固定化红曲葡萄糖母液流加发酵红曲色素的研究

对固定化红曲(Monascus purpureus)，在生物反应器中流加葡萄糖母液发酵生产红曲色素进行了研究，建立了简单的数学模型控制流加。结果表明：当总葡萄糖母液浓度为150g/L时，以90g/L初始葡萄糖母液开始发酵，当流加因子K=0．0013时，变速流加发酵组的色素浓度比非流加发酵组的色价提高32％。     

利用葡萄糖母液生产红曲色素的研究

对红曲霉（Monascuspurpureus）以葡萄糖母液为原料,在生物反应器中流加发酵生产红曲色素进行了研究,建立了简单的数学模型控制流加。结果表明：当总葡萄糖母液浓度为150g／L时,以90g／L初始葡萄糖母液开始发酵,当流加因子K为0．0013时,变速流加发酵组的色素浓度比非流加发酵组的色价增加32％。     

流加混合碳源的谷氨酸发酵工艺研究

采用糖蜜与葡萄糖的混合液作为流加碳源，对谷氨酸发酵工艺进行了探索。试验采用葡萄糖为基础碳源，以发酵初糖浓度为160g／L的培养基进行谷氨酸发酵，以糖蜜与葡萄糖的混合液为流加碳源，结果表明当糖蜜中还原糖占混合液总还原糖30％时，发酵产酸水平和糖酸转化率分别达到142.2g／L和64．88％，与葡萄糖作为唯一流加碳源的谷氨酸发酵工艺比较，其发酵水平十分相近。但生产谷氨酸的碳源成本可降低5％左右。     

赖氨酸发酵工业研究：赖氨酸流加发酵中氮源浓度的选择及控制模式

以黄我短杆菌（Ｂｒｅｖｉｂａｃｔｅｒｉｕｍｆｌａｖｕｍ）ＷＳＨＬ１为产生菌,了确定了２．５Ｌ罐赖氨酸流加发酵中氮源浓度的初始值及过程控制模式。首先分析了不同初始有机氮源浓度对赖氨酸流加发酵过程菌体生长,产物积累以及微生物稳定性的影响,并得到了适宜的初始有机氮源浓度为２０ｇ／Ｌ;在流加糖液中添加１０ｇ／Ｌ的有机氮源使发酵产酸和产物对耗糖转化率分别达到１０９．０ｇ／Ｌ和３８．５％。在分析ＰＨ值反馈控制     

赖氨酸发酵工业化研究

以黄色短杆菌（Brevibacterium flavum）WSH L1为产生菌,研究确定了2.5 L罐赖氨酸流加发酵中氮源浓度的初始值及过程控制模式。首先分析了不同初始有机氮源浓度对赖氨酸流加发酵过程菌体生长、产物积累以及微生物稳定性的影响,并得到适宜的初始有机氮源浓度为20g/L;在流加糖液中添加10g/L的有机氮源使发酵产酸和产物对耗糖转化率分别达到109.0g/L和38.5%。在分析pH值反馈控制铵离子浓度时的发酵液硫酸铵浓度变化过程的基础上,提出了葡萄糖浓度反馈控制铵离子浓度的基质流加模式。对铵离子浓度采取复合反馈控制方式后,发酵64 h,赖氨酸盐酸盐浓度和产物对葡萄糖的转化率分别达到119.0 g/L和40.2%。     

流加糖培养提高红曲色素发酵产量的研究

本文对流加糖发酵红曲色素进行了初步研究。结果表明：总糖浓度为５％时，以３％初糖开始发酵至４８小时、６０小时时，分别流加１％的糖。流加发酵组的色素浓度比非流加发酵组的色素浓度增加２３．５％。     

赖氨酸发酵工业化研究——赖氨酸流加发酵中氮源浓度的选择及控制模式

以黄色短杆菌(Brevibacteriumflavum)WSHL1为产生菌,研究确定了2.5L罐赖氨酸流加发酵中氮源浓度的初始值及过程控制模式。首先分析了不同初始有机氮源浓度对赖氨酸流加发酵过程菌体生长、产物积累以及微生物稳定性的影响,并得到适宜的初始有机氮源浓度为20g/L;在流加糖液中添加10g/L的有机氮源使发酵产酸和产物对耗糖转化率分别达到109.0g/L和38.5%。在分析pH值反馈控制铵离子浓度时的发酵液硫酸铵浓度变化过程的基础上,提出了葡萄糖浓度反馈控制铵离子浓度的基质流加模式。对铵离子浓度采取复合反馈控制方式后,发酵64h,赖氨酸盐酸盐浓度和产物对葡萄糖的转化率分别达到119.0g/L和40.2%。     

利用Crypthecodinium cohnii高密度发酵生产DHA的流加策略研究

利用流加策略实现了隐甲藻(Crypthecodinium cohnii)生产DHA的高密度发酵。根据隐甲藻间歇式发酵的特性,探讨最佳补料时间及流加液中最佳碳氮比,结果表明,在葡萄糖浓度降至4g/L左右时流加碳氮比为30∶1的营养液对隐甲藻的生长和脂肪酸积累最有利。根据以上结果,初始葡萄糖浓度25g/L,采用5d连续发酵多次流加策略,细胞干重达6.37%,DHA产量为4.08g/L。     

国内期刊文摘

清液补料酒精发酵工艺研究李永飞，吕欣，段作营，毛忠贵食品与发酵工业，２００２，（１２）：１７－１９．清液发酵具有醪液易输送，废液能大比例甚至“全循环”直接拌料，利于提高设备利用率、降低能耗等诸多优点。清液发酵的初始糖采用玉米粉糖化液进行发酵，初始糖浓度为１２％，采用３次补糖，分别在８h，１２h，２４h进行，补糖后糖浓度控制在１５％左右。在３２℃下发酵７２h，酒精体积分数可达１５％（２０℃）以上，残糖降至０．１以下，葡萄糖转化率达５０％，酒精得率９４％。（丹妮）０．１以下，葡萄糖转化率达５０％，酒精得…     

木薯淀粉高温高浓度生产酒精的工艺研究

对木薯淀粉高温高浓度生产酒精的三角瓶发酵条件进行了优化。在单因素实验的基础上,首先应用Plackett-Burman试验设计筛选影响酒精高温高浓度发酵的重要参数,利用最陡爬坡实验逼近最大酒精生产区域后,利用Box-Behnken设计确定重要参数的最佳水平。筛选结果表明,影响酒精产量的重要参数是糖化酶用量、肌醇浓度和初始淀粉浓度（料水比）。最佳工艺条件为糖化酶用量为0．27AGU／g淀粉、肌醇的添加量为0．065％、淀粉浓度为33．64％,在此条件下发酵48h,酒精浓度可达15．02％。优化条件与初始条件相比较,酒精浓度提高了25％。     

耐氨米根霉的分批补料发酵及发酵动力学初探

以氨水为中和剂,替代CaCO3,对耐氨米根霉R.oryzaeJS-N0-2-02进行15L自动发酵罐的分批和分批补料发酵及其发酵动力学的初步研究,结果表明,降低起始糖浓度,产酸期补糖可明显提高菌体L-乳酸比生产速率和耗糖产酸能力,提高L-乳酸产量和纯度,降低残糖。在发酵起始时添加1 g/L CaCO3能进一步提高补糖发酵的L-乳酸比生产速率,增强发酵后期菌体耗糖产酸能力,从而进一步提高L-乳酸产量和纯度,降低残糖。发酵结果:起始糖浓度为120 g/L,25h时补糖使最终发酵总糖浓度达137 g/L,发酵培养60 h,L-乳酸产量可达101.8 g/L,纯度97.3%,菌体耗糖转化率76%,比生产速率0.27 g/g.h,残糖降至3 g/L。     

利用微处理机控制的补料分批培养提高树状黄杆菌的细胞浓度和葡萄糖异构酶的活力

在实验室用16L发酵罐中采用树状黄杆菌进行以微机控制的分批培养和补料分批培养,结果发现树状黄杆菌细胞生长及葡萄糖异构酶的合成需要高水平溶解氧。当溶解氧由80％饱和度变为50％饱和度时,比细胞生长率由0.52/h下降到0.36/h,培养24小时后,细胞浓度和葡萄糖异构酶活力逐渐达到最高值,此后继续培养至48小时,溶氧水平下降到50％饱和度时,细胞浓度及酶活无明显变化,这很可能是由于培养初期细胞生长需要大量溶解氧之故。 与分批培养结果相比,树状黄杆菌的补料分批培养由于在发酵罐内适时添加了营养物质,而使细胞浓度提高了48.8％,酶活提高了47.1％。 这一实验结果可用于葡萄糖异构酶的工业化生产。     

Fed‐batch l‐(+)‐lactic acid fermentation of brewer's spent grain hydrolysate

Brewer's spent grain (BSG) hydrolysates were used for l ‐(+)‐lactic acid (LA) fermentation by Lactobacillus rhamnosus ATCC 7469. The aim of this study was to evaluate fed‐batch LA fermentation of BSG hydrolysate with the addition of glucose, glucose and yeast extract, and wort during LA fermentation and its effect on fermentation parameters such as LA concentration, its volumetric productivity and yield, and L. rhamnosus cell viability. The highest LA yield, volumetric productivity and concentration of 93.3%, 2.0 g/L/h, and 116.1 g/L, respectively, were achieved with glucose and yeast extract addition during fermentation. In fed‐batch fermentation with glucose and yeast extract addition significantly higher LA concentration, yield and volumetric productivity (by 194.8; 2.2, and 20.7%, respectively) were achieved compared with batch fermentation. The results indicated that fed‐batch fermentation could be used to increase LA fermentation efficiency. Copyright © 2017 The Institute of Brewing & Distilling     

High butanol production by Clostridium saccharoperbutylacetonicum N1-4 in fed-batch culture with pH-Stat continuous butyric acid and glucose feeding method

A pH-stat fed-batch culture by feeding butyric acid and glucose has been studied in an acetone-butanol-ethanol (ABE) fermentation using Clostridium saccharoperbutylacetonicum N1-4. The specific butanol production rate increased from 0.10 g-butanol/g-cells/h with no feeding of butyric acid to 0.42 g-butanol/g-cells/h with 5.0 g/l butyric acid. The pH value in broth decreases with butyric acid production during acidogenesis, and then butyric acid reutilization and butanol production result in a pH increase during solventogensis. The pH-stat fed-batch culture was performed to maintain a constant pH and butyric acid concentration in the culture broth, but feeding only butyric acid could not support butyric acid utilization and butanol production. Subsequently, when a mixture of butyric acid and glucose was fed, butyric acid was utilized and butanol was produced. To investigate the effect of the feeding ratio of butyric acid to glucose (B/G ratio), several B/G ratio solutions were fed. The maximum butanol production was 16 g/l and the residual glucose concentration in broth was very low at a B/G ratio of 1.4. Moreover, yields of butanol in relation to cell mass and glucose utilization were 54% and 72% higher in pH-stat fed-batch culture with butyric acid than that of conventional batch culture, respectively.     

碱性中和与补料分批高密度培养保加利亚乳杆菌的研究

本实验采用葡萄糖反馈抑制补料、调节发酵液pH 值、碱性中和与补料分批复合培养等方法对保加利亚乳杆菌高密度培养进行研究。研究表明,碱性中和与补料分批复合培养条件为：保加利亚乳杆菌培养18h 和26h 时,向培养液补加碳氮比为0.67 的补料液5ml,并且每隔1.5h 调节pH 值至6.5,培养36h,培养液中保加利亚乳杆菌菌体浓度最高达9.02 × 1011CFU/ml,菌体干重达14.266g/L。     

指数流加模型在乙醇气提发酵过程中的应用研究

通过实验选择并考核了一个指数流加模型 ,同时也对比地考察了均速流加方式的发酵效果。结果表明 ,指数流加相比匀速流加过程的细胞生物量平均浓度增加了 1 2 2倍 ,乙醇生产速率和糖消耗速率分别提高到 3 0 1 g/(h·L)和 6 2 1g/(h·L) ,是匀速流加时的 1 2倍和 1 1 9倍。研究表明 ,在乙醇气提发酵过程中 ,如果选用适当的指数流加模型 ,就能够消除发酵过程中底物和产物的双抑制作用 ,简单而有效地改进现有的在线分离乙醇的连续发酵工艺 ,提高乙醇生产速率     

拟无枝酸菌ST2710转化洛伐他汀为无锡他汀的发酵工艺的初步研究

无锡他汀是胆固醇合成途径中限速酶羟甲基戊二酰辅酶A(HMG-CoA)还原酶抑制剂,由洛伐他汀经拟无枝酸菌(Amycolatopsis sp.ST 2710)转化产生。文中在摇瓶水平考察了底物浓度、溶氧和剪切力等因素对洛伐他汀(底物)转化为无锡他汀(产物)的影响,并在5 L发酵罐上进行了分批发酵及材料分批发酵研究。摇瓶结果表明,菌株对溶氧要求较高,对剪切力很敏感,底物适宜添加浓度为1 g/L。在5 L发酵罐间歇发酵过程中。在控制溶氧不低于35%.搅拌转速为300r/min,产物产量达到最高,为0.77 g/L左右,发酵周期为80 h,较摇瓶发酵缩短16 h。采用补料发酵工艺后,有效减缓底物抑制,产物产量达到1.83 g/L。是分批发酵的2.4倍。     

Maximizing yellow pigment production in fed-batch culture of Monascus sp

Yellow pigment production in exponential fed-batch cultivation of Monascus sp. was studied. Due to the difficulty of measuring the optical density for accurate determination of the cell concentration, a capacitance probe was employed on-line. The feed rate needed to keep the specific growth rate, mu, constant in fed-batch culture was determined on the basis of the cell concentration measured by the capacitance probe. Control of mu was improved by using updated information on the cell concentration compared with the simple feed-forward determination method using the initial cell concentration only. The highest specific pigment production rate was achieved with a mu of 0.02 h(-1) in the feeding phase. However, among several fermentation examined, the largest pigment production in the final step was obtained at a mu of 0.01 h(-1); in each case the same amount of substrates was used. An investigation of the optimal initial glucose concentration revealed that pigment production was maximum when the initial glucose concentration in the batch mode was 10 g/l and mu was 0.01 h(-1) in the fed-batch mode. It was also found that the pellet weight in the fermentation could be accurately estimated by image analysis. The ratio of the mycelium weight to the total cell weight estimated from information on the total cell weight and the estimated pellet weight was found to be more than 80%. However, no clear quantitative relationship could be discerned between the specific pigment production rate, rho, and the ratio of mycelium in the cell population.