maximum xylitol yield (0.84 g/g) and volumetric productivity (0.49 g/l h) were obtained for substrates containing high arabinose and low glucose and mannose contents.     

Efficient ethanol production from glucose, lactose, and xylose by recombinant Escherichia coli.

Lactose and all of the major sugars (glucose, xylose, arabinose, galactose, and mannose) present in cellulose and hemicellulose were converted to ethanol by recombinant Escherichia coli containing plasmid-borne genes encoding the enzymes for the ethanol pathway from Zymomonas mobilis. Environmental tolerances, plasmid stability, expression of Z. mobilis pyruvate decarboxylase, substrate range, and ethanol production (from glucose, lactose, and xylose) were compared among eight American Type Culture Collection strains. E. coli ATCC 9637(pLO1297), ATCC 11303(pLO1297), and ATCC 15224(pLO1297) were selected for further development on the basis of environmental hardiness and ethanol production. Volumetric ethanol productivities per hour in batch culture were 1.4 g/liter for glucose (12%), 1.3 g/liter for lactose (12%), and 0.64 g/liter for xylose (8%). Ethanol productivities per hour ranged from 2.1 g/g of cell dry weight with 12% glucose to 1.3 g/g of cell dry weight with 8% xylose. The ethanol yield per gram of xylose was higher for recombinant E. coli than commonly reported for Saccharomyces cerevisiae with glucose. Glucose (12%), lactose (12%), and xylose (8%) were converted to (by volume) 7.2% ethanol, 6.5% ethanol, and 5.2% ethanol, respectively.     

Efficient ethanol production from glucose, lactose, and xylose by recombinant Escherichia coli

Lactose and all of the major sugars (glucose, xylose, arabinose, galactose, and mannose) present in cellulose and hemicellulose were converted to ethanol by recombinant Escherichia coli containing plasmid-borne genes encoding the enzymes for the ethanol pathway from Zymomonas mobilis. Environmental tolerances, plasmid stability, expression of Z. mobilis pyruvate decarboxylase, substrate range, and ethanol production (from glucose, lactose, and xylose) were compared among eight American Type Culture Collection strains. E. coli ATCC 9637(pLO1297), ATCC 11303(pLO1297), and ATCC 15224(pLO1297) were selected for further development on the basis of environmental hardiness and ethanol production. Volumetric ethanol productivities per hour in batch culture were 1.4 g/liter for glucose (12%), 1.3 g/liter for lactose (12%), and 0.64 g/liter for xylose (8%). Ethanol productivities per hour ranged from 2.1 g/g of cell dry weight with 12% glucose to 1.3 g/g of cell dry weight with 8% xylose. The ethanol yield per gram of xylose was higher for recombinant E. coli than commonly reported for Saccharomyces cerevisiae with glucose. Glucose (12%), lactose (12%), and xylose (8%) were converted to (by volume) 7.2% ethanol, 6.5% ethanol, and 5.2% ethanol, respectively.     

Ethanol production from wood hydrolysate using genetically engineered Zymomonas mobilis

An ethanologenic microorganism capable of fermenting all of the sugars released from lignocellulosic biomass through a saccharification process is essential for secondary bioethanol production. We therefore genetically engineered the ethanologenic bacterium Zymomonas mobilis such that it efficiently produced bioethanol from the hydrolysate of wood biomass containing glucose, mannose, and xylose as major sugar components. This was accomplished by introducing genes encoding mannose and xylose catabolic enzymes from Escherichia coli. Integration of E. coli manA into Z. mobilis chromosomal DNA conferred the ability to co-ferment mannose and glucose, producing 91 % of the theoretical yield of ethanol within 36 h. Then, by introducing a recombinant plasmid harboring the genes encoding E. coli xylA, xylB, tal, and tktA, we broadened the range of fermentable sugar substrates for Z. mobilis to include mannose and xylose as well as glucose. The resultant strain was able to ferment a mixture of 20 g/l glucose, 20 g/l mannose, and 20 g/l xylose as major sugar components of wood hydrolysate within 72 h, producing 89.8 % of the theoretical yield. The recombinant Z. mobilis also efficiently fermented actual acid hydrolysate prepared from cellulosic feedstock containing glucose, mannose, and xylose. Moreover, a reactor packed with the strain continuously produced ethanol from acid hydrolysate of wood biomass from coniferous trees for 10 days without accumulation of residual sugars. Ethanol productivity was at 10.27 g/l h at a dilution rate of 0.25 h(-1).     

Glass capillary or fused-silica gas chromatography—mass spectrometry of several monosaccharides and related sugars: Improved resolution

The gas chromatographic separation of several monosaccharides and related sugars derivatized by methoxylation and trimethylsilylation reactions was optimized with glass capillary (SP-2250) and fused silica (SP-2100) columns. Individual sugars included aldoses, ketoses, polyols, acidic forms and N-acetylated amino sugars. Peaks were detected by selected ion monitoring (SIM). The fused silica column gave complete resolution of all peaks (two per hexose and one per hexitol) arising from glucose, galactose, mannose, fructose, sorbitol, mannitol and dulcitol. The resolution of these sugars with the glass capillary column was not as good, but full differentiation was possible on the basis of SIM. Because the fused silica column gave a better resolution of 33 sugars tested and was more easily installed than the glass capillary column, it was utilized for quantitative analysis. A deuterated algal sugar mixture used for quantitation by isotope dilution was found to contain glucose, galactose, mannose, xylose, arabinose, ribose and rhamnose. Full recoveries were obtained of various amounts of glucose, galactose, mannose, fructose and xylose added to human serum.     

Effect of lpdA gene knockout on the metabolism in Escherichia coli based on enzyme activities, intracellular metabolite concentrations and metabolic flux analysis by 13C-labeling experiments

The lipoamide dehydrogenase (LPD) encoded by lpdA gene is a component of the pyruvate dehydrogenase complex (PDHc), alpha-ketoglutarate dehydrogenase (AKGDH) and the glycine cleavage multi-enzyme (GCV) systems. In the present study, cell growth characteristics, enzyme activities and intracellular metabolite concentrations were compared between the parent strain Escherichia coli BW25113 and its lpdA knockout mutant in batch and continuous cultures. The lpdA knockout mutant produced significantly more pyruvate and L-glutamate under aerobiosis. Some D-lactate and succinate also accumulated in the culture broth. Based on the investigation of enzyme activities and intracellular metabolite concentrations, acetyl-CoA was considered to be formed by the combined reactions through pyruvate oxidase (PoxB), acetyl-CoA synthetase (Acs) and acetate kinase (Ack)-phosphoacetyltransferase (Pta) in the lpdA mutant. The effect of the lpdA gene knockout on the intracellular metabolic flux distributions was investigated based on 1H-13C NMR spectra and GC-MS signals obtained from 13C-labeling experiment using the mixture of [U-13C] glucose, [1-13C] glucose, and naturally labeled glucose. Flux analysis of the lpdA mutant indicated that the Entner-Doudoroff (ED) pathway and the glyoxylate shunt were activated. The fluxes through glycolysis and oxidative pentose phosphate (PP) pathway (except for the flux through glucose-6-phosphate dehydrogenase) were slightly downregulated. The TCA cycle was also downregulated in the mutant strain. On the other hand, the fluxes through the anaplerotic reactions of PEP carboxylase, PEP carboxykinase and malic enzyme were upregulated, which were consistent with the results of enzyme activities. Furthermore, the influence of the poxB gene knockout on the growth of E. coli was also studied because of its similar function to PDHc which connects the glycolysis to the TCA cycle. Under aerobiosis, a comparison of lpdA mutant and poxB mutant indicated that PDHc is the main enzyme which catalyzes the reaction from pyruvate to acetyl-CoA in the parent strain, while PoxB plays a very important role in the PDHc-deficient strain.     

L-lactic acid production from apple pomace by sequential hydrolysis and fermentation

The potential of apple pomace (a solid waste from cider and apple juice making factories) as a source of sugars and other compounds for fermentation was evaluated. The effect of the cellulase-to-solid ratio (CSR) and the liquor-to-solid ratio (LSR) on the kinetics of glucose and total monosaccharide generation was studied. Mathematical models suitable for reproducing and predicting the hydrolyzate composition were developed. When samples of apple pomace were subjected to enzymatic hydrolysis, the glucose and fructose present in the raw material as free monosaccharides were extracted at the beginning of the process. Using low cellulase and cellobiase charges (8.5 FPU/g-solid and 8.5 IU/g-solid, respectively), 79% of total glucan was saccharified after 12 h, leading to solutions containing up to 43.8 g monosaccharides/L (glucose, 22.8 g/L; fructose, 14.8 g/L; xylose+mannose+galactose, 2.5 g/L; arabinose+rhamnose, 2.8g/L). These results correspond to a monosaccharide/cellulase ratio of 0.06 g/FPU and to a volumetric productivity of 3.65 g of monosaccharides/L h. Liquors obtained under these conditions were used for fermentative lactic acid production with Lactobacillus rhamnosus CECT-288, leading to media containing up to 32.5 g/L of L-lactic acid after 6 h (volumetric productivity=5.41 g/L h, product yield=0.88 g/g).