Production of ethanol from raw cassava starch by a nonconventional fermentation method

Raw cassava root starch was transformed into ethanol in a one-step process of fermentation, in which are combined the conventional processes of liquefaction, saccharification, and fermentation to alcohol. Aspergillus awamori NRRL 3112 and Aspergillus niger were cultivated on wheat bran and used as Koji enzymes. Commercial A. niger amyloglucosidase was also used in this experiment. A raw cassava root homogenate–enzymes–yeast mixture fermented optimally at pH 3.5 and 30°C, for five days and produced ethanol. Alcohol yields from raw cassava roots were between 82.3 and 99.6%. Fungal Koji enzymes effectively decreased the viscosity of cassava root fermentation mashes during incubation. Commercial A. niger amyloglucosidase decreased the viscosity slightly. Reduction of viscosity of fermentation mashes was 40, 84, and 93% by commercial amyloglucosidase, A. awamori, and A. niger enzymes, respectively. The reduction of viscosity of fermentation mashes is probably due to the hydrolysis of pentosans by Koji enzymes.     

Effect of polyphenol content on the hydrolysis and fermentation of grain sorghum starch

The high polyphenol content of birdproff grain sorghum has been associated with impaired nutritional quality of the grain and with reduced brewing value of birdproof grain sorghum malt due to enzyme inhibition. In this investigation, high polyphenol grain sorghum was evaluated as a feedstock for fermentation ethanol production using NaOH pretreatment to inactivate the polyphenolic compounds prior to hydrolysis with commercial amylases. The polyphenolic inhibition of starch hydrolysis was minimal at a grain sorghum slurry concentration of 20% dry solids, but became pronounced at slurry concentrations of 28% and higher. At these high slurry concentrations the liquefaction and subsequent saccharification and fermentation were markedly improved by alkaline pretreatment. The highest ethanol concentration (12·3%, vol/vol), coupled with the best starch conversion efficiency to ethanol (83·5%), was obtained with a 28% grain sorghum slurry using a partial simultaneous saccharification and fermentation procedure. The residual fermented solids had a crude protein content of 45·4%. Tannic acid decreased yeast cell viability in synthetic media, but had no effect on the hydrolysis or fermentation of grain sorghum starch.     

The enzymatic hydrolysis and fermentation of pretreated wheat straw to ethanol

Autohydrolysis and ethanol-alkali pulping were used as pretreatment methods of wheat straw for its subsequent saccharification by Trichoderma reesei cellulase. The basic hydrolysis parameters, i.e., reaction time, pH, temperature, and enzyme and substrate concentration, were optimized to maximize sugar yields from ethanol-alkali modified straw. Thus, a 93% conversion of 2.5% straw material to sugar syrup containing 73% glucose was reached in 48 h using 40 filter paper units/g hydrolyzed substrate. The pretreated wheat straw was then fermented to ethanol at 43 degrees C in the simultaneous saccharification and fermentation (SSF) process using T. reesei cellulase and Kluyveromyces fragilis cells. From 10% (w/v) of chemically treated straw (dry matter), 2.4% (w/v) ethanol was obtained after 48 h. When the T. reesei cellulase system was supplemented with beta-glucosidase from Aspergillus niger, the ethanol yield in the SSF process increased to 3% (w/v) and the reaction time was shortened to 24 h.     

Production of ethanol from extruded corn starch by a nonconvencional fermentation method

Summary In single-step 48-hour fermentations of extruded, liquefied and raw corn starch, the yields of ethanol from extruded starch were similar to those from liquefied starch, whereas the yields of ethanol from raw starch were lower.     

Production of fuel ethanol from bamboo by concentrated sulfuric acid hydrolysis followed by continuous ethanol fermentation

An efficient process for the production of fuel ethanol from bamboo that consisted of hydrolysis with concentrated sulfuric acid, removal of color compounds, separation of acid and sugar, hydrolysis of oligosaccharides and subsequent continuous ethanol fermentation was developed. The highest sugar recovery efficiency was 81.6% when concentrated sulfuric acid hydrolysis was carried out under the optimum conditions. Continuous separation of acid from the saccharified liquid after removal of color compounds with activated carbon was conducted using an improved simulated moving bed (ISMB) system, and 98.4% of sugar and 90.5% of acid were recovered. After oligosaccharide hydrolysis and pH adjustment, the unsterilized saccharified liquid was subjected to continuous ethanol fermentation using Saccharomycescerevisiae strain KF-7. The ethanol concentration, the fermentation yield based on glucose and the ethanol productivity were approximately 27.2 g/l, 92.0% and 8.2 g/l/h, respectively. These results suggest that the process is effective for production of fuel ethanol from bamboo.     

Solid-state fermentation of sweet sorghum to ethanol

Solid-state fermentation of chopped sweet sorghum particles to ethanol was studied in static flasks using an ethanol tolerant yeast strain. The influence of various process parameters, such as temperature, yeast cell concentration, and moisture content, on the rate and extent of ethanol fermentation was investigated. Optimal values of these parameters were found to be 35 degrees C, 7 x 10(8) cells/g raw sorghum, and 70% moisture level, respectively.     

Enzyme hydrolysis and ethanol fermentation of liquid hot water and AFEX pretreated distillers' grains at high-solids loadings

The dry milling ethanol industry produces distiller's grains as major co-products, which are composed of unhydrolyzed and unfermented polymeric sugars. Utilization of the distiller's grains as an additional source of fermentable sugars has the potential to increase overall ethanol yields in current dry grind processes. In this study, controlled pH liquid hot water pretreatment (LHW) and ammonia fiber expansion (AFEX) treatment have been applied to enhance enzymatic digestibility of the distiller's grains. Both pretreatment methods significantly increased the hydrolysis rate of distiller's dried grains with solubles (DDGS) over unpretreated material, resulting in 90% cellulose conversion to glucose within 24h of hydrolysis at an enzyme loading of 15FPU cellulase and 40 IU beta-glucosidase per gram of glucan and a solids loading of 5% DDGS. Hydrolysis of the pretreated wet distiller's grains at 13-15% (wt of dry distiller's grains per wt of total mixture) solids loading at the same enzyme reduced cellulose conversion to 70% and increased conversion time to 72h for both LHW and AFEX pretreatments. However, when the cellulase was supplemented with xylanase and feruloyl esterase, the pretreated wet distiller's grains at 15% or 20% solids (w/w) gave 80% glucose and 50% xylose yields. The rationale for supplementation of cellulases with non-cellulolytic enzymes is given by Dien et al., later in this journal volume. Fermentation of the hydrolyzed wet distiller's grains by glucose fermenting Saccharomyces cerevisiae ATCC 4124 strain resulted in 100% theoretical ethanol yields for both LHW and AFEX pretreated wet distiller's grains. The solids remaining after fermentation had significantly higher protein content and are representative of a protein-enhanced wet DG that would result in enhanced DDGS. Enhanced DDGS refers to the solid product of a modified dry grind process in which the distiller's grains are recycled and processed further to extract the unutilized polymeric sugars. Compositional changes of the laboratory generated enhanced DDGS are also presented and discussed.     

Bioconversion of wheat straw to ethanol: Chemical modification,enzymatic hydrolysis,and fermentation

Native wheat straw (WS) was pretreated with various concentrations of H₂SO₄ and NaOH followed by secondary treatments with ethylene diamine (EDA) and NH₄OH prior to enzymatic saccharification. Conversion of the cellulosic component to sugar varied with the chemical modification steps. Treatment solely with alkali yield 51–75% conversion, depending on temperature. Acid treatment at elevated tempeatures showed a substantial decrease in the hemicellulose component, whereas EDA-treated WS (acid pretreated) showed a 69–75% decrease in the lignin component. Acid-pretreated EDA-treated straw yielded a 98% conversion rate, followed by 83% for alkali–NH₄OH treated straws. In other experiments, WS was pretreated with varying concentration of H₂SO₄ or NaOh followed by NH₄OH treatment prior to enzymatic hydrolysis. Pretreatment of straw with 2% NaOH for 4 h coupled to enzymatic hydrolysis yield a 76% conversion of the cellulosic component. Acid–base combination pretreatment yielded only 43% conversions. A reactor column was subsequently used to measure modification–saccharification–fermentation for wheat straw conversion on a larger scale. Thirty percent conversions of wheat straw cellulosics to sugar were observed with subsequent fermentation to alcohol. The crude cellulase preparation yielded considerable quantities of xylose in addition to the glucose. Saccharified materials were fermented directly with actively proliferating proliferating yeast cells without concentration of the sugars.     

Pretreatment of starch raw materials and their enzymatic hydrolysis by immobilized glucoamylase

The pretreatment of starch raw materials such as sweet potato, potato and cassava has been carried out using various types of crusher, viz juice mixer, homogenizer and high-speed planetary mill. The effect of pretreatment of the materials on their enzymatic hydrolysis was studied. High-speed planetary mill treatment was the most effective and comparable with heat treatment (pasting). Various crushing times were used to examine the effect of crushing by mill treatment on the enzymatic hydrolysis. In the enzymatic hydrolysis of cassava, the use of both cellulase [1,4-(1,3; 1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4] and glucoamylase [1,4-α-d-glucan glucohydrolase, EC 3.2.1.3] enhanced the d-glucose yield. The immobilization of glucoamylase was studied by radiation polymerization of hydrophilic monomers at low temperature, and it was found that enzymatic activity of the immobilized glucoamylase particles varied with monomer concentration and particle size. Starchy raw materials pretreated with the mill can be efficiently hydrolysed by immobilized glucoamylase.     

Production of an amylase-degrading raw starch by Gibberella pulicaris

An endophytic fungus, Gibberella pulicaris, produced an amylase which degraded raw starches from cereals and other crops including raw potato, sago, tapioca, corn, wheat and rice starch. In each case, glucose was the main product. Among the raw starches used, raw potato starch gave the highest enzyme activity (85 units mg^–1 protein) and raw wheat starch the lowest (49 units mg^–1 protein). The highest amylase production (260 units mg^–1 protein) was achieved when the concentration of raw potato starch was increased to 60 g l^–1. Optimum hydrolysis was at 40°C and pH 5.5.     

Alcoholic fermentation of raw cassava starch by Rhizopus koji without cooking

Using only wheat bran koji from the Rhizopus strain, raw cassava starch and cassava pellets converted reasonably well to alcohol (ethanol) without cooking at 35 degrees C and pH 4.5-5.0. When the initial broth contained 30 g raw cassava starch, 10 g Rhizopus sp. koji, and 100 mL tap water, 12.1 g of alcohol was recovered by final distillation from fermented broth. In this case, 12.1 g alcohol corresponds to an 85.5% conversion rate based on the theoretical values of the starch content. When the initial broth contained 40 g cassava starch, 14.1 g of alcohol was recovered, where 14.1 g corresponds to a 74.5% conversion rate. The alcoholic fermentation process described in the present work is considered more effective and reasonable than the process using raw starch without cooking reported until now, since the new process makes it unnecessary to add yeast cells and glucoamylase preparation.     

小麦淀粉废水发酵生产丁醇

为降低丁醇发酵的生产成本,以工业废弃物小麦淀粉废水为辅料,在分析废水组成的基础之上补加适当营养成分发酵生产丁醇。选取对丁醇发酵影响最大的木薯浓度、N源种类、N源浓度、无机盐和原料处理方式等因素分别进行考察。结果表明:对于低浓度废水,添加70 g/L木薯、2 g/L酵母粉、1 g/L K2HPO4,原料糊化水解,能够获得较好的摇瓶发酵效果,丁醇和总溶剂产量最高可分别达到14.72和22.65 g/L。在7 L发酵罐水平上,丁醇和总溶剂产量也分别能达到13.51和23.13 g/L。最终,利用生物柴油进行萃取发酵,其溶剂水平得到进一步提高,丁醇和总溶剂产量可分别达到15.13和29.38 g/L。     

Ethanol production from raw starch by simultaneous fermentation using Schizosaccharomyces pombe and a raw starch saccharifying enzyme from Corticium rolfsii

Alcoholic fermentation from raw corn starch using Schizosaccharomyces pombe AHU 3179 and a raw starch saccharifying enzyme (RSSE) from Corticium rolfsii AHU 9627 was investigated. The optimum ethanol production was achieved at pH 3.5, 27°C and under the yeast cell concentration of 2.7 × 10⁹ cells/ml. Addition of RSSE 5 units (as glucoamylase)/g raw corn starch was found sufficient. Under these optimum conditions, 18.5% (v/v, at 15°C) ethanol was obtained from 30% raw corn starch (30.8% as glucose) after incubation for 48 h.     

Amylolysis of raw corn by Aspergillus niger for simultaneous ethanol fermentation

The novelty of this approach was hydrolysis of the raw starch in ground corn to fermentable sugars that are simultaneously fermented to ethanol by yeast in a non-sterile environment. Thus, the conventional cooking step can be eliminated for energy conservation. A koji of Aspergillus niger grown on whole corn for 3 days was the crude enzyme source. A ratio of 0.2 g dry koji/g total solids was found sufficient. Optimum pH was 4.2. Ethanol concentration was 7.7% (w/w) in the aqueous phase with 92% raw starch conversion. Agitation increased rate. Sacharification was the rate-limiting step. The initial ethanol concentration preventing fermentation was estimated to be 8.3% by weight.     

Production of ethanol by coupling fermentation and solvent extraction

Summary A new technology of fermentation is proposed. The inhibitor product is removed continuously by coupling fermentation and solvent extraction. Applied to ethanol fermentation this technology is suitable to any case where the terminal product is inhibitory.The proposed technology uses both plug flow reactor and liquid-liquid extraction to achieve continuously the extractive fermentation of ethanol. The solvent used for liquid-liquid extraction is dodecanol. A new reactor was used. It is a column packed with a porous material . The fermentation broth is pulsed (a) to increase the interfacial area between the liquid medium and the dodecanol, and (b) to: decrease the gas hold up.Alcoholic fermentations were performed on glucose syrup at 35°C using Saccharomyces cerevisiae, with adsorbed cells as reference, with adsorbed cells and extractive fermentation. The results show that the fermentation is substantially improved. By this new method the ethanol productivity was multiplied by 5 and a solution of 407 g/l of glucose was totally fermented with a yeast which cannot normally transform more than 200 g/l glucose.     

Direct production of ethanol from raw corn starch via fermentation by use of a novel surface-engineered yeast strain codisplaying glucoamylase and alpha-amylase

Direct and efficient production of ethanol by fermentation from raw corn starch was achieved by using the yeast Saccharomyces cerevisiae codisplaying Rhizopus oryzae glucoamylase and Streptococcus bovis alpha-amylase by using the C-terminal-half region of alpha-agglutinin and the flocculation functional domain of Flo1p as the respective anchor proteins. In 72-h fermentation, this strain produced 61.8 g of ethanol/liter, with 86.5% of theoretical yield from raw corn starch.