仙人掌复合保健饮料的工艺试验

以仙人掌、牛奶、麦芽为原料,采用酵母菌和乳酸菌共同发酵研制成含低醇的麦芽仙人掌乳酸饮料。通过实验确定了发酵的最佳工艺条件及饮料的最佳配方,并对饮料的稳定性进行了探讨,从而生产出酸甜可口、均一稳定的营养保健型乳酸饮料。     

玉米发酵面团工艺优化研究

通过单因素试验和正交试验确定了玉米发酵面团最佳制作工艺,并采用感官评价和质构特性对玉米发酵面团品质进行分析,得出酵母添加量0.8%、发酵时间为1.5h、醒发时间为40min条件下制得的玉米发酵面团硬度5 967.618、弹性809、黏聚性772、咀嚼性3 728.860、回复性354,品质良好。研究结果可为玉米主食化加工奠定良好的基础,间接推动玉米产业发展。     

玉米青贮过程中乳酸菌动态变化

为了揭示青贮玉米在发酵过程中乳酸菌数量及种群的动态变化,以及微生物添加剂对乳酸菌种群变化的影响,采用了培养方法计数发酵过程中乳酸菌数目的变化,利用16S rRNA基因序列比对方法分析青贮玉米中乳酸菌的多样性及种群变化趋势。经过对15d时间内青贮玉米中乳酸菌变化趋势的分析显示:一周后对照组乳酸菌数最高达到2.1×106CFU/g,两处理组中处理组Ⅱ乳酸菌数达到最高5.5×107CFU/g;利用MRS平板分离、培养出典型乳酸菌菌落152株,经16S rRNA基因序列比对分析为乳杆菌属和片球菌属,其中86%的菌株属于乳杆菌属。此研究表明微生物添加剂有利于青贮玉米发酵过程中乳酸菌的快速增殖,乳杆菌属和片球菌属都是青贮玉米发酵的启动菌之一,在发酵前期一直存在,但发酵后期乳杆菌属是玉米青贮过程中乳酸菌的主要菌群。     

酵母发酵玉米秸秆水解液产麦角甾醇应用研究

生物质是一种可再生资源,生物质发酵可产生高端化工产品.本文主要探讨蒸汽爆破处理玉米秸秆及水解可发酵单糖,考察酵母发酵玉米秸秆糖化液产麦角甾醇的应用研究.实验结果表明:当固液比10%,盐酸浓度1.5%,90℃水解反应3 h,还原糖含量达到53.3%,纤维素转化率79%.发酵工艺参数为玉米秸秆糖化液6.0°Bx,玉米浆4%,pH 7.5,接种量10%,28℃摇床振荡培养32 h,细胞生物量达8.5 g/L,麦角甾醇含量可达2.35%.同时对玉米秸秆发酵产麦角甾醇晶体进行结构表征.     

玉米黄浆水在丙酮-丁醇厌氧梭菌发酵中的应用

为降低丙酮-丁醇厌氧梭菌发酵生产丁醇的成本,研究了不同添加量玉米黄浆水对发酵的影响。与葡萄糖培养基相比,在发酵培养基中添加少量玉米黄浆水对发酵产量无显著影响。当添加体积分数为25％的玉米黄浆水时,丙酮、丁醇和乙醇的最终质量浓度分别是0．31、2．70和8．00g/L,总溶剂量为11．01g／L。通过成本核算,每生产1kg溶剂,添加体积分数25％的玉米黄浆水可比葡萄糖培养基节约成本2．11元。     

木薯和玉米原料丁醇发酵中丁醇丙酮质量比的图论理论计算及其验证

在丁醇发酵产溶剂阶段,乙酸和丁酸的生成途径、消耗途径同时存在,各自形成一个闭环路径。本研究利用图论对丁醇发酵中丁醇丙酮质量比进行了理论计算,并对以木薯和玉米为原料的丁醇发酵进行了模拟计算,结果表明:丁酸闭环路径(L2环)的代谢强度是影响丁醇丙酮质量比的主要因素,并且L2环的代谢强度越弱,丁醇丙酮质量比越高;与玉米原料丁醇发酵相比,木薯原料发酵的m(丁醇)/m(丙酮)提高了16.7%。实验结果证实了以上计算结果:在传统发酵、油醇萃取发酵和生物柴油萃取发酵中,以木薯(适时添加酵母浸粉)为原料的发酵批次与以玉米为原料的发酵批次相比,由于其丁酸闭环路径代谢强度较弱,相应发酵方式下丁醇丙酮质量比分别提高了12.9%、61.4%和6.7%,而且两种原料相应发酵方式的丁醇总产量和生产效率基本持平。另外,高丁醇丙酮质量比的木薯发酵所得改良型生物柴油中丁醇浓度与玉米发酵的相比提高了16%,性能得到进一步提高。     

不同培养料和发酵次数栽培巴氏菇比较

分别以玉米秸秆和稻草为培养料栽培巴氏菇,对菌丝生长性状进行对比;同时,在我国传统发酵栽培方法的基础上,将三次发酵法与二次发酵法进行了对比。试验结果表明:利用玉米秸秆栽培的巴氏菇在发菌速度及子实体质量和产量上均优于稻草;培养料经过3次发酵更适宜巴氏菇生长。经过3次发酵的玉米秸秆培养料栽培的巴氏菇产量和生物学效率分别为7.7 kg/m2和27.5%,子实体粗蛋白含量44.89%,可溶性糖含量44.01%,18种氨基酸总量31.70%,明显高于2次发酵的玉米秸秆培养料及2次、3次发酵的稻草培养料。     

白星花金龟幼虫对酵化玉米秸秆取食效果的研究

为探寻玉米秸秆资源化利用新途径、提高玉米秸秆利用效益,本研究利用白星花金龟Protaetia brevitaris Lewis幼虫的腐食性行为,选择其3龄幼虫,用EM菌液发酵玉米秸秆,以每5 d取食量为评价指标,选出幼虫取食的玉米秸秆最佳发酵时间及取食温度;以玉米秸秆发酵饲料为对照,以筛选出牛粪添加量分别为20%、60%的两组发酵饲料为处理,研究了白星花金龟幼虫对发酵饲料的利用率、转化率、消化率以及发酵饲料对白星花金龟幼虫死亡率、生物量增长率的影响。结果表明玉米秸秆发酵时间为25 d,温度为28℃时白星花金龟幼虫取食量最大;白星花金龟幼对玉米秸秆的转化率达到63.82%±30.90%,消化率为22.75%±3.07%,利用率为17.51%±8.50%,显著高于添加的组合;取食玉米秸秆发酵料的白星花金龟幼虫死亡率为5.75%±5.75%,生物量增长率达到11.01%±5.25%,均显著优于牛粪添加的玉米秸秆发酵料;添加牛粪可显著提高白星花金龟幼虫对玉米秸秆发酵饲料的取食量及虫粪产量,可利用白星花金龟3龄幼虫对玉米秸秆进行资源化利用,具有较好的应用前景。     

小麦和玉米原料生产柠檬酸工艺研究

利用小麦和玉米为生产原料生产柠檬酸。研究黑曲霉菌种对碳源的适应性、发酵过程中氮源比例,无机盐成分和添加比例,发酵最适温度的确定。优化柠檬酸发酵培养基条件,提高柠檬酸发酵代谢水平。     

萃取耦合技术对玉米秸秆水解液发酵产丁醇的影响

本研究以玉米秸秆水解液为原料,通过萃取发酵技术生产燃料丁醇,以提高丁醇产量,降低生产成本。通过对萃取剂的筛选与条件优化,确定纤维丁醇发酵的萃取剂为油醇,添加时间为发酵0 h,添加比例为1:1 (V/V)。该条件下发酵32 g/L糖浓度的玉米秸秆水解液,丁醇和总溶剂产量分别为3.28 g/L和4.72 g/L,比对照分别提高958.1%和742.9%。以D301树脂脱毒后5%总糖浓度的玉米秸秆水解液进行丁醇萃取发酵,丁醇和总溶剂产量分别达到10.34 g/L和14.72 g/L,发酵得率为0.31 g/g,与混合糖发酵结果相当。研究结果表明萃取发酵技术能够显著提高原料的利用率和丁醇产量,为纤维丁醇工业化生产提供了技术支撑。     

Production of bakers' yeast in cheese whey ultrafiltrate

A process for the production of bakers' yeast in whey ultrafiltrate (WU) is described. Lactose in WU was converted to lactic acid and galactose by fermentation. Streptococcus thermophilus was selected for this purpose. Preculturing of S. thermophilus in skim milk considerably reduced its lag. Lactic fermentation in 2.3x-concentrated WU was delayed compared with that in unconcentrated whey, and fermentation could not be completed within 60 h. The growth rate of bakers' yeast in fermented WU differed among strains. The rate of galactose utilization was similar for all strains, but differences in lactic acid utilization occurred. Optimal pH ranges for galactose and lactic acid utilization were 5.5 to 6.0 and 5.0 to 5.5, respectively. The addition of 4 g of corn steep liquor per liter to fermented WU increased cell yields. Two sources of nitrogen were available for growth of Saccharomyces cerevisiae: amino acids (corn steep liquor) and ammonium (added during the lactic acid fermentation). Ammonium was mostly assimilated during growth on lactic acid. This process could permit the substitution of molasses by WU for the industrial production of bakers' yeast.     

Fermentation of swine waste-corn mixtures for animal feed: Pilot-plant studies

Summary Aerobic culture with solid substrates of fresh swine waste combined with corn resulted in lactic acid fermentation with odor control. Heterofermentative lactic acid bacteria produced lactic and homologous tatty acids from acetic through valeric acid (0.1 meq/dry g) to reduce pH 2 units to 4.2 to 4.6. During the fermentation, lactic acid organisms increased from 10⁷ to 10⁹/dry g. Coliform organisms remained steady in number at 10⁶ organisms/dry g. Pilot-plant scale fermentation produced a product with 21 to 39% more methionine than corn but was still limiting for this amino acid as well as lysine for young pigs. Fermentation product from fresh waste-corn cultures was fed as the major dietary component to young pigs, hens, and sheep. Pigs showed gain and gain/feed diminished by one-third in 13-day trials. Laying hens performed comparably to controls in a 21-day test, and sheep did not discriminate against fermentation product.     

Production of Bakers' Yeast in Cheese Whey Ultrafiltrate

A process for the production of bakers' yeast in whey ultrafiltrate (WU) is described. Lactose in WU was converted to lactic acid and galactose by fermentation. Streptococcus thermophilus was selected for this purpose. Preculturing of S. thermophilus in skim milk considerably reduced its lag. Lactic fermentation in 2.3×-concentrated WU was delayed compared with that in unconcentrated whey, and fermentation could not be completed within 60 h. The growth rate of bakers' yeast in fermented WU differed among strains. The rate of galactose utilization was similar for all strains, but differences in lactic acid utilization occurred. Optimal pH ranges for galactose and lactic acid utilization were 5.5 to 6.0 and 5.0 to 5.5, respectively. The addition of 4 g of corn steep liquor per liter to fermented WU increased cell yields. Two sources of nitrogen were available for growth of Saccharomyces cerevisiae: amino acids (corn steep liquor) and ammonium (added during the lactic acid fermentation). Ammonium was mostly assimilated during growth on lactic acid. This process could permit the substitution of molasses by WU for the industrial production of bakers' yeast.     

利用固定化米根霉在三相流化床中发酵生成L-乳酸

用聚氨酯泡沫吸附固定米根霉菌丝,在三相流化床中对葡萄糖、木糖以及木糖渣的纤维素酶解液等不同碳源进行Ｌ－乳酸发酵研究,并对游离菌丝和固定化菌丝发酵Ｌ－乳酸进行了比较。结果表明,聚氨酯泡沫是米根霉的良好载体,具有经济、高效等特点。实验条件下,不同碳源的乳酸转化率分别为：葡萄糖,８２．５％;木糖,５３．８％;木糖渣酶水解液,７１．９％。三相流化床中固定化米根霉产酸速率（对葡萄糖）为１９．１ｇ．ｈ＾－１．     

Lactic acid production from corn stover using mixed cultures of Lactobacillus rhamnosus and Lactobacillus brevis

Mixed cultures of Lactobacillus rhamnosus and Lactobacillus brevis was studied for improving utilization of both cellulose- and hemicellulose-derived sugars from corn stover for lactic acid production. During simultaneous saccharification and fermentation (SSF) of NaOH-treated corn stover by the mixed cultures, a lactic acid yield of 0.70 g/g was obtained, which was about 18.6% and 29.6% higher than that by single cultures of L. rhamnosus and L. brevis, respectively. Our results indicated that lactic acid yield from NaOH-pretreated corn stover by mixed cultures of L. rhamnosus and L. brevis was comparable to that from pure sugar mixtures (0.73 g/g of glucose/xylose mixture at 3:1 w/w).     

Simultaneous saccharification and fermentation of ground corn stover for the production of fuel ethanol using Phanerochaete chrysosporium, Gloeophyllum trabeum, Saccharomyces cerevisiae, and Escherichia coli K011

Enzymatic saccharification of corn stover using Phanerochaete chrysosporium and Gloeophyllum trabeum and subsequent fermentation of the saccharification products to ethanol by Saccharomyces cerevisiae and Escherichia coli K011 were achieved. Prior to simultaneous saccharification and fermentation (SSF) for ethanol production, solid-state fermentation was performed for four days on ground corn stover using either P. chrysosporium or G. trabeum to induce in situ cellulase production. During SSF with S. cerevisiae or E. coli, ethanol production was the highest on day 4 for all samples. For corn stover treated with P. chrysosporium, the conversion to ethanol was 2.29 g/100 g corn stover with S. cerevisiae as the fermenting organism, whereas for the sample inoculated with E. coli K011, the ethanol production was 4.14 g/100 g corn stover. Corn stover treated with G. trabeum showed a conversion 1.90 and 4.79 g/100 g corn stover with S. cerevisiae and E. coli K011 as the fermenting organisms, respectively. Other fermentation co-products, such as acetic acid and lactic acid, were also monitored. Acetic acid production ranged between 0.45 and 0.78 g/100 g corn stover, while no lactic acid production was detected throughout the 5 days of SSF. The results of our experiment suggest that it is possible to perform SSF of corn stover using P. chrysosporium, G. trabeum, S. cerevisiae and E. coli K011 for the production of fuel ethanol.     

Production of lactic acid and fungal biomass by Rhizopus fungi from food processing waste streams

This study proposed a novel waste utilization bioprocess for production of lactic acid and fungal biomass from waste streams by fungal species of Rhizopus arrhizus 36017 and R. oryzae 2062. The lactic acid and fungal biomass were produced in a single-stage simultaneous saccharification and fermentation process using potato, corn, wheat and pineapple waste streams as production media. R. arrhizus 36017 gave a high lactic acid yield up to 0.94-0.97 g/g of starch or sugars associated with 4-5 g/l of fungal biomass produced, while 17-19 g/l fungal biomass with a lactic acid yield of 0.65-0.76 g/g was produced by the R. oryzae 2062 in 36-48 h fermentation. Supplementation of 2 g/l of ammonium sulfate, yeast extract and peptone stimulated an increase in 8-15% lactic acid yield and 10-20% fungal biomass.     

Kinetics of direct fermentation of agricultural commodities to L(+) lactic acid byRhizopus oryzae

Summary The kinetics of fermenting barley, cassava, corn, oats, and rice directly to L(+) lactic acid byRhizopus oryzae NRRL 395 were determined. The rates of carbohydrate consumption and L(+) lactic acid production were found to be influenced by the type of substrate, the substrate concentration, the fermentation temperature, and the presence of a neutralizing agent.     

Production of mannitol and lactic acid by fermentation with Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius B-3693 was selected as a good producer of mannitol from fructose after screening 72 bacterial strains. The bacterium produced mannitol, lactic acid, and acetic acid from fructose in pH-controlled batch fermentation. Typical yields of mannitol, lactic acid, and acetic acid from 250 g/L fructose were 0.70, 0.16, and 0.12 g, respectively per g of fructose. The fermentation time was greatly dependent on fructose concentration but the product yields were not dependent on fructose level. Fed-batch fermentation decreased the time of maximum mannitol production from fructose (300 g/L) from 136 to 92 h. One-third of fructose could be replaced with glucose, maltose, galactose, mannose, raffinose, or starch with glucoamylase (simultaneous saccharification and fermentation), and two-thirds of fructose could be replaced with sucrose. L. intermedius B-3693 did not co-utilize lactose, cellobiose, glycerol, or xylose with fructose. It produced lactic acid and ethanol but no acetic acid from glucose. The bacterium produced 21.3 +/- 0.6 g lactic acid, 10.5 +/- 0.3 g acetic acid, and 4.7 +/- 0.0 g ethanol per L of fermentation broth from dilute acid (15% solids, 0.5% H(2)SO(4), 121 degrees C, 1 h) pretreated enzyme (cellulase, beta-glucosidase) saccharified corn fiber hydrolyzate.     

Characteristics of aerobic,solid substrate fermentation of swine waste-corn mixtures

Summary Aerobic fermentation of swine waste combined with corn produced differences in microbial and biochemical patterns dependent on use of fresh or stored excrement. Lactic acid fermentation and odor control resulted with either waste. Homofermentative lactic acid bacteria were present initially at 10⁷ organisms/dry g with stored waste-corn cultures and total microflora amounted to 10⁸ organisms/dry g. Fresh waste-corn fermentations initially yielded heterofermentative lactic acid bacteria at 10⁷ organisms/dry g and total viable population was 10⁹ organisms/dry g. These respective groups of lactic acid bacteria dominated from 12 through 144 h in cultures with either waste, and acid production (0.2 meq/dry g) decreased pH by 2 units to 4.5. The major acid component with stored waste-corn was lactic acid, whereas fresh waste-corn fermentation produced both lactic and homologous fatty acids from acetic through valeric acid. Coliform bacteria present initially at 10⁵ organisms/dry g in stored waste-corn cultures were not detected after 36 h; coliform bacteria in fresh waste-corn fermentations persisted at 10⁶ organisms/dry g. A silage-like fermentation product resulted which may have use in animal feed formulations.