复合乳酸菌提高干玉米秸秆微贮效果及产乙醇能力分析

为提高干玉米秸秆的可生化性,文章参考强化微生物微贮原理,探讨接种复合乳酸菌对干玉米秸秆微贮品质的影响。以干玉米秸秆为原料,接种复合微生物干酪乳杆菌、发酵乳杆菌和粪链球菌,在不同时间取样分析微贮料的成分变化,以确定微贮指标,运用高通量测序技术分析微贮料的微生物组成和多样性,并考察秸秆微贮前后的微观变化及产乙醇潜力。研究结果表明:微贮料中的乳杆菌属是优势菌,厌氧发酵4周后,乳酸含量达到4.30%左右,p H值降低至4.22,微贮过程趋于稳定,这些都是微贮结束的指标;微贮料表面布满塌陷的孔洞,增加了酶或微生物的可及性;水洗后的微贮料利用酿酒酵母发酵56 h后,乙醇浓度达到32.76 g/L,乙醇转化率为57.21%。     

Optimization of ethanol production from high dry matter liquefied dry sweet sorghum stalks

The ability of sweet sorghum to be utilized as feedstock for ethanol production at high initial dry material concentration was investigated. Sweet sorghum, after being dried, was liquefacted employing commercial cellulase solution Celluclast^® 1.5L, in order submerged fermentation to be permitted under high-solids concentrations. The presence of a separate enzymatic liquefaction step at 350 kg m⁻³ initial DM enhanced both ethanol production and productivity by 29.76% and 250%, respectively. Response surface methodology, based on the central composite design was applied to explore the combined effect of liquefaction duration and enzyme loading in order liquefaction conditions to be optimized. When the optimum conditions were tested using an enzyme load of 8.32 FPU g⁻¹ of dry material for 8.6 h at 50 °C, high productivity (3.0 kg m⁻³ h⁻¹) and final ethanol production (62.5 kg m⁻³) were achieved.     

Fuel ethanol production from sweet sorghum bagasse using microwave irradiation

Sweet sorghum is a hardy crop that can be grown on marginal land and can provide both food and energy in an integrated food and energy system. Lignocellulose rich sweet sorghum bagasse (solid left over after starch and juice extraction) can be converted to bioethanol using a variety of technologies. The largest barrier to commercial production of fuel ethanol from lignocellulosic material remains the high processing costs associated with enzymatic hydrolysis and the use of acids and bases in the pretreatment step. In this paper, sweet sorghum bagasse was pretreated and hydrolysed in a single step using microwave irradiation. A total sugar yield of 820 g kg⁻¹ was obtained in a 50 g kg⁻¹ sulphuric acid solution in water, with a power input of 43.2 kJ g⁻¹ of dry biomass (i.e. 20 min at 180 W power setting). An ethanol yield based on total sugar of 480 g kg⁻¹ was obtained after 24 h of fermentation using a mixed culture of organisms. These results show the potential for producing as much as 0.252 m³ tonne⁻¹ or 33 m³ ha⁻¹ ethanol using only the lignocellulose part of the stalks, which is high enough to make the process economically attractive.     

Hydrothermal pretreatment of switchgrass and corn stover for production of ethanol and carbon microspheres

Pretreatment of biomass is viewed as a critical step to make the cellulose accessible to enzymes and for an adequate yield of fermentable sugars in ethanol production. Recently, hydrothermal pretreatment methods have attracted a great deal of attention because it uses water which is a inherently present in green biomass, non-toxic, environmentally benign, and inexpensive medium. Hydrothermal pretreatment of switchgrass and corn stover was conducted in a flow through reactor to enhance and optimize the enzymatic digestibility. More than 80% of glucan digestibility was achieved by pretreatment at 190 °C. Addition of a small amount of K₂CO₃ (0.45-0.9 wt.%) can enhance the pretreatment and allow use of lower temperatures. Switchgrass pretreated at 190 °C only with water had higher internal surface area than that pretreated in the presence of K₂CO₃, but both the substrates showed similar glucan digestibility. In comparison to switchgrass, corn stover required milder pretreatment conditions. The liquid hydrolyzate generated during pretreatment was converted into carbon microspheres by hydrothermal carbonization, providing a value-added byproduct. The carbonization process was further examined by GC-MS analysis to understand the mechanism of microsphere formation.     

Fuel ethanol production from sugarcane and corn: Comparative analysis for a Colombian case

The Colombian government has defined the use of bioethanol as a gasoline enhancer to reduce greenhouse gases, gasoline imports, and to boost the rural economy. To meet the projected fuel ethanol demand needed to oxygenate the gasoline in the whole country, the construction of about five additional ethanol production plants is required. For this, a comparative analysis of the technological options using different feedstocks should be performed. In this work, a comparison of the economical and environmental performance of the ethanol production process from sugarcane and corn under Colombian conditions has been carried out. Net present value and total output rate of potential environmental impact were used as the economical and environmental indicators, respectively. Through the integration of these indicators into one index by using the analytical hierarchy process (AHP) approach, sugarcane ethanol process was determined as the best choice for Colombian ethanol production facilities. AHP scores obtained in this study for sugarcane and corn ethanol were 0.571 and 0.429, respectively. However, starchy crops like corn, cassava or potatoes used as feedstock for ethanol production could potentially cause a higher impact on the rural communities and boost their economies if social matters are considered.     

Ethanol production from hydrothermal pretreated corn stover with a loop reactor

Hydrothermal pretreatment on raw corn stover (RCS) with a loop reactor was investigated at 195 °C for different times varying between 10 min and 30 min. After pretreatment, the slurry was separated into water-insoluble solid (WIS) and liquid phase. Glucan and xylan were found in the both phases. The pretreatment condition showed a significant impact on xylan recovery. As the pretreatment time prolonged from 10 min to 30 min, the xylan recovery from liquid phase changed between 39.5% and 45.6% and the total xylan recoveries decreased from 84.7% to 61.6%. While the glucan recovery seemed not sensitive to the different pretreatment times. The glucan recovered from liquid was from 4.9% to 5.6% and the total glucan recoveries from all the pretreatments were higher than 98%. Besides HMF and furfural, acetic, lactic, formic and glycolic acids were also found in the liquid phase. All the concentrations of these potential inhibitors were lower enough not to affect the activity of the Saccharomyces cerevisiae (S. cerevisiae). Compared with the ethanol production of 32.4% from the RCS with S. cerevisiae, all the WISs gave higher ethanol productions ranging between 61.2% and 71.2%. When the xylan was taken into consideration, the best pretreatment condition would be 195 °C, 15 min and the estimated total ethanol production was 201 g kg^?1 RCS by assuming the fermentation of both C-6 and C-5 with the ethanol yield of 0.51 g g^?1 and 0.47 g g^?1, respectively.     

Evaluating fuel ethanol feedstocks from energy policy perspectives: A comparative energy assessment of corn and corn stover

Concerns surrounding the continued, un-checked use of petroleum-based fuels in the transportation sector, the search for more sustainable, renewable alternatives, and the constraints of the existing supply infrastructure in the United States have placed a spotlight on biomass-derived fuels. The central question of the ethanol debate has changed from “Should we make ethanol?” to “From what should we make ethanol?” emphasizing the importance of understanding the differences between specific biomass supply systems for fuel ethanol. When presented with numerous options, the priorities of an individual decision maker will define which feedstock alternative is the most appropriate choice for development from their perspective. This paper demonstrates how energy data can be successfully used to quantify assessment metrics beyond a standard net energy value calculation, thus quantifying the relative “value” of ethanol supply systems. This value is defined based on decision-maker priorities that were adopted from national energy policy priorities: increased national energy security and increased conservation of energy resources. Nine energy assessment metrics that quantify detailed system energy data are calculated and a straightforward comparative assessment is performed between corn and corn stover feedstocks produced under the same farm scenario. Corn stover is shown to be more compatible with the national energy policy priorities and it is recommended that additional research be performed on utilizing this feedstock from the corn farm.     

Acid hydrolysis of corn stover for biohydrogen production using Thermoanaerobacterium thermosaccharolyticum W16

Lignocellulosic biomass, if properly hydrolyzed, can be an ideal feedstock for fermentative hydrogen production. This work considered the pretreatment of corn stover (CS) using a dilute acid hydrolysis process and studied its fermentability for hydrogen production by the strain Thermoanaerobacterium thermosaccharolyticum W16. The effects of sulfuric acid concentration and reaction time in the hydrolysis stage of the process were determined based on a 2² central composite experimental design with respect to maximum hydrogen productivity. The optimal hydrolysis conditions to yield the maximum quantity of hydrogen by W16 were 1.69% sulfuric acid and 117 min reaction time. At these conditions, the hydrogen yield was shown to be 3305 ml H₂ L⁻¹ medium, which corresponds to 2.24 mol H₂ mol⁻¹ sugar. The present results indicate the potential of using T. thermosaccharolyticum W16 for high-yield conversion of CS hemicellulose into bio-H₂ integrated with acid hydrolysis.     

Optimization of biohydrogen production using acid pretreated corn stover hydrolysate followed by nickel nanoparticle addition

The dilute acid hydrolysis using corn stover (CS) to produce reducible sugars was optimized by the response surface methodology. The electron-equivalent balances of the main metabolites during the dark fermentation (DF) using acid hydrolysate were investigated to identify the evolutions of the electron sinks over the course of DF. The additions of nickel ion and Ni⁰ nanoparticles (NPs) were found to effectively enhance the hydrogen production at experimental conditions. The optimal condition (HCl 2.5 wt%, hydrolyzing duration 105 minutes, pH=5, S/B=3.5, Ni⁰ NPs=10 mg/L^-1) was achieved with Y_H2/S reaching 1.18 (mol.mol^-1-glucose). The Y_H2/S increased from 0.7 (mol.mol^-1-glucose) to 1.18 (mol.mol^-1-glucose) reaching 40% hydrogen yield increase when Ni⁰ NPs was added to the fermentation broth. Among the investigated significant soluble metabolites, the butyric acid was found to serve as the largest e-sink in the electron-equivalent balance. The additions of Ni⁰ NPs at low level (below 10 mg/L) were found to appreciably increase the hydrogen production. The increased pH and substrate to biomass ratio were found to skew the metabolic balance from hydrogen production to the biosynthesis (an increase of biomass). The proposed anaerobic digestion model with consideration of the inhibitory factors model presents a good agreement with the experimental data. The chemical addition such as nickel ions, Ni⁰ NPs was found to be a practical approach in enhancing biohydrogen production using CS acid hydrolysate as cultivation broth.     

Bioaugmentation with Thermoanaerobacterium thermosaccharolyticum W16 to enhance thermophilic hydrogen production using corn stover hydrolysate

In the present work, with corn stover hydrolysate as the substrate, an efficient hydrogen-producing thermophile, Thermoanaerobacterium thermosaccharolyticum W16, was added to three kinds of seed sludge (rotten corn stover (RCS), cow dung compost (CDC), and sludge from anaerobic digestion (SAD)) to investigate the effect of bioaugmentation on thermophilic hydrogen production. Batch test results indicate that the bioaugmentation with a small amount of the strain T. thermosaccharolyticum W16 (5% of total microbes) increased the hydrogen yield to varying degrees (RCS: from 8.78 to 9.90 mmol H₂/g utilized sugar; CDC: from 8.18 to 8.42 mmol H₂/g utilized sugar; SAD: from 8.55 to 9.17 mmol H₂/g utilized sugar). The bioaugmentation process also influenced the soluble metabolites composition towards more acetate and less butyrate production for RCS, and more acetate and less ethanol accumulation for SAD. Microbial community analysis indicates that Thermoanaerobacterium spp. and Clostridium spp. dominated microbial community in all situations and might be mainly responsible for thermophilic hydrogen generation. For RCS and SAD, the bioaugmentation obviously increased the relative abundance of the strain T. thermosaccharolyticum W16 in microbial community, which might be the main reason for the improvement of hydrogen production in these cases.     

Simultaneous saccharification and fermentation (SSF) of non-starch polysaccharides and starch from fresh tuber of Canna edulis ker at a high solid content for ethanol production

Canna edulis ker is a potential feedstock for ethanol production because of its low nutrition requirements and the high starch content of its tubers. The processing of C. edulis is limited by the high viscosity of the biomass. In this study, cell wall degrading enzymes (CWDEs) containing acid xylanase and β-glucanase were successful in reducing the viscosity (from 167.30 Pa s to 8.66 Pa s) at 50 °C for 120 min. The effect of CWDEs on simultaneous saccharification and fermentation (SSF) was investigated. Addition of CWDEs before SSF, resulted in an increase in total sugar and fermentable sugar. Meanwhile, the viscosity decreased sharply from approximately 200.00 Pa s to 2.98 Pa s, thereby improving the fermentation parameters and the mass fraction of the theoretical ethanol yield was 94.5%. Only special demand of nutritional ingredients was nitrogen, urea at 750 mg kg⁻¹ was found to be suitable for this purpose. In the verification experiments, the mass fraction of the theoretical ethanol yield in a 5 L fermentor was 98.3%. In conclusion, the pretreatment with CWDEs has significant effect on high level ethanol production using roots and tubers on an industrial scale from the biomass utilization efficiency and economic standpoint.     

Enhanced biohydrogen production from corn stover hydrolyzate by pretreatment of two typical seed sludges

Five individual pretreatment methods (heat, ultrasonic, ultraviolet, acid, and base) were performed on two typical seed sludges (river sediments and anaerobic granular sludge) to evaluate their effectiveness on enriching efficient hydrogen (H₂)-producing bacteria and enhancing H₂ production using corn stover hydrolyzate. Results indicated that pretreatment processes caused more remarkable improvements for river sediments than anaerobic granular sludge. Among the five protocols, heat pretreatment reached high H₂ yield for both river sediments (4.17 mmol H₂/g utilized sugar) and anaerobic granular sludge (2.84 mmol H₂/g utilized sugar). Ultraviolet and ultrasonic pretreatments were conditionally effective for river sediments and anaerobic granular sludge, respectively. In most cases, pretreatment processes altered soluble metabolites distribution towards more acetate and less ethanol production. Microbial community analysis indicated that heat and ultrasonic pretreatments can respectively lead to significant and indistinctive change on original microbial community. Besides frequently detected Escherichia spp., Serratia spp., and Klebsiella spp., some species of Clostridium spp. and Bacillus spp. might be efficient H₂ producer responsible for better H₂-producing performances.     

Hydrogen production from the fermentation of corn stover biomass pretreated with a steam-explosion process

Lignocellulosic biomass contains 70–80% carbohydrates and could serve as the ideal feedstock for fermentative hydrogen production. We conducted the pretreatment of corn stover using a steam-explosion process and studied its fermentability for hydrogen production. Using natural inoculant obtained from the heated sludge of a local wastewater treatment plant, we demonstrated that the indigenous microbes were capable of efficiently fermenting the aqueous hydrolyzate derived from the hemicellulose fraction of the steam-pretreated corn stover with and without acid during pretreatment. Biogas contained equal amounts of hydrogen and carbon dioxide. The carbon mass balance is approximately 84%, with acetic and butyric acids as the major carbon byproducts along with carbon dioxide. Hydrogen molar yields of 2.84 and 3.0 were obtained using the mixed sugars present in the hydrolyzate derived from neutral and acidic steam explosion, respectively. These findings verify that hemicellulose from corn stover could be a suitable feedstock for hydrogen production via dark fermentation.     

Pre-treatment and ethanol fermentation potential of olive pulp at different dry matter concentrations

Renewable energy sources have received increased interest from the international community with biomass being one of the oldest and the most promising ones. In the concept of exploitation of agro-industrial residues, the present study investigates the pre-treatment and ethanol fermentation potential of the olive pulp, which is the semi solid residue generated from the two-phase processing of the olives for olive oil production. Wet oxidation and enzymatic hydrolysis have been applied aiming at the enhancement of carbohydrates' bioavailability. Different concentrations of enzymes and enzymatic durations have been tested. Both wet oxidation and enzymic treatment were evaluated based on the ethanol obtained in a subsequent fermentation step by Saccharomyces cerevisiae and Thermoanaerobacter mathranii. It was found that a four-day hydrolysis time was adequate for a satisfactory release of glucose and xylose. The combination of wet oxidation and enzymatic hydrolysis resulted in the glucose and xylose concentration increase of 138 and 444%, respectively, compared to 33 and 15% with only enzymes added. However, the highest ethanol production was obtained when only enzymic pre-treatment was applied, implying that wet oxidation is not a recommended pre-treatment process for olive pulp at the conditions tested. It was also showed that increased dry matter concentration did not have a negative effect on the release of sugars, indicating that the cellulose and xylan content of the olive pulp is relatively easily available. The results of the experiments in batch processes clearly emphasize that the simultaneous saccharification and fermentation (SSF) mode is advantageous in comparison with the separate hydrolysis and fermentation (SHF) mode concerning process contamination.     

Syngas production from ethanol dry reforming using Cu-based perovskite catalysts promoted with rare earth metals

This paper reports about the production of syngas from dry reforming of ethanol (EDR) upon LaCuO₃ and CeCuO₃ catalysts that were prepared by using citrate sol-gel method. EDRs were run with fresh catalyst at each varied variable and 42 L/g_cat/h of feed in a tubular reactor under atmospheric pressure. At equal feed pressure of reactants, steady state CO₂ conversion increased exponentially from 700 to 800 °C while H₂ and CO yields were increasing differently in sigmoid trend rendering H₂/CO ratios to drop linearly from 1.7 to 1.0. However, these reaction results except the latter are otherwise when ethanol-CO₂ ratio was increased (reducing CO₂ pressure) at 750 °C. A minimum H₂/CO ratio was evidenced at the ethanol-CO₂ ratio of 1.48. LaCuO₃ catalyst was more superior in producing syngas owing to its relatively low reduction temperature, high surface area and crystallinity, many active sites, good surface morphology and many C–O, C–H and hydroxyl groups.     

Comparative study on bio-hydrogen production from corn stover: Photo-fermentation,dark-fermentation and dark-photo co-fermentation

In this study, three different fermentation methods, such as photo-fermentation (PF), dark-fermentation (DF) and dark-photo co-fermentation (DPCF) for bio-hydrogen production from corn stover were compared in terms of hydrogen production, substrate consumption, by-products formation and energy conversion efficiency. A modified Gompertz model was applied to perform the kinetic analysis of hydrogen production. The maximum cumulative hydrogen yield of 141.42 mL·(g TS)⁻¹ was achieved by PF, DF with the minimum cumulative hydrogen yield of 36.08 mL· (g TS)⁻¹ had the shortest lag time of 4.33 h, and DPCF had the maximum initial hydrogen production rate of 1.88 mL· (g TS)⁻¹·h⁻¹ and maximum initial hydrogen content of 44.40%. The results also indicated PF was an acid-consuming process with a low total VFAs concentration level of 2.90–4.19 g·L⁻¹, DF was a process of VFAs accumulation with a maximum total VFAs concentration of 12.66 g·L⁻¹, and DPCF was a synergistic process in which the total VFAs concentration was significantly reduced and the hydrogen production efficiency was effectively improved compared with DF. The energy conversion efficiency of PF, DF and DPCF were 10.12%, 2.58% and 6.45%, respectively.     

Biological hydrogen production from corn stover by moderately thermophile Thermoanaerobacterium thermosaccharolyticum W16

This study addressed the utilization of an agro-waste, corn stover, as a renewable lignocellulosic feedstock for the fermentative H₂ production by the moderate thermophile Thermoanaerobacterium thermosaccharolyticum W16. The corn stover was first hydrolyzed by cellulase with supplementation of xylanase after delignification with 2% NaOH. It produced reducing sugar at a yield of 11.2 g L⁻¹ glucose, 3.4 g L⁻¹ xylose and 0.5 g L⁻¹ arabinose under the optimum condition of cellulase dosage 25 U g⁻¹ substrate with supplement xylanase 30 U g⁻¹ substrate. The hydrolyzed corn stover was sequentially introduced to fermentation by strain W16, where, the cell density and the maximum H₂ production rate was comparable to that on simulated medium, which has the same concentration of reducing sugars with hydrolysate. The present results suggest a promising combined hydrogen production process from corn stover with enzymatic hydrolysis stage and fermentation stage using W16.     

玉米秸秆产乙醇两种工艺路径的对比研究

通过以玉米秸秆为原料生产乙醇的两条工艺路径的对比,分析了不同转化路径的特点和结果。路径一,将粉粹的玉米秸秆经超低酸处理后进行酶解,利用酶解液发酵产乙醇;路径二,通过气化技术将玉米秸秆产生CO,H_2等混合气体,由微生物转化成乙醇。通过路径一处理及发酵后,发酵溶液中的乙醇浓度为21.5 g/L。通过路径2处理后,发酵溶液中的乙醇浓度为2.6 g/L。对比分析显示,虽然路径一的乙醇产量高于路径二,但其成本、能耗也高;路径二能耗较低,但对厌氧发酵条件要求严格,乙醇产量较低。     

CO2 emissions from the production and combustion of fuel ethanol from corn

Concern over the increasing concentration of CO₂ in the Earth's atmosphere is causing us to re-evaluate how we use energy. In particular, we need to inquire if there are alternative energy systems which discharge less net CO₂ per unit of energy service. This paper deals with the CO₂ fluxes associated with the use of one biomass fuel, ethanol derived from corn. In a sustainable agricultural system, there is no net CO₂ flux to the atmosphere from the corn itself but there is a net CO₂ flux due to the fossil-fuel supplements currently used to produce and process corn. A comparison between ethanol from corn and gasoline from crude oil becomes very complex because of the variability of corn yield, the lack of available data on corn processing, and the complexity of treating the multiple products from corn processing. When the comparison is made on an energy content basis only, with no consideration of how the products are to be used, and at the margin of the current U.S. energy system, it appears that there is a net CO₂ saving associated with ethanol from corn. This net saving in CO₂ emissions may be as large as 40% or as small as 20%, depending on how one chooses to evaluate the by-product credits. This analysis also demonstrates that the frequently posed question, whether the energy inputs to ethanol exceed the energy outputs, would not be an over-riding consideration even if it were true, because most of the inputs are as coal and natural gas, whereas the output is as a high-quality liquid fuel.     

Bioethanol production from corn stalk juice using Saccharomyces cerevisiae TISTR 5020

This study aimed to use sweet corn hybrid hi-brix53 stalk juice for bioethanol production, to give a solution to the growing problem of food vs. fuel and to utilize waste for cheaper production. Hi-brix 53 stalk juice contained 112.07 ± 2.99 g L^?1 of total sugars and 21.83 ± 1.09 g L^?1 of reducing sugars. Through fermentation (24–120 h) using yeast (Saccharomyces cerevisiae), it produced 6.01% (v/v) bioethanol. The final ethanol produce (g L^?1) yield efficiency and volumetric ethanol productivity were at the highest at 24 h with 47.87 L^?1, 87.62% and 1.97 ± 0.06 (g L^?1 h^?1). These results suggest that hi-brix 53 stalk juice is an ideal substrate for bioethanol production.