Organosolv pretreatment by crude glycerol from oleochemicals industry for enzymatic hydrolysis of wheat straw

In order to defray the cost of biodiesel production, the ensuing work was to further investigate utilization of the crude glycerol (CG) from oleochemicals industry in the atmospheric autocatalytic organosolv pretreatment (AAOP) to enhance enzymatic hydrolysis.

The AAOP–CG enabled wheat straw to achieve with reasonable enzymatic hydrolysis yields, reaching 75% for the wet substrate and 63% for the dried. Lipophilic compounds from the CG formed pitch deposition on the fiber, which was responsible for low delignification (30%) and also troublesome in practical operation. Pitch deposits itself had no significant role on enzymatic hydrolysis. A striking finding of the lignin recondensation and/or lignin–carbohydrate complex helped explain why dried pretreated wheat straw had a low enzymatic hydrolysis yield. The CG was suitable for the AAOP to enhance enzymatic hydrolysis of lignocellulosic biomass. But it was advisable to remove lipophilic compounds from crude glycerol before utilization.     

Production of SCP and cellulase by Aspergillus terreus from bagasse substrate

The fermentation of 1.0% untreated bagasse under optimum cultural and nutritional conditions with Aspergillus terreus GN1 indicated that the maximum rate of protein and cellulase production could be obtained during three days of submerged fermentation. Even though 16.4% protein recovery, 0.55 units CMCase/mL, and 0.027 FPase units/mL were obtained on the seventh day, the rates of increase in protein recovery and cellulase production were slower than those obtained up to these days, which were 14.3% protein recovery, 0.45 units CMCase/mL, and 0.019 units FPase/mL. There was an initial lag in the utilization of cellulose up to two days due to the utilization of the water-soluble carbohydrate present in untreated bagasse. Cellulose utilization and water-soluble carbohydrate content during fermentation were correlated with protein recovery and enzyme production. The protein and cellulase production during three days fermentation with 1.0% untreated and treated bagasse were compared and the protein content of the total biomass was calculated and treated bagasse were compared and the protein content of the biomass was calculated into constituent protein contributed by the fungal mycelium and the under graded bagasse. The total biomass recovered with untreated and treated bagasse was 1020 and 820 mg/g bagasse substrate, respectively, and contained 14.3 and 20.6% crude protein, respectively. The contribution of fungal biomass and under graded bagasse was 309 and 711, and 373 and 447 mg/g untreated and treated bagasse substrates, respectively. In an 8-L-flask trial during three days of fermentation, the recovery of SCP and cellulase were 66 g and 32,400 units (Sigma) for treated bagasse and 82 g and 8200 units (Sigma) for untreated bagasse, respectively.     

Bioethanol Production from Horticultural Waste Using Crude Fungal Enzyme Mixtures Produced by Solid State Fermentation

It was desired to study efficient and simplified methods to convert organosolv-pretreated horticultural waste (HW) to ethanol fuel using cellulase produced under solid-state fermentation (SSF). The unprocessed cellulase crude (72.2 %) showed better reducing sugar yield using filter paper than the commercial enzyme blend (68.7 %). Enzymatic hydrolysis of organosolv-pretreated HW using the crude cellulase with 20 % solid content, enzyme loading of 15 FPU/g HW at 50 °C, and pH 5.5 resulted in a HW hydrolysate containing 25.06 g/L glucose after 72 h. Fermentation of the hydrolysate medium produced 12.39 g/L ethanol with 0.49 g/g yield from glucose and 0.062 g/g yield from HW at 8 h using Saccharomyces cerevisiae. This study proved that crude cellulase complex produced under SSF and organosolv pretreatment can efficiently convert woody biomass to ethanol without any commercial cellulase usage.     

Hydrolysis of lignocellulosic materials for ethanol production: a review

Lignocellulosic biomass can be utilized to produce ethanol, a promising alternative energy source for the limited crude oil. There are mainly two processes involved in the conversion: hydrolysis of cellulose in the lignocellulosic biomass to produce reducing sugars, and fermentation of the sugars to ethanol. The cost of ethanol production from lignocellulosic materials is relatively high based on current technologies, and the main challenges are the low yield and high cost of the hydrolysis process. Considerable research efforts have been made to improve the hydrolysis of lignocellulosic materials. Pretreatment of lignocellulosic materials to remove lignin and hemicellulose can significantly enhance the hydrolysis of cellulose. Optimization of the cellulase enzymes and the enzyme loading can also improve the hydrolysis. Simultaneous saccharification and fermentation effectively removes glucose, which is an inhibitor to cellulase activity, thus increasing the yield and rate of cellulose hydrolysis.     

微生物发酵对木薯渣营养成分的影响

[背景]将木薯渣作为饲料资源进行开发和利用能够减轻环境污染,实现资源就地转化,已成为国内外研究热点.微生物发酵可降低木薯渣的粗纤维含量,改善适口性,提高饲料转化率.[目的]筛选对木薯渣发酵效果较好的微生物发酵剂及其发酵时长.[方法]试验选用A(芽孢菌+乳酸菌+酿酒酵母菌)、B(戊糖片球菌+酿酒酵母菌)和C(植物乳杆菌+...     

Effect of nutritional factors on cellulase enzyme and microbial protein production by Aspergillus terreus and its evaluation

The biomass yield, cellulolytic activity, and protein recovery using Aspergillus terreus GN1 with alkali-treated sugarcane bagasse was studied using different levels (250-600 mg of N/L of broth) of organic and inorganic nitrogen sources. e.g., cattle urine, urea, cornsteep liquor, ammonium sulfate, ammonium nitrate, ammonium iron sulfate, ammonium chloride, and sodium nitrate. Among different levels of alkali-treated bagasse substrate concentrations (0.5-4.0% w/v) tested, 1.0% substrate yielded the highest crude protein content, protein recovery, and cellulolytic activity. The biomass recovery with 1.0% substrate ranged from 290-380 mg/500 mg bagasse substrate in a 50-mL broth with a nitrogen level of 250-600 mg of N/L in all the sources except ammonium iron sulfate, which yielded 402-439 mg/500 mg bagasse substrate. However, crude protein content of biomass obtained with an ammonium iron sulfate nitrogen source was the lowest. Cornsteep liquor nitrogen source at the rate of 600 mg of N/L yielded the maximum crude protein of 32.9%, protein recovery of 22.2 g/100 g of bagasse, and carboxymethyl cellulase and filter paper enzyme activities of 1.1 and 0.09 units/mL, among the organic and inorganic nitrogen sources studied. In general, the organic nitrogen sources and inorganic nonammonium nitrogen sources were utilized preferentially for protein production over the inorganic ammonium nitrogen sources. The fermentation time required under optimum cultural and nutritional conditions for A. terreus GN1 was also evaluated. The crude protein content of the biomass increased gradually up to the seventh day of fermentation, but the protein recovery rate was high up to two or three days. It was observed that the cellulose utilization rate increased after an initial lag of one day up to the third day and gradually increased further, which corresponded positively with protein content, biomass protein recovery, and cellulase enzyme activity. On the seventh day of fermentation, the crude protein content, biomass protein recovery, water-soluble carbohydrate, bagasse cellulose utilization, CMCase, and FPase activities were 32.8%, 20.1 g/100 g of bagasse, 6.2%, 82.7%, 1.0. and 0.08 U/mL, respectively. The final biomass recovered contained 32.8% crude protein content and had an in vitro rumen digestibility (IVRD) coefficient of 68.8%. The biomass contained almost all the essential and nonessential amino acids and was comparable with FAO reference protein. It is concluded that a fermentation time of 72 h gave a faster rate of protein production of 16.9 g/100 g of bagasse with 69.8% bagasse cellulose utilization with 76.0% IVRD. and contained almost all the essential and nonessential amino acids.     

Utilization of pretreated coir pith for the optimized bioproduction of cellulase by Aspergillus nidulans

The present study is aimed at simultaneous cellulase synthesis and coir pith degradation by Aspergillus nidulans using coir pith as chief substrate. The lignocellulosic biomass, coir pith is known to be an excellent carbon source for microbial cellulase production under solid state fermentation. The alkali pretreatment with sodium hydroxide was seen to enhance enzymatic hydrolysis. The effect of coir pith weight, moisture content, initial pH and growth temperature on cellulase activity and yield were investigated by response surface methodology (RSM) employing a four-factor-five-level central composite design (CCD). The results of Fourier transform infrared spectroscopy (FTIR), X-Ray diffraction (XRD) and Scanning electron microscopy (SEM) of coir pith showed structural changes through pretreatment, in favor of enzymatic hydrolysis. Maximum carboxy methyl cellulase activity (CMCase) of 28.64 U/g and cellulase yield of 66.32% were achieved with 8 g coir pith at 70% moisture content and 40 °C temperature with pH 5 as evident from run numbers 25 and 30. Filter paper (FPase) and cellobiase (CBase) activities of 10.23 U/g and 4.31 U/g respectively were observed on the 11th day after the inoculation.     

An integrative process of bioconversion of oil palm empty fruit bunch fiber to ethanol with on-site cellulase production

The aim of this study was to efficiently convert oil palm empty fruit bunch fiber (OPEFB), one of the most commonly generated lingo-wastes in Southeast Asia, into both cellulase and bioethanol. The unprocessed cellulase crude (37.29 %) produced under solid-state fermentation using OPEFB as substrate showed a better reducing sugar yield using filter paper than the commercial enzyme blend (34.61 %). Organosolv pretreatment method could efficiently reduce hemicellulose (24.3–18.6 %) and lignin (35.2–22.1 %) content and increase cellulose content (40.5–59.3 %) from OPEFB. Enzymatic hydrolysis of pretreated OPEFB using the crude cellulase with 20 % solid content, enzyme loading of 15 FPU/g OPEFB at 50 °C, and pH 5.5 resulted in a OPEFB hydrolysate containing 36.01 g/L glucose after 72 h. Fermentation of the hydrolysate medium produced 17.64 g/L ethanol with 0.49 g/g yield from glucose and 0.088 g/g yield from OPEFB at 8 h using Saccharomyces cerevisiae.     

Lactic acid production from sugarcane bagasse hydrolysates by Lactobacillus pentosus: Integrating xylose and glucose fermentation

Lactic acid, traditionally obtained through fermentation process, presents numerous applications in different industrial segments, including production of biodegradable polylactic acid (PLA). Development of low cost substrate fermentations could improve economic viability of lactic acid production, through the use of agricultural residues as lignocellulosic biomass. Studies regarding the use of sugarcane bagasse hydrolysates for lactic acid production by Lactobacillus spp. are reported. First, five strains of Lactobacillus spp. were investigated for one that had the ability to consume xylose efficiently. Subsequently, biomass fractionation was performed by dilute acid and alkaline pretreatments, and the hemicellulose hydrolysate (HH) fermentability by the selected strain was carried out in bioreactor. Maximum lactic acid concentration and productivity achieved in HH batch were 42.5 g/L and 1.02 g/L h, respectively. Hydrolyses of partially delignified cellulignin (PDCL) by two different enzymatic cocktails were compared. Finally, fermentation of HH and PDCL hydrolysate together was carried out in bioreactor in a hybrid process: saccharification and co-fermentation with an initial enzymatic hydrolysis. The high fermentability of these process herein developed was demonstrated by the total consumption of xylose and glucose by Lactobacillus pentosus, reaching at 65.0 g/L of lactic acid, 0.93 g/g of yield, and 1.01 g/L h of productivity. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2718, 2019     

Study of the enzymatic hydrolysis of cellulose for production of fuel ethanol by the simultaneous saccharification and fermentation process

The biochemical conversion of cellulosic biomass to ethanol, a promising alternative fuel, can be carried out efficiently and economically using the simultaneous saccharification and fermentation (SSF) process. The SSF integrates the enzymatic hydrolysis of cellulose to glucose, catalyzed by the synergistic action of cellulase and beta-glucosidase, with the fermentative synthesis of ethanol. Because the enzymatic step determines the ethanol. Because the enzymatic step determines the availability of glucose to the ethanologenic fermentation, the kinetic of cellulose hydrolysis by cellulase and beta-glucosidase and the susceptibility of the two enzymes to inhibition by hydrolysis and fermentation products are of significant importance to the SSF performance and were investigated under realistic SSF conditions. A previously developed SSF mathematical model was used to conceptualize the depolymerization of cellulose. The model was regressed to the collected data to determine the values of the enzyme parameters and was found to satisfactorily predict the kinetics of cellulose hydrolysis. Cellobiose and glucose were identified as the strongest inhibitors of cellulase and beta-glucosidase, respectively. Experimental and modeling results are presented in light of the impact of enzymatic hydrolysis on fuel ethanol production. (c) 1993 Wiley & Sons, Inc.     

斑茅酶解转化可发酵单糖的液氨预处理及参数优化

斑茅(Saccharum arundinaceum Retz.)的生物产量高,对土壤条件要求低,可作为纤维素乙醇生产的原料作物在我国南方地区广泛种植.实验以斑茅为原料,采用液氨预处理法克服其水解顽抗性,并添加纤维素酶进行酶解,运用高效液相色谱(HPLC)测定了酶解液中的单糖含量.实验结果表明在纤维素酶添加量为15FPU/(g当量葡聚糖)、预处理原料含水率为80％、预处理温度为130℃、预处理驻留时间为10 min、液氨与生物质的质量比例为2∶1时,葡聚糖和木聚糖的总转化率分别为69.34％和82.60％,相比于未作预处理的原料分别提高了573％和1 056％,单糖产量提高8倍.实验结果表明液氨预处理对斑茅是一种有效的预处理方式,并优于稀酸或湿爆法预处理,与酸预处理和氨爆法(AFEX)处理效果接近.     

Influence of solid loading on enzymatic hydrolysis of steam exploded or liquid hot water pretreated olive tree biomass

Olive tree pruning biomass, pretreated by either liquid hot water or steam explosion under selected conditions, was used as a substrate for enzymatic hydrolysis. The pretreated material was further submitted to alkaline delignification, the objective being to improve hydrolysis yields as well as increasing cellulose content in the pretreated feedstock. The enzymatic hydrolysis of pretreated residues was performed using a commercial cellulase mixture supplemented with β-glucosidase, using a solid loading range from 2 to 30% (w/v). The influence of substrate concentration on the enzymatic hydrolysis yield and on glucose concentration was studied. Comparative results with and without a delignification step are presented. Enzymatic hydrolysis at high substrate concentration (≥20%) is possible, yielding a concentrated glucose solution (>50 g/L). Nevertheless, a cellulose fraction of the pretreated residue remains unaltered.     

Differences in glucose yield of residues from among varieties of rice,wheat, and sorghum after dilute acid pretreatment

Bio-refinery processes require use of the most suitable lignocellulosic biomass for enzymatic saccharification and microbial fermentation. Glucose yield from biomass solid fractions obtained after dilute sulfuric acid (1%) pretreatment (at 180 °C) was investigated using 14, 8, and 16 varieties of rice, wheat, and sorghum, respectively. Biomass solid fractions of each crop showed similar cellulose content. However, glucose yield after enzymatic hydrolysis (cellulase loading at 6.6 filter paper unit/g-biomass) was different among the varieties of each crop, indicating genotypic differences for rice, wheat, and sorghum. Nuclear magnetic resonance method revealed that the high residual level of lignin aromatic regions decreased glucose yield from solid fraction of sorghum.     

BSA treatment to enhance enzymatic hydrolysis of cellulose in lignin containing substrates

Cellulase and bovine serum albumin (BSA) were added to Avicel cellulose and solids containing 56% cellulose and 28% lignin from dilute sulfuric acid pretreatment of corn stover. Little BSA was adsorbed on Avicel cellulose, while pretreated corn stover solids adsorbed considerable amounts of this protein. On the other hand, cellulase was highly adsorbed on both substrates. Adding a 1% concentration of BSA to dilute acid pretreated corn stover prior to enzyme addition at 15 FPU/g cellulose enhanced filter paper activity in solution by about a factor of 2 and beta-glucosidase activity in solution by about a factor of 14. Overall, these results suggested that BSA treatment reduced adsorption of cellulase and particularly beta-glucosidase on lignin. Of particular note, BSA treatment of pretreated corn stover solids prior to enzymatic hydrolysis increased 72 h glucose yields from about 82% to about 92% at a cellulase loading of 15 FPU/g cellulose or achieved about the same yield at a loading of 7.5 FPU/g cellulose. Similar improvements were also observed for enzymatic hydrolysis of ammonia fiber explosion (AFEX) pretreated corn stover and Douglas fir treated by SO(2) steam explosion and for simultaneous saccharification and fermentation (SSF) of BSA pretreated corn stover. In addition, BSA treatment prior to hydrolysis reduced the need for beta-glucosidase supplementation of SSF. The results are consistent with non-specific competitive, irreversible adsorption of BSA on lignin and identify promising strategies to reduce enzyme requirements for cellulose hydrolysis.     

The Role of Polymeric Micelles on Chemical Changes of Pretreated Corn Stover,Cellulase Structure,and Adsorption

Enzymatic hydrolysis of lignocellulosic biomass is limited by rapid cellulase deactivation, consequently requiring large amounts of enzyme to maintain acceptable biomass conversion. In this study, a new approach to improve lignocellulose hydrolysis was investigated. Performing enzymatic hydrolysis of corn stover (CS) in the presence of polymeric–surfactant micelles (PMs) was demonstrated to improve hydrolysis yield to a greater extent than using only surfactant micelles. Application of 2 % (w/w) of polyethylene glycol (PEG 6000) with casein, Tween-20, and Triton X-100 at levels above the critical micelle concentrations increased the hydrolysis yield of CS containing high-bound lignin (extrusion-pretreated) by up to 87.8, 11.7, and 7.5 %, respectively. These PMs were not effective during enzymatic hydrolysis of biomass lacking lignin (Avicel) or alkali-pretreated CS (7.2 % lignin). The main reasons for the enhanced cellulase activity observed due to PEG-casein, PEG-Tween, and PEG-Triton were enhanced cellulase solubilization; reformation of α-helix substructure; and combination of induced cellulase solubilization, α-helix reformation, and chemical changes in the microstructure of biomass, respectively. Deformation of the cellulase substructure during hydrolysis of biomass and its subsequent reformation in the presence of surfactants were shown in this study for the first time. Chemical changes in the microstructure of biomass (e.g., lignin side changes, C–O bonds, and amorphous cellulose) were found to be another potential reason for the effectiveness of surfactants when they are incubated at above 6 g/L for 72 h with biomass.     

Mild pretreatment of yellow poplar biomass using sequential dilute acid and enzymatically-generated peracetic acid to enhance cellulase accessibility

Biomass contains cellulose, xylan and lignin in a complex interwoven structure that hinders enzymatic hydrolysis of the cellulose. To separate these components in yellow poplar biomass, we sequentially pretreated with dilute sulfuric acid and enzymatically-generated peracetic acid. In the first step, the dilute acid with microwave heating (140°C, 5 min) hydrolyzed 90% of xylan. The xylose yield in hydrolysate after dilute acid pretreatment was 83.1%. In the second step, peracetic acid (60°C, 6 h) removed up to 80% of lignin. This sequential pretreatment fractionated biomass into xylan and lignin, leaving a solid residue enriched in cellulose (~80%). The sequential pretreatment enhanced enzymatic digestibility of the cellulase by removal of the other components in biomass. The glucose yield after enzymatic hydrolysis was 90.5% at a low cellulase loading (5 FPU/g of glucan), which is 1.6 and 18 times higher than for dilute acid-pretreated biomass and raw biomass, respectively. This novel sequential pretreatment with dilute acid and peracetic acid efficiently separates the three major components of yellow poplar biomass, and reduces the amount of cellulase needed.     

Solid state fermentation of aquatic macrophytes for crude protein extraction

Aquatic macrophytes such as Elodea nuttalli, Vallisneria natans, Alterranthera philoxerides that are widely distributed in water environments of Lake Taihu basin were used as substrate of solid state fermentation to produce crude protein extraction. The effects of single-strain fermentation and mixed strains fermentation of aquatic macrophytes on the production of crude protein extraction and cellulase activity are analyzed, respectively. The experimental results showed that the crude protein content of products with mixed strains fermentation is higher than that with single-strain fermentation. The crude protein content of V. natans fermented by Aspergillus niger and Candida utilis is the highest among the aquatic macrophytes examined in this study. V. natans is used as the substrate to be fermented by C. utilis and A. niger; their ratio is 1:1 at 28 ± 1 °C for 72 h. The crude protein of fermented V. natans is as high as 49.54%, with 128.82% of its increase rate. The cellulose activity reaches a maximum of 4.21 μ/ml at 84 h of fementation of V. natans. Thus, the solid state fermentation of aquatic macrophytes to produce crude protein extraction is promising, which make aquatic macrophytes a potential resource and thus is beneficial to the long-term ecological restoration of eutrophic lakes.     

Aqueous ammonia pretreatment, saccharification, and fermentation evaluation of oil palm fronds for ethanol production

Oil palm fronds are the most abundant lignocellulosic biomass in Malaysia. In this study, fronds were tested as the potential renewable biomass for ethanol production. The soaking in aqueous ammonia pretreatment was applied, and the fermentability of pretreated fronds was evaluated using simultaneous saccharification and fermentation. The optimal pretreatment conditions were 7?% (w/w) ammonia, 80?°C, 20?h of pretreatment, and 1:12 S/L ratio, where the enzymatic digestibility was 41.4?% with cellulase of 60?FPU/g-glucan. When increasing the cellulase loading in the hydrolysis of pretreated fronds, the enzymatic digestibility increased until the enzyme loading reached 60?FPU/g-glucan. With 3?% glucan loading in the SSF of pretreated fronds, the ethanol concentration and yield based on the theoretical maximum after 12 and 48?h of the SSF were 7.5 and 9.7?g/L and 43.8 and 56.8?%, respectively. The ethanol productivities found at 12 and 24?h from pretreated fronds were 0.62 and 0.36?g/L/h, respectively.     

2种纤维素酶水解效果比较及酶蛋白组分分析

比较了自产纤维素酶和商品纤维素酶的水解效果,并采用超滤、层析、SDS-PAGE相结合的方法分析2种纤维素酶蛋白组分的差异。里氏木霉以纸浆为C源合成的自产纤维素酶的水解得率高于商品纤维素酶,自产纤维素酶水解48h的得率为66.24%,商品纤维素酶的得率为52.19%。自产纤维素酶中存在着Cel6A酶组分和XYNⅡ酶组分,而商品纤维素酶中没有检测到这2种酶组分。自产纤维素酶和商品纤维素酶的Cel1A酶组分和Cel7A酶组分间存在着分布和含量上的差异。自产纤维素酶在相对分子质量(2.5～3.5)×104范围内存在着几条蛋白条带,而商品纤维素酶则是在相对分子质量3.5×104附近存在着几条蛋白条带。     

Ethanol and anaerobic conditions reversibly inhibit commercial cellulase activity in thermophilic simultaneous saccharification and fermentation (tSSF)

ABSTRACT: BACKGROUND: A previously developed mathematical model of low solids thermophilic simultaneous saccharification and fermentation (tSSF) with Avicel was unable to predict performance at high solids using a commercial cellulase preparation (Spezyme CP) and the high ethanol yield Thermoanaerobacterium saccharolyticum strain ALK2. The observed hydrolysis proceeded more slowly than predicted at solids concentrations greater than 50 g/L Avicel. Factors responsible for this inaccuracy were investigated in this study. RESULTS: Ethanol dramatically reduced cellulase activity in tSSF. At an Avicel concentration of 20 g/L, the addition of ethanol decreased conversion at 96 hours, from 75% in the absence of added ethanol down to 32% with the addition of 34 g/L initial ethanol. This decrease is much greater than expected based on hydrolysis inhibition results in the absence of a fermenting organism. The enhanced effects of ethanol were attributed to the reduced, anaerobic conditions of tSSF, which were shown to inhibit cellulase activity relative to hydrolysis under aerobic conditions. Cellulose hydrolysis in anaerobic conditions was roughly 30% slower than in the presence of air. However, this anaerobic inhibition was reversed by exposing the cellulase enzymes to air. CONCLUSION: This work demonstrates a previously unrecognized incompatibility of enzymes secreted by an aerobic fungus with the fermentation conditions of an anaerobic bacterium and suggests that enzymes better suited to industrially relevant fermentation conditions would be valuable. The effects observed may be due to inactivation or starvation of oxygen dependent GH61 activity, and manipulation or replacement of this activity may provide an opportunity to improve biomass to fuel process efficiency.