柳枝稷青贮用乳酸菌复合系的组成多样性及其代谢特性

摘要:【目的】筛选一组乳酸产量高、组成稳定的柳枝稷青贮用乳酸菌复合系。【方法】通过连续限制性培养方法获得乳酸菌复合系SGL,使用变性梯度凝胶电泳(DGGE)和高通量测序技术分别分析其群落结构的稳定性和组成多样性。在培养基中添加不同氮源,测定氮源对SGL菌体生长和代谢产酸的影响。【结果】连续限制性培养8代,SGL的菌群结构趋于稳定,主要菌种为同型发酵乳酸菌,包括Lactobacillus nantensis (78.78%)、Lactobacillus plantarum(7.92%)、Lactobacillus pantheris(5.27%)、Bacillus coagulans(4.41%)和Lactococcus lactics(3.31%),是现有唯一的同时包含Lactobacillus、Lactococcus和Bacillus的乳酸菌复合系。酵母浸粉是促进SGL菌体生长和产乳酸的最好氮源,最适添加量为20 g/L。当(NH4)2SO4和酵母浸粉中N的比例为1:4时,菌体生长量和乳酸产量与20 g/L 酵母浸粉等同。【结论】乳酸菌复合系SGL 多样性高、组成稳定、可利用无机氮源,作为青贮饲料添加剂,具有很大的应用潜力,本研究为SGL的培养和应用提供了理论依据。     

柳枝稷的生物学研究现状及其生物能源转化前景

柳枝稷(Panicum virgatum,L.)是起源于北美的一种热带草原高秆草,具有优良的草料特性和水土保持功能。因其有很大的能源利用前景,而目前全球能源紧缺,因此全世界范围内已有许多国家把研究柳枝稷转化生物能源这一利国利民的项目提到议事日程,展开了全方位的研究。这篇论文综述了柳枝稷的生物学研究现状以及其生物能源转化前景。     

盐胁迫对柳枝稷苗期生长和生理特性的影响

2010年,在人工气候室中设置了0、50、100、150和200 mmol·L-15种NaCl浓度处理,分析盐胁迫对柳枝稷苗期生长的影响.结果表明:随着NaCl浓度的增加,柳枝稷的生长明显受到抑制,株高降低、叶片变小、光合叶面积减少、净光合速率下降,干物质积累量显著降低,表现出甜土植物的特点.柳枝稷的耐盐能力较强,在200 mmol·L-1NaCl溶液中处理30 d后仍能存活,单株绿叶面积为491.9 cm2,净光合速率为0.93 μmol CO2·m-2·s-1.本试验条件下,以生长量下降50％为标准求得柳枝稷的耐盐阈值为178.6 mmol·L-1.     

水培条件下pH值对柳枝稷幼苗生长发育的影响

土壤的p H值是限制植物生长发育的一个关键因素。柳枝稷是一种可作为牧草,水土保持的多年生C4能源植物。试验在水培条件下,利用裂区试验设计,以柳枝稷品种(系)为主区,水培液p H值为副区,对反映柳枝稷幼苗生长发育状况的指标进行统计分析。结果显示,随水培液p H值的酸碱强度增大,柳枝稷不同品种(系)幼苗的分蘖数、株高、苗鲜重、根冠比、根系活力以及净光合速率都极显著降低(P0.01),而幼苗保护酶活性以及丙二醛(MDA)含量则极显著升高(P0.01)。尤其是当PH值低于5.0时,幼苗的受到的胁迫更为明显,幼苗超氧化物歧化酶(SOD)和过氧化物酶(POD)活性反而急剧下降。与酸胁迫(p H值7.0)相比,柳枝稷对碱胁迫(p H值7.0)的适应能力更强,其中以西稷2号的抗逆性表现最好。因此应用柳枝稷在边际土壤地区推广种植时,要尽量避免强酸性土壤(p H值5.0),且选用西稷2号品系较为适宜。     

木薯纤维素乙醇发酵的纤维素酶成本评价

木薯中的纤维素成分约占木薯干重的10％(W/W).文中以木薯燃料乙醇生产的木薯纤维素酒渣为原料,从纤维素酶成本角度评估了三种利用木薯纤维素组分发酵生产乙醇的方法,包括木薯纤维素酒渣的直接糖化和乙醇发酵、木薯纤维素酒渣预处理后的糖化与乙醇发酵、木薯乙醇发酵中同步淀粉与纤维素糖化以及乙醇发酵.结果表明,前两种方法的纤维素利用效率不高,酶成本分别达到13602、11659元/吨乙醇.第三种方法,即在木薯乙醇发酵过程同时加入糖化酶和纤维素酶,进行同步淀粉与纤维素糖化,进而进行乙醇发酵,木薯纤维素乙醇的收益最高.发酵结束时的乙醇浓度从101.5g/L提高到107.0g/L,纤维素酶成本为3 589元/吨乙醇.此方法利用木薯纤维素与木薯淀粉同时进行,不会带来额外的设备及操作投入,酶成本低于产品乙醇价格,可实现盈利,因此第三种方法为木薯纤维用于乙醇发酵的最适方法,本研究结果将为木薯乙醇产业深度利用木薯纤维提供依据.     

白腐真菌Pleurotus sajor-caju预处理对红麻秸秆发酵乙醇的影响

为研究微生物法预处理对红麻秸秆中木质素的降解及后续的红麻纤维素酶促糖化和发酵效率的影响,将白腐真菌Pleurotus sajor-caju接种在红麻秸秆培养基上固态培养,对红麻秸秆进行预处理。经P. sajor-caju培养25~35 d后,有效转化红麻秸秆中的木质素,转化率最高可达50.20％,并提高红麻纤维素的酶促水解效率,糖化率达69.33％~78.64％,与对照组相比提高了3.5~4.1倍。以微生物法预处理后的红麻秸秆样品为底物的同步糖化发酵实验表明,发酵72 h,发酵液中乙醇浓度达到18.35~     

以玉米秸秆为原料同步糖化发酵生产燃料乙醇

以玉米秸秆为原料,经酸法预处理后,采用同步糖化发酵SSF工艺生产燃料乙醇。正交试验获得的最佳体系为:培养温度34℃、发酵pH值5.5、发酵的液固比8:1、当发酵108h后,乙醇浓度可达8.33g/L。该实验为纤维质燃料乙醇的产业化生产提供技术依据。     

混播下柳枝稷叶绿素荧光参数及对水氮条件的响应特征

采用盆栽试验,按照白羊草(Bothriochloa ischaemum)与柳枝稷(Panicum virgatum)株数比设置5个混播比例(0∶8、2∶6、4∶4、6∶2、8∶0),在两种氮肥处理(不施氮和0.1g N·kg-1)下,测定分析柳枝稷叶绿素荧光参数对土壤水分短期自然干旱并复水[土壤含水量从80%FC(田间持水量为20%)逐渐降至20%FC后再复水至80%FC]的响应,以期揭示不同水氮及混播比例下柳枝稷与白羊草竞争关系的生理生态机制。结果显示:(1)随干旱胁迫加剧,柳枝稷最大光化学效率(Fv/Fm)、光化学猝灭(qP)、实际光化学效率(ΦPSⅡ)和表观光合量子传递速率(ETR)逐渐下降,复水后第2天各指标均可恢复到对照水平;(2)两氮肥处理下,单播柳枝稷的ETR显著高于混播,施氮处理下单播的qP显著高于混播,但非光化学猝灭系数(NPQ)相反(P0.05),且柳枝稷比例越小各指标降幅越大,表明混播后柳枝稷PSⅡ反应中心活性下降,显示出其对混播竞争的适应;(3)施氮显著提高了柳枝稷的ΦPSⅡ(13.64%~23.53%)和qP(6.12%~11.11%),降低了NPQ值(9.76%~12.82%)(P0.05),表明施氮可提高其光能利用能力,增强其与白羊草的竞争力。研究认为,不同水氮条件下,柳枝稷表现出较强的混播竞争适应性,施氮会提高其对白羊草的生态竞争能力。     

预处理苎麻秆和红麻秆糖化发酵生产燃料乙醇

苎麻和红麻是我国传统纤维作物,皮部纤维在造纸、纺织等工业具有广泛用途,但剥皮后剩余的茎秆部分并没有被有效利用。由于其中含有较多纤维素,可望被生物转化生产燃料乙醇。比较了几种不同化学预处理方法对苎麻秆和红麻秆纤维素酶解性能的改善效果,进而选择碱法预处理后原料,进行半同步糖化发酵产乙醇实验。结果表明,苎麻秆和红麻秆经4%NaOH和0.02%蒽醌-2-磺酸钠盐(AQSS),在170℃下处理1 h,继而在固形物底物浓度18%时发酵168 h,发酵液中乙醇浓度达到51 g/L。采用少量多次补料至20%的底物浓度,乙醇浓度都能达到63 g/L,纤维素转化率分别为77%和79%。红麻秆经5.2%NaHSO3和0.2%H2SO4,在170℃下处理1 h,补料至20%的底物浓度时,乙醇浓度可达到65 g/L,纤维素转化率为72%。     

不同盐胁迫对柳枝稷生物量、品质和光合生理的影响

为明确不同盐胁迫对柳枝稷生物量、品质及光合生理的影响,以无盐胁迫作为对照(CK),选取0.40%Na Cl、0.80%Na2SO4和0.80%Na HCO3进行了土柱试验。结果表明:(1)与CK相比,Na Cl、Na2SO4、Na HCO3胁迫下柳枝稷地上生物量、地下生物量、总生物量、籽粒产量及根冠比均显著降低(P0.05),总生物量分别降低49.39%、60.52%、76.45%,Na HCO3对柳枝稷的生长抑制作用最强,Na Cl最弱;(2)Na Cl胁迫下柳枝稷地上生物质灰分含量显著增高14.89%,Na2SO4胁迫下硫(S)含量显著增高262.32%,纤维素含量显著降低13.71%,Na HCO3胁迫下钾(K)含量显著增高54.95%,半纤维素含量显著增高10.87%,灰分和S含量的增高不利于柳枝稷地上生物质的燃烧利用,纤维素含量的降低和半纤维素含量的增高不利于其转化利用;(3)Na Cl、Na2SO4、Na HCO3胁迫下柳枝稷叶片净光合速率(Pn)分别显著降低21.89%、29.54%和24.59%,气孔限制因素可能是其光合作用受到抑制、生物量下降的关键因素。     

Enzymatic digestion of liquid hot water pretreated hybrid poplar

Liquid hot (LHW) water pretreatment (LHW) of lignocellulosic material enhances enzymatic conversion of cellulose to glucose by solubilizing hemicellulose fraction of the biomass, while leaving the cellulose more reactive and accessible to cellulase enzymes. Within the range of pretreatment conditions tested in this study, the optimized LHW pretreatment conditions for a 15% (wt/vol) slurry of hybrid poplar were found to be 200^oC, 10 min, which resulted in the highest fermentable sugar yield with minimal formation of sugar decomposition products during the pretreatment. The LHW pretreatment solubilized 62% of hemicellulose as soluble oligomers. Hot‐washing of the pretreated poplar slurry increased the efficiency of hydrolysis by doubling the yield of glucose for a given enzyme dose. The 15% (wt/vol) slurry of hybrid poplar, pretreated at the optimal conditions and hot‐washed, resulted in 54% glucose yield by 15 FPU cellulase per gram glucan after 120 h. The hydrolysate contained 56 g/L glucose and 12 g/L xylose. The effect of cellulase loading on the enzymatic digestibility of the pretreated poplar is also reported. Total monomeric sugar yield (glucose and xylose) reached 67% after 72 h of hydrolysis when 40 FPU cellulase per gram glucan were used. An overall mass balance of the poplar‐to‐ethanol process was established based on the experimentally determined composition and hydrolysis efficiencies of the liquid hot water pretreated poplar. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Biological pretreatment of corn stover with Phlebia brevispora NRRL‐13108 for enhanced enzymatic hydrolysis and efficient ethanol production

Biological pretreatment of lignocellulosic biomass by white‐rot fungus can represent a low‐cost and eco‐friendly alternative to harsh physical, chemical, or physico‐chemical pretreatment methods to facilitate enzymatic hydrolysis. In this work, solid‐state cultivation of corn stover with Phlebia brevispora NRRL‐13018 was optimized with respect to duration, moisture content and inoculum size. Changes in composition of pretreated corn stover and its susceptibility to enzymatic hydrolysis were analyzed. About 84% moisture and 42 days incubation at 28°C were found to be optimal for pretreatment with respect to enzymatic saccharification. Inoculum size had little effect compared to moisture level. Ergosterol data shows continued growth of the fungus studied up to 57 days. No furfural and hydroxymethyl furfural were produced. The total sugar yield was 442 ± 5 mg/g of pretreated corn stover. About 36 ± 0.6 g ethanol was produced from 150 g pretreated stover per L by fed‐batch simultaneous saccharification and fermentation (SSF) using mixed sugar utilizing ethanologenic recombinant Eschericia coli FBR5 strain. The ethanol yields were 32.0 ± 0.2 and 38.0 ± 0.2 g from 200 g pretreated corn stover per L by fed‐batch SSF using Saccharomyces cerevisiae D5A and xylose utilizing recombinant S. cerevisiae YRH400 strain, respectively. This research demonstrates that P. brevispora NRRL‐13018 has potential to be used for biological pretreatment of lignocellulosic biomass. This is the first report on the production of ethanol from P. brevispora pretreated corn stover. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:365–374, 2017     

Dilute acid pretreatment, enzymatic saccharification and fermentation of wheat straw to ethanol

Wheat straw consists of 48.57 ± 0.30% cellulose and 27.70 ± 0.12% hemicellulose on dry solid (DS) basis and has the potential to serve as a low cost feedstock for production of ethanol. Dilute acid pretreatment at varied temperature and enzymatic saccharification were evaluated for conversion of wheat straw cellulose and hemicellulose to monomeric sugars. The maximum yield of monomeric sugars from wheat straw (7.83%, w/v, DS) by dilute H₂SO₄ (0.75%, v/v) pretreatment and enzymatic saccharification (45 °C, pH 5.0, 72 h) using cellulase, β-glucosidase, xylanase and esterase was 565 ± 10 mg/g. Under this condition, no measurable quantities of furfural and hydroxymethyl furfural were produced. The yield of ethanol (per litre) from acid pretreated enzyme saccharified wheat straw (78.3 g) hydrolyzate by recombinant Escherichia coli strain FBR5 was 19 ± 1 g with a yield of 0.24 g/g DS. Detoxification of the acid and enzyme treated wheat straw hydrolyzate by overliming reduced the fermentation time from 118 to 39 h in the case of separate hydrolysis and fermentation (35 °C, pH 6.5), and increased the ethanol yield from 13 ± 2 to 17 ± 0 g/l and decreased the fermentation time from 136 to 112 h in the case of simultaneous saccharification and fermentation (35 °C, pH 6.0).     

Dry biorefining maximizes the potentials of simultaneous saccharification and co‐fermentation for cellulosic ethanol production

Despite the well‐recognized merits of simultaneous saccharification and co‐fermentation (SSCF) on relieving sugar product inhibition on cellulase activity, a practical concomitance difficulty of xylose with inhibitors in the pretreated lignocellulose feedstock prohibits the essential application of SSCF for cellulosic ethanol fermentation. To maximize the SSCF potentials for cellulosic ethanol production, a dry biorefining approach was proposed starting from dry acid pretreatment, disk milling, and biodetoxification of lignocellulose feedstock. The successful SSCF of the inhibitor free and xylose conserved lignocellulose feedstock after dry biorefining reached a record high ethanol titer at moderate cellulase usage and minimum wastewater generation. For wheat straw, 101.4 g/L of ethanol (equivalent to 12.8% in volumetric percentage) was produced with the overall yield of 74.8% from cellulose and xylose, in which the xylose conversion was 73.9%, at the moderate cellulase usage of 15 mg protein per gram cellulose. For corn stover, 85.1 g/L of ethanol (equivalent to 10.8% in volumetric percentage) is produced with the overall conversion of 84.7% from cellulose and xylose, in which the xylose conversion was 87.7%, at the minimum cellulase usage of 10 mg protein per gram cellulose. Most significantly, the SSCF operation achieved the high conversion efficiency by generating the minimum amount of wastewater. Both the fermentation efficiency and the wastewater generation in the current dry biorefining for cellulosic ethanol production are very close to that of corn ethanol production, indicating that the technical gap between cellulosic ethanol and corn ethanol has been gradually filled by the advancing biorefining technology.     

白腐菌协同热水预处理对毛白杨化学组分和酶水解效果的影响

【目的】增强真菌预处理的效率和降低热水预处理对反应条件的要求。【方法】综合利用白腐菌和热水预处理毛白杨,分析此方法对毛白杨化学组分和酶水解效果的影响。【结果】白腐菌Lenzites betulinus C5617协同热水处理,损失率最高达70.70%。纤维素在2个预处理阶段都有损失,其中L.betulinus C5617达到29.62%。木质素的降解主要集中在白腐菌预处理阶段,其中L.betulinus C5617降解的酸不溶木素较多,达到了16.98%。综合预处理显著改善了毛白杨的酶水解效果。与只经热水预处理的样品相比较,L.betulinus C5617和P.sanguineus D9497协同热水处理分别引起还原糖得率上升了20.60%和12.23%。【结论】综合预处理降低了热水解对反应条件的要求,节约了预处理成本。     

High solid simultaneous saccharification and fermentation of wet oxidized corn stover to ethanol

In this study ethanol was produced from corn stover pretreated by alkaline and acidic wet oxidation (WO) (195 degrees C, 15 min, 12 bar oxygen) followed by nonisothermal simultaneous saccharification and fermentation (SSF). In the first step of the SSF, small amounts of cellulases were added at 50 degrees C, the optimal temperature of enzymes, in order to obtain better mixing condition due to some liquefaction. In the second step more cellulases were added in combination with dried baker's yeast (Saccharomyces cerevisiae) at 30 degrees C. The phenols (0.4-0.5 g/L) and carboxylic acids (4.6-5.9 g/L) were present in the hemicellulose rich hydrolyzate at subinhibitory levels, thus no detoxification was needed prior to SSF of the whole slurry. Based on the cellulose available in the WO corn stover 83% of the theoretical ethanol yield was obtained under optimized SSF conditions. This was achieved with a substrate concentration of 12% dry matter (DM) acidic WO corn stover at 30 FPU/g DM (43.5 FPU/g cellulose) enzyme loading. Even with 20 and 15 FPU/g DM (corresponding to 29 and 22 FPU/g cellulose) enzyme loading, ethanol yields of 76 and 73%, respectively, were obtained. After 120 h of SSF the highest ethanol concentration of 52 g/L (6 vol.%) was achieved, which exceeds the technical and economical limit of the industrial-scale alcohol distillation. The SSF results showed that the cellulose in pretreated corn stover can be efficiently fermented to ethanol with up to 15% DM concentration. A further increase of substrate concentration reduced the ethanol yield significant as a result of insufficient mass transfer. It was also shown that the fermentation could be followed with an easy monitoring system based on the weight loss of the produced CO2.     

Effect of hot water extraction and liquid hot water pretreatment on the fungal degradation of biomass feedstocks

Exhaustive hot water extraction (HWE) and liquid hot water (LHW) pretreatment were evaluated for their effects on degradation of biomass feedstocks (i.e., corn stover, wheat straw, and soybean straw) by Ceriporiopsis subvermispora. HWE (85 °C for 10 min) partially removed water soluble extractives and subsequently improved fungal degradation on wheat straw while it had little or no effect on the fungal degradation of corn stover and soybean straw. In contrast, LHW pretreatment at 170 °C for 3 min improved the fungal degradation of soybean straw; thus, lignin removal of 36.70% and glucose yield of 64.25% were obtained from the combined LHW and fungal pretreatment. However, corn stover, which was effectively degraded by fungal pretreatment alone, was less affected by this combined pretreatment. Our results indicated that a HWE or LHW pretreatment conducted under mild conditions worked synergistically with fungal degradation for some recalcitrant feedstocks.