废糟液全循环对自絮凝酵母糖酵解途径关键酶、胁迫相关代谢物及胞内组分的影响

旨在研究废糟液直接全循环对絮凝酵母乙醇发酵、糖酵解关键酶以及细胞组成的影响。在一有效容积1.5 L的搅拌式生物反应器中,使用葡萄糖为220 g/L,添加8 g/L酵母粉和6 g/L蛋白胨的培养基,以0.04 h?1的稀释率进行自絮凝颗粒酵母乙醇连续发酵。每隔3天将收集到的发酵液集中精馏处理,得到的废糟液用于配制发酵培养基。装置运行近20 d,实验结果表明,随着废液循环批次的增加,系统乙醇和生物量浓度明显降低,糖酵解途径3个关键限速酶:己糖激酶、6-磷酸果糖激酶和丙酮酸激酶不同程度受到抑制。为了应对废糟液中高沸点副产物积累导致的环境胁迫,维持细胞正常代谢,甘油和菌体胞内蛋白生物合成加强,碳水化合物积累减弱。这些研究结果对进一步研究高沸点副产物积累对酵母细胞乙醇发酵影响的机理和菌种的代谢工程改造,具有重要意义。     

多级串联悬浮床反应器系统中自絮凝颗粒酵母乙醇连续发酵耦合废糟液直接全循环使用的研究

在一套四级串联悬浮床生物反应器系统中,以双酶法制备的玉米粉糖化液为底物,进行了废糟液全循环条件下自絮凝颗粒酵母乙醇连续发酵的实验研究。在实验中,每隔5 d将从末级反应器收集到的发酵液集中精馏处理,得到的废糟液直接用于玉米粉调浆制糖。系统连续运行了120d,共进行了24批次实验,数据分析表明系统达到了平衡状态。在平均发酵时间为20h条件下,发酵终点乙醇浓度平均为11.7%（V/V）,残还原糖浓度平均为7.9g/L,装置运行平稳。这些工作为自絮凝颗粒酵母乙醇发酵耦合废糟液直接全循环使用、实现污染物源头减废、清洁生产奠定了理论和实验基础。     

自絮凝颗粒酵母乙醇连续发酵耦合废液全循环工艺的研究

在以CO2为驱动力的单级悬浮床生物反应器中,进行了自絮凝颗粒酵母乙醇连续发酵耦合废液全循环实验研究。以双酶法制备的玉米粉糖化液为底物,系统连续运行了28 d,每隔5 d将收集到的发酵液集中精馏处理,得到的废糟液直接用于玉米粉调浆制糖。实验数据表明,在稀释率为0.05 h-1条件下,发酵液中乙醇、残还原糖、残总糖质量浓度基本稳定,其平均值为82.97,30.02和40.87 g.L-1。对废液循环工艺过程中,发酵液中的8种高沸点有机酸进行了定量分析,发现发酵液中仅丙酮酸有明显积累,并最终在0.1~0.3 mol.L-1范围内波动。实验结果表明:系统中存在的高沸点副产物不对乙醇发酵产生明显抑制作用,乙醇连续发酵能够在废液全循环条件下良好运行。     

戊糖和己糖共发酵生产燃料乙醇条件研究

利用嗜鞣管囊酵母P-01对木糖和葡萄糖共发酵生产燃料乙醇的条件进行了试验研究,结果表明,木糖和葡萄糖混合液生产燃料乙醇的最佳条件为发酵液的pH值5.5、30℃、摇床转速120 r/min、接种量10%、发酵液初始糖浓度6%、葡萄糖与木糖之比为2、发酵周期为84h。在最佳发酵条件下,发酵醪液中的燃料乙醇浓度为2.101%,糖醇转化率为35%。     

自絮凝颗粒酵母酒精高浓度连续发酵的研究

在四釜串联气升环流悬浮床生物反应器系统中 ,进行了絮凝颗粒酵母酒精连续发酵的研究。以CO2 为驱动动力 ,发酵液液蒸馏废液全循环 ,稀释率为 0 2 h。发酵成熟醑酒精平均浓度为 96 6g L ,残余还原糖和总糖分别为 1 2g L和 4 1g L。     

不用离心机高浓度单细胞蛋白的制取

<正> 美国的菲利普石油公司最近成功地开发了独特的Provesteen过程。该过程以甲醇或乙醇为原料,用连续发酵法制取。单细胞的生成浓度高,适于作动物饲料,也可生产人类食用的酵母。在酵母发酵罐中供给由石油或天然气合成的酒精、也可用发酵法制得的酒精。此外还向发酵罐中供给氨、无机盐、氧或空气。发酵液连续地经过灭菌装置后送入喷雾干燥器。过程的重要特点是,由于使用该公司的独特的酵母,在发酵罐内生成的单细胞蛋白浓度     

串联填充管式反应系统中高浓度乙醇连续发酵

在一套由搅拌罐和管式反应器串联而成的组合式反应系统中,利用酿酒酵母进行连续发酵生产高浓度乙醇。后续管式反应器内通过装填聚氨酯颗粒和木块对酵母细胞进行吸附固定化,在乙醇抑制造成细胞活性大幅降低的情况下,通过大幅提高细胞浓度保证发酵效率,在稀释速率0.02h^-1和280g/L葡萄糖的条件下,系统的终点乙醇浓度为15.4 % (v/v)。研究表明在一定稀释速率之下,应该通过增加反应器的级数来降低稀释速率,以达到提高终点乙醇浓度,如简单地降低进料速率则可能增加整个系统所受的乙醇抑制,对提高终点乙醇浓度效果不显著。     

乙醇-黄原胶耦联两步发酵

初步探索乙醇-黄原胶耦联两步发酵的可行性和生产工艺,即控制乙醇发酵,发酵液去除固形物后蒸馏回收酒精,然后利用酒精糟液中剩余营养物质进行黄原胶发酵。摇瓶和小罐试验证实方案是可行的,耦联发酵工艺优化条件:选择木薯淀粉进行乙醇发酵60 h后的酒精糟液,添加2 g/L KH2PO4,不添加无机N源。在优化条件下,7 L发酵罐中耦联发酵的黄原胶产量达到20 g/L,转化率约为50%。     

纤维素乙醇发酵液中复杂组分对乙醇渗透汽化传质过程的影响

考察了木质纤维素乙醇发酵液中各组分对乙醇透过聚二甲基硅氧烷(PDMS)-silicalite-1渗透汽化膜传质性能的影响。结果表明:酵母细胞、玉米秸秆残渣和发酵用无机盐可增加乙醇通过膜的通量和选择性;而葡萄糖和甘油的存在会对乙醇的透膜传质产生负面影响;木质纤维素水解后的产物如糠醛和羟基丙酮,表现出对膜分离乙醇轻微的抑制作用。本文建立了渗透汽化优先透醇与纤维素乙醇发酵集成过程,批次发酵20 h后乙醇产率从最初的12.95下降到10.22 g/(L·h),60 h后乙醇产率下降为0,葡萄糖消耗速率与乙醇消耗产率呈同样趋势;连续发酵过程中,乙醇产率较稳定地维持在13.30 g/(L·h)。实验证明,集成过程可及时地将产物乙醇分离出去,能够有效地消除产物抑制,提高乙醇生产速率和葡萄糖转化率。     

超高浓度培养基条件下酵母细胞生长及酒精生成的准稳态动力学研究

在1．5L搅拌式发酵罐中,使用葡萄糖质量浓度分别为120、200、280g／L的培养基进行酿酒酵母Saccharomyces cerevisiae连续发酵生成酒精的动力学研究。研究发现,当培养基中葡萄糖浓度为200和280g／L时,发酵液中残糖浓度、酒精浓度以及菌体生物量从小幅度波动的准稳态发展到大幅度波动的振荡状态。提出了伴有周期性振荡现象准稳态过程的概念,并针对该过程,建立了兼有底物和产物抑制的酵母细胞生长和产物酒精生成动力学模型。     

Stillage backset and its impact on ethanol fermentation by the flocculating yeast

The second largest cost in fuel ethanol production is from energy consumption with ethanol distillation and stillage treatment, particularly when stillage is treated by the multi-evaporation process. Therefore, stillage backset is the most economically competitive strategy for reducing discharge and saving energy consumption. In this article, continuous ethanol fermentation was performed by the flocculating yeast under stillage backset conditions. Compared to regular yeast, immobilized yeast within the fermentor through flocculation reduced byproducts formation in the stillage, since heat lysis of yeast during ethanol distillation was prevented, and many side reactions were thus eliminated, making more stillage backset within the fermentation system possible. Although pyruvic acid, succinic acid, citric acid, α-ketoglutaric acid, fumaric acid and glycerol from yeast metabolism, furfural and 5-hydroxymethyl furfural from process operations, and acetic acid and lactic acid from slight contamination were accumulated with the stillage backset, they had no significant impact on yeast growth and ethanol fermentation due to low concentrations accumulated within the fermentation system. However, propionic acid that was generated mainly during hydrolysate sterilization and distillation of the fermentation broth was detected as the major inhibitor, but this byproduct would be significantly reduced under industrial conditions without hydrolysate sterilization, making the stillage backset more reliable for industrial application.     

Effect of propionic acid on citric acid fermentation in an integrated citric acid–methane fermentation process

In this study, an integrated citric acid-methane fermentation process was established to solve the problem of wastewater treatment in citric acid production. Citric acid wastewater was treated through anaerobic digestion and then the anaerobic digestion effluent (ADE) was further treated and recycled for the next batch citric acid fermentation. This process could eliminate wastewater discharge and reduce water resource consumption. Propionic acid was found in the ADE and its concentration continually increased in recycling. Effect of propionic acid on citric acid fermentation was investigated, and results indicated that influence of propionic acid on citric acid fermentation was contributed to the undissociated form. Citric acid fermentation was inhibited when the concentration of propionic acid was above 2, 4, and 6 mM in initial pH 4.0, 4.5 and, 5.0, respectively. However, low concentration of propionic acid could promote isomaltase activity which converted more isomaltose to available sugar, thereby increasing citric acid production. High concentration of propionic acid could influence the vitality of cell and prolong the lag phase, causing large amount of glucose still remaining in medium at the end of fermentation and decreasing citric acid production.     

Treatment of thin stillage by Aspergillus oryzae and its effect on alcoholic fermentation in syrup liquid

The microbial degradation of thin stillage for environment-friendly treatment has been studied extensively in recent years, and useful compounds in the treated-thin stillage are expected to be utilized in the subsequent fermentation. In this study, an Aspergillus oryzae H18, suitable for growing in thin stillage, was isolated from soil and served to degrade the organic matter in thin stillage, with the increase in pH (from 3·75 to 4·8) and decrease in chemical oxygen demand (COD, 81·3% removal rate). The effect of thin stillage as backset water after degradation of the strain H18 on alcohol production in syrup liquid was investigated. Compared with zero addition of thin stillage, the alcohol yield in mixed syrup liquid increased by 8·6% when the concentration of treated-thin stillage was 20%. After the addition of nutrients at proper concentration (0·5% urea, 1% molasses, 0·25% NaCl, 0·2% NaH₂PO₄, 0·3% MgSO₄ and 0·25% CaCl₂) in thin stillage, the alcohol yield in yeast fermentation was increased by 32·7% when mixed syrup liquid (with 40% thin stillage treated by H18) was employed, in comparison to control group without thin stillage addition. Meanwhile, the fermentation time was shortened, and alcohol production rate was enhanced.     

Salmonella typhimurium poultry isolate growth response to propionic acid and sodium propionate under aerobic and anaerobic conditions

Propionic acid and its sodium salt have long been used as additives in poultry feed to reduce microbial populations, including Salmonella spp. Propionic acids in poultry feed may have a potential role in inhibiting growth of Salmonella in the chicken intestine. In this study, we determined growth response of a Salmonella typhimurium poultry isolate to propionic acid and sodium propionate under aerobic and anaerobic conditions. Growth rate consistently decreased with the addition of greater concentrations of either propionic acid or sodium propionate. The extent of growth inhibition was much greater with propionic acid than the sodium form. Media pH decreased only with addition of propionic acid. Growth inhibition was more effective under anaerobic growth conditions with either propionic acid or sodium propionate. When determined at the same pH level, growth rate was significantly lowered by addition of 25 mM of either propionate or sodium propionate alone, and also by the decrease in pH levels (P<0.05). These results showed that growth inhibition of S. typhimurium by propionic acid or sodium propionate is greatly enhanced by pH decrease, and to lesser extent by anaerobiosis. We also found that sodium propionate was more inhibitory for growth of S. typhimurium than propionic acid when compared at the same pH levels.     

New technologies in value addition to the thin stillage from corn-to-ethanol process

Grain-to-ethanol production has increased steadily in the United States in the past few decades, which resulted in remarkable records in the availability of co-products. Dry-grind is the most common method of ethanol production worldwide, which concentrates the corn and yeast nutrients in the downstream operations. The ethanol co-products have traditionally been a commodity for livestock feed as they contain desirable nutrients, mostly sold as distiller’s grains. The liquid fraction produced after the centrifugation of the bottoms of the ethanol rectifying and distilling operations is named thin stillage, produced at volumes several times greater than those of ethanol. A portion of thin stillage is normally recycled as backset water, while the remaining goes through a series of evaporations. Evaporating a large amount of water from thin stillage is an energy-consuming process and recycling the thin stillage may lead to the accumulation of nutrients in co-products in distiller’s grains. There are several other industrial processes to utilize thin stillage, such as oil extraction, anaerobic digestion, and secondary fermentation. Recently, promising results have been reported on the production of important commodity chemicals, extracting high-value products, and energy production from thin stillage. This review provides an overview on the new processes and products via valorization of thin stillage by innovative technologies that are being currently developed. The new applications of thin stillage discussed in this review could open new opportunities for the ethanol plants and ethanol researchers by increasing the revenue and simultaneously reducing negative environmental impacts of ethanol production.     

Enhanced propionic acid production from Jerusalem artichoke hydrolysate by immobilized Propionibacterium acidipropionici in a fibrous-bed bioreactor

Propionic acid is an important chemical that is widely used in the food and chemical industries. To enhance propionic acid production, a fibrous-bed bioreactor (FBB) was constructed and Jerusalem artichoke hydrolysate was used as a low-cost renewable feedstock for immobilized fermentation. Comparison of the kinetics of immobilized-cell fermentation using the FBB with those of fed-batch free-cell fermentation showed that immobilized-cell fermentation gave a much higher propionic acid concentration (68.5 vs. 40.6 g/L), propionic acid yield (0.434 vs. 0.379 g/g) and propionic acid productivity (1.55 vs. 0.190 g/L/h) at pH 6.5. Furthermore, repeated batch fermentation, carried out to evaluate the stability of the FBB system, showed that long-term operation with a high average propionic acid yield of 0.483 g/g, high productivity of 3.69 g/L/h and propionic acid concentration of 26.2 g/L were achieved in all eight repeated batches during fermentation for more than 200 h. It is thus concluded that the FBB culture system can be utilized to realize the economical production of propionic acid from Jerusalem artichoke hydrolysate during long-term operation.     

Growth engineering of Propionibacterium freudenreichii shermanii for organic acids and other value-added products formation

Propionic acid production from glucose was studied using Propionibacterium freudenreichii shermanii. Conditions were optimized for high yields of propionic acid and total organic acids by sequential optimization of parameters like pH, inoculum age, inoculum volume and substrate concentration. Near-theoretical yield (0.54?±?0.023?g/g) was achieved for propionic acid with fermentation of 1% glucose using 20% (v/v) of 48?hr old P. shermanii at 30°C, pH maintained at 5.5. Total organic acid yield under these conditions was 0.74?±?0.06?g/g. The study resulted in achieving 98% and 95% theoretical yields of propionic acid and total organic acids, respectively. Under optimized conditions, along with organic acids, P. shermanii also produced vitamin B12 and trehalose intracellularly, showing its potential to be used as a cell factory.     

Propionic acid fermentation of lactose by Propionibacterium acidipropionici: effects of pH

Batch propionic acid fermentation of lactose by Propionibacterium acidipropionici were studied at various pH values ranging from 4.5 to 7.12. The optimum pH range for cell growth was between 6.0 and 7.1, where the specific growth rate was approximately 0.23 h(-1). The specific growth rate decreased with the pH in the acids have been identified as the two major fermentation products from lactose. The production of propionic acid was both growth and nongrowth associated, while acetic acid formation was closely associated with cell growth. The propionic acid yield increased with decreasing pH; It changed from approximately 33% (w/w) at pH 6.1-7.1 to approximately 63% at pH 4.5-5.0. In contrast, the acetic acid yield was not significantly affected by the pH; it remained within the range of 9%-12% at all pH values. Significant amounts of succinic and pyruvic acids were also formed during propionic acid fermentation of lactose. However, pyruvic acid was reconsumed and disappeared toward the end of the fermentation. The succinic acid yield generally decreased with the pH, from a high value of 17% at pH 7.0 to a low 8% at pH 5.0 Effects of growth nutrients present in yeast ex-tract on the fermentation were also studied. In general, the same trend of pH effects was found for fermentations with media containing 5 to 10 g/L yeast extract. However, More growth nutrients would be required for fermentations to be carried out efficienytly at acidic pH levels.     

Survival of a Salmonella typhimurium poultry isolate in the presence of propionic acid under aerobic and anaerobic conditions

Propionic acid is commonly found as a fermentation product in the gastrointestinal tracts of food animals and has also been used to limit the microbial contaminants in animal feeds. Because propionic acid is known to have antibacterial activity, the propionic acid encountered by foodborne pathogens during their life cycles may play an important role in inhibiting the survival of the pathogens. The survival patterns of Salmonella typhimurium poultry isolate were determined both in aerobic and anaerobic tryptic soy broth (TSB; pH 5.0 or 7.0) containing various concentrations of propionic acid (0-200 mM). The levels of recovered cells were consistently greater at pH 7.0 compared to those at pH 5.0. For the first 4 days, the levels were significantly decreased by incubation under anaerobic conditions as compared to aerobic condition at pH 7.0 (P<0.05). However, there were fluctuations of cell populations with different patterns depending on both concentrations and growth conditions. To characterize the nature of the capability which allowed the cell multiplication following decreases in cell population during incubation at pH 7.0, the cells isolated from the outgrowth cultures were tested for survival in aerobic or anaerobic TSB (pH 5.0 or pH 7.0) containing propionic acid (50 mM). The outgrowth isolates did not show significant differences in the level of recovered cells in the presence of propionic acid when compared to the wild type strain (P>0.05), suggesting that the cells in the outgrowth cultures did not harbour mutation(s) conferring increased resistance to propionic acid. In addition, the level of recovered cells of isogenic rpoS mutant strain of S. typhimurium was not significantly different from that of the wild type strain in the same assay conditions (P<0.05). The results of this study show that the bactericidal activity of propionic acid on S. typhimurium can be affected by environmental conditions such as acidic pH levels and anaerobiosis in food materials and gastrointestinal tracts. However, S. typhimurium is also able to multiply in the presence of sublethal concentrations of propionic acid at neutral pH during prolonged incubation under both aerobic and anaerobic conditions.