生物质热裂解生产生物燃料的研究进展

生物质能源是一种绿色的可以替代化石能源的一种可再生的能源。尽管高温分解生物质处于发展阶段,但在目前水平,高温裂解因其可以在氧存在下热分解将生物材料直接转化为固态,液态和气态能源产品而受到广泛关注。本文介绍了生物质的热裂解,包括慢速热裂解、快速热裂解、闪解、催化热裂解等过程,重点讨论了在各种生物质材料的热裂解过程中各种操作参数如温度和生物粒子大小等对生物燃料收率的影响。     

盐胁迫下氯丙嗪和LaCl3对稻苗K^＋、Na^＋、Cl^—吸收转运的影响

研究了氯丙嗪（CPZ）和LaCl3预处理阻碍Ca^2 。CaM信使系统传导后,盐胁迫下稻苗体内Na^ 、K^ 和Cl^-含量及吸收转运的变化。结果表明：CPZ和LaCl3预处理后,盐胁迫下稻苗对K^ /Na^ 的选择性吸收下降,致使稻苗K^ 含量减少、Na^ 含量增加,Na^ /K^ 比值显著增加;并且稻苗地上部Cl^-含量也显著增加,盐胁迫处理稻苗2d后解除盐胁迫,改用蒸馏水培养,在蒸馏水中加入CPZ或LaCl3时,稻苗中含有较高的Na^ ,即CPZ和LaCl3抑制稻苗将体内Na^ 排出体外的能力,上述结果表明,盐胁迫下,Ca^2 .CaM信使系统可能参与稻苗对K^ 、Na^ 和Cl^-的吸收转运以适应盐胁迫。     

盐胁迫下氯丙嗪和LaCl_3对稻苗K~ 、Na~ 、Cl~-吸收转运的影响

研究了氯丙嗪 (CPZ)和LaCl3 预处理阻碍Ca2 ·CaM信使系统传导后 ,盐胁迫下稻苗体内Na 、K 和Cl-含量及吸收转运的变化 ,结果表明 :CPZ和LaCl3 预处理后 ,盐胁迫下稻苗对K /Na 的选择性吸收下降 ,致使稻苗K 含量减少、Na 含量增加 ,Na /K 比值显著增加 ;并且稻苗地上部Cl-含量也显著增加。盐胁迫处理稻苗 2d后解除盐胁迫 ,改用蒸馏水培养 ,在蒸馏水中加入CPZ或LaCl3 时 ,稻苗中含有较高的Na ,即CPZ和LaCl3 抑制稻苗将体内Na 排出体外的能力。上述结果表明 ,盐胁迫下 ,Ca2 ·CaM信使系统可能参与稻苗对K 、Na 和Cl-的吸收转运以适应盐胁迫     

固定化脂肪酶催化毛棉籽油制备生物柴油

研究了固定化脂肪酶Lipozyme TL IM和Novozym435催化毛棉籽油和乙酸甲酯制备生物柴油的过程。通过向反应体系中添加甲醇,可减少乙酸的抑制,明显提高生物柴油得率,确定最佳反应条件为:正己烷作溶剂,乙酸甲酯与油摩尔比9:1,添加油重3%的甲醇、油重10%的LipozymeTLIM和5%的Novozym435复合使用,温度55°C,反应8h,生物柴油得率达到91.83%。最后探索了酶催化毛棉籽油合成生物柴油的动力学,得到动力学方程。     

ZSM-5(38)/Al-MCM-41复合分子筛对纤维素催化热解的影响

以纤维素为原料,以自制的不同硅铝比ZSM-5(38)/Al-MCM-41微-介孔复合分子筛为催化剂,在固定床反应器上进行了催化热解实验。采用XRD表征分子筛,采用GC-MS分析生物油成分,考查了催化剂的改变对生物质热解产物及生物油成分的影响。实验结果表明:添加催化剂后,生物油产率降低,且其含水率也有所增加。与未添加催化剂相比,生物油中D L-2,3-丁二醇有明显提高。其中,ZSM-5(38)/Al-MCM-41(20)最有利于苯酚、愈创木酚(2-甲氧基-苯酚)的生成。此外,这几种催化剂均有利于小分子化合物的生成,其中,ZSM-5(38)有利于C4~C5化合物的生成,微-介孔复合分子筛则有利于C6~C8化合物的生成。     

应用树脂吸附分离制取茶多酚

从茶中分离制取天然抗氧化剂茶多酚,现行工业化生产多采用有机溶剂萃取和金属盐沉淀法,这两种方法,工艺繁琐,有机溶剂、金属盐或酸、碱损耗大,严重污染环境,提取率低、得率低、成本高、销售困难。笔者采用大孔吸附树脂层析法从茶中分离,纯化茶多酚,制得低含咖啡碱的茶多酚粗制品,得率为１８％～２１％,纯度≥７０％,ＥＧＣＧ＞２０％,咖啡碱＜２％。吸附树脂具有表面积大,吸附量大,吸附与洗脱高峰集中,不用或少用除乙醇外的有机溶剂,洗脱与再生容易,成本低,得率高等优点,大有开发前景。     

ZSM-5(38)/Al-MCM-41复合分子筛对纤维素催化热解的影响

以纤维素为原料,以自制的不同硅铝比ZSM-5(38)/Al-MCM-41微-介孔复合分子筛为催化剂,在固定床反应器上进行了催化热解实验。采用XRD表征分子筛,采用GC-MS分析生物油成分,考查了催化剂的改变对生物质热解产物及生物油成分的影响。实验结果表明：添加催化剂后,生物油产率降低,且其含水率也有所增加。与未添加催化剂相比,生物油中D L-2,3-丁二醇有明显提高。其中,ZSM-5(38)/Al-MCM-41(20) 最有利于苯酚、愈创木酚 (2-甲氧基-苯酚) 的生成。此外,这几种催化剂均有利于小分子化合物的生成,其中,ZSM-5(38) 有利于C4~C5化合物的生成,微-介孔复合分子筛则有利于C6~C8化合物的生成。     

新书介绍

生物油制备技术与应用 作者基于多年的研究积累编写了本书,全书构成了一套完整的生物质热解与生物油制备的技术体系。共分八章,第一章讲述我国的能源形势和生物质能特点;第二章讲述生物质的组成、结构和性质;第三章讲述生物质的热解原理;第四章讲述生物油制备技术;第五章讲述生物油的组成和性质;第六章讲述生物油的品质改良与燃烧应用;第七章讲述生物油的分离与精制;第八章讲述生物油水蒸气重整制氢。     

三种粪便总DNA提取方法的比较

目的比较不同粪便总DNA提取方法对肠道菌群多样性研究的影响。方法采用Bead beating法、化学裂解法和QIAamp DNA Stool Mini Kit提取同一份人粪便样品的总DNA,对比3种方法的DNA得率和16S rRNA基因V3区的变性梯度凝胶电泳（DGGE）图谱。结果Bead beating法的DNA得率约是其他2种方法的2倍;3种方法得到的DGGE图谱的Dice相似性为60％～70％,2条优势条带只出现在Bead beating法图谱中。在2～5min的Bead beating法击打时间里,DNA得率随击打时间的延长有一定的增加,但DGGE图谱无显著变化。结论不同的DNA提取方法会影响菌群的多样性分析。比较其他2种方法,Bead beating的裂解效率更高,能够检测到更多种类的细菌,更合适肠道菌群组成的分子研究。     

基于钙基催化剂的生物质焦油催化裂解试验

生物质气化技术是生物质高值利用的重要技术之一，然而却存在副产品焦油难以处理的问题。为了解决生物质气化过程中副产品焦油的问题，以钙基催化剂为床料，在流化床反应器内开展焦油催化裂解试验。结果表明，钙基催化剂对焦油裂解具有很好的催化作用，可显著提高焦油裂解效率；流化床的操作条件对生物质焦油的催化裂解过程产生了重要影响，即操作温度越高，焦油裂解效率也越高，加入适当比例的水蒸气可以提高焦油裂解效率，且能增大产品气的产量。研究结果显示，添加钙基催化剂后，理想的操作温度为850℃，水蒸气与焦油质量比例为5∶1。研究结果为焦油的再利用相关研究提供了参考。     

Steam reforming of bio-oil from rice husks fast pyrolysis for hydrogen production

Steam reforming of two kinds of bio-oil from rice husks fast pyrolysis was conducted for hydrogen production at three temperatures (650, 750 and 850 °C) with Ni-based catalyst in a fixed-bed reactor. The gas composition and organic compounds in liquid condensate were detected by gas chromatography (GC) and gas chromatography-mass spectrometry (GC-MS), respectively. In addition, the carbon deposition was also investigated. The results showed that the mole fraction range of hydrogen was within 55.8-61.3% at all temperatures and more hydrogen was produced at the higher temperature. The highest H? efficiency of bio-oil steam reforming was 45.33% when extra water was added. The bio-oil with lower content of chemical compounds has a higher H? efficiency, but its hydrogen volume was less. Analysis of the liquid condensate showed that most of the organic compounds were circularity compounds. The carbon deposition can decrease the bio-oil conversion, and it was easier to form at the temperature of 750 °C.     

Subcritical Water Hydrolysis of Microalgal Biomass for Protein and Pyrolytic Bio-oil Recovery

Microalgae are a promising source of protein and biofuels. This study involved the extraction of soluble proteins from raw microalgae using subcritical water hydrolysis followed by pyrolysis of the resulting spent microalgal biomass for bio-oil production. The extraction process produced solubilized protein in amounts up to 10 wt% of the dry biomass. The effects of hydrolysis temperature (150–220 °C), process time (90–180 min), and initial pH (2–12) on the chemical compositions and reactivity of the spent biomass as biofuel intermediates were investigated. It was found that when the temperature and time increased, the protein and carbohydrate fractions of the spent biomass were reduced, while their lipid fraction increased. A low initial pH led to lower protein content in the spent biomass. Compared with the raw microalgae, the spent biomass gave a higher yield of pyrolytic bio-oil that contained much less of the N-containing compounds and higher amounts of long-chain fatty acids (C₁₆) and C₁₄–C₂₀ long-chain hydrocarbons. In addition, enhanced energy recovery and a reduction in the energy consumption of the pyrolysis process were the other benefits acquired from the protein extraction. Therefore, subcritical water hydrolysis was considered to be an effective process to recover solubilized proteins, enhance the properties of the spent biomass, improve the energy balance of the subsequent pyrolysis process, and raise the quality of the bio-oil.     

High yield bio-oil production from fast pyrolysis by metabolic controlling of Chlorella protothecoides

The use of renewable energy sources is becoming increasingly necessary to mitigate global warming. Recently much research has been focused on identifying suitable biomass species, which can provide high-energy outputs, to replace conventional fossil fuels. This paper reports an approach for increasing the yield of bio-oil production from fast pyrolysis after manipulating the metabolic pathway in microalgae through heterotrophic growth. The yield of bio-oil (57.9%) produced from heterotrophic Chlorella protothecoides cells was 3.4 times higher than from autotrophic cells by fast pyrolysis. The bio-oil was characterized by a much lower oxygen content, with a higher heating value (41 MJ kg(-1)), a lower density (0.92 kg l(-1)), and lower viscosity (0.02 Pas) compared to those of bio-oil from autotrophic cells and wood. These properties are comparable to fossil oil. The research could contribute to the creation of a system to produce energy from microalgae, and also could have great commercial potential for liquid fuel production.     

The characteristics of bio-oil produced from the pyrolysis of three marine macroalgae

The pyrolysis of two brown macroalgae (Undaria pinnatifida and Laminaria japonica) and one red macroalgae (Porphyra tenera) was investigated for the production of bio-oil within the temperature range of 300-600°C. Macroalgae differ from lignocellulosic land biomass in their constitutional compounds and high N, S and ash contents. The maximum production of bio-oil was achieved at 500°C, with yields between 37.5 and 47.4 wt.%. The main compounds in bio-oils vary between macroalgae and are greatly different from those of land biomass, especially in the presence of many nitrogen-containing compounds. Of the gaseous products, CO(2) was dominant, while C(1)-C(4) hydrocarbons gradually increasing at 400°C and above. The pretreatment of macroalgae by acid washing effectively reduced the ash content. The pyrolysis of macroalgae offers a new opportunity for feedstock production; however, the utilization of bio-oil as a fuel product needs further assessment.     

Impact of Harvest Time and Cultivar on Conversion of Switchgrass to Bio-oils Via Fast Pyrolysis

The study of the effects of harvest time on switchgrass (Panicum virgatum L.) biomass and bioenergy production reported herein encompasses a large study evaluating the harvest of six switchgrass cultivars grown at three northern US locations over 3 years, harvested at upland peak crop (anthesis), post-frost, and post-winter. Delaying harvest of switchgrass until after frost and until after winter has resulted in decreased yields of switchgrass and reduced amounts of minerals in the biomass. This report examines how changes in biomass composition as a result of varying harvest time and other factors affect the distribution of products formed via fast pyrolysis. A subset (50) of the population (n = 864) was analyzed for fast pyrolysis and catalytic pyrolysis (zeolite catalyst) product yields using a pyrolysis-GC/MS system. The subset was used to build calibrations that were successful in predicting the pyrolysis product yield using near-infrared reflectance spectroscopy (NIRS), and partial least squares predictive models were applied to the entire sample set. The pyrolysis product yield was significantly affected by the field trial location, year of harvest, cultivar, and harvest time. Delaying harvest time of the switchgrass crop led to greater production of deoxygenated aromatics improving the efficiency of the catalytic fast pyrolysis and bio-oil quality. The changes in the pyrolysis product yield were related to biomass compositional changes, and key relationships between cell wall polymers, potassium concentration in the biomass, and pyrolysis products were identified. The findings show that the loss of minerals in the biomass as harvest time is delayed combined with the greater proportion in cellulose and lignin in the biomass has significant positive influences on conversion through fast pyrolysis.     

Effect of hot vapor filtration on the characterization of bio-oil from rice husks with fast pyrolysis in a fluidized-bed reactor

To produce high quality bio-oil from biomass using fast pyrolysis, rice husks were pyrolyzed in a 1-5 kg/h bench-scale fluidized-bed reactor. The effect of hot vapor filtration (HVF) was investigated to filter the solid particles and bio-char. The results showed that the total bio-oil yield decreased from 41.7% to 39.5% by weight and the bio-oil had a higher water content, higher pH, and lower alkali metal content when using HVF. One hundred and twelve different chemical compounds were detected by gas chromatography-mass spectrometry (GC-MS). The molecular weight of the chemical compounds from the condenser and the EP when the cyclone was coupled with HVF in the separation system decreased compared with those from the condenser and EP when only cyclone was used.     

Biomass fast pyrolysis in a fluidized bed reactor under N2, CO2, CO, CH4 and H2 atmospheres

Biomass fast pyrolysis is one of the most promising technologies for biomass utilization. In order to increase its economic potential, pyrolysis gas is usually recycled to serve as carrier gas. In this study, biomass fast pyrolysis was carried out in a fluidized bed reactor using various main pyrolysis gas components, namely N₂, CO₂, CO, CH₄ and H₂, as carrier gases. The atmosphere effects on product yields and oil fraction compositions were investigated. Results show that CO atmosphere gave the lowest liquid yield (49.6%) compared to highest 58.7% obtained with CH₄. CO and H₂ atmospheres converted more oxygen into CO₂ and H₂O, respectively. GC/MS analysis of the liquid products shows that CO and CO₂ atmospheres produced less methoxy-containing compounds and more monofunctional phenols. The higher heating value of the obtained bio-oil under N₂ atmosphere is only 17.8 MJ/kg, while that under CO and H₂ atmospheres increased to 23.7 and 24.4 MJ/kg, respectively.     

Crop Management Impacts Biofuel Quality: Influence of Switchgrass Harvest Time on Yield, Nitrogen and Ash of Fast Pyrolysis Products

Although upgrading bio-oil from fast pyrolysis of biomass is an attractive pathway for biofuel production, nitrogen (N) and mineral matter carried over from the feedstock to the bio-oil represents a serious contaminant in the process. Reducing the N and ash content of biomass feedstocks would improve process reliability and reduce production costs of pyrolytic biofuels. This study investigated: (1) How does switchgrass harvest date influence the yield, N concentration ([N]), and ash concentration of biomass and fast pyrolysis products? and (2) Is there a predictive relationship between [N] of switchgrass biomass and [N] of fast pyrolysis products? Switchgrass from five harvest dates and varying [N] from central Iowa were pyrolyzed using a free-fall reactor. Harvestable biomass peaked in August (8.6 Mg ha^?1), dropping significantly by November (6.7 Mg ha^?1, P?=?0.0027). Production of bio-oil per unit area mirrored that of harvested biomass at each harvest date; however, bio-oil yield per unit dry biomass increased from 46.6 % to 56.7 % during the season (P?=?0.0018). Allowing switchgrass to senesce lowered biomass [N] dramatically, by as much as 68 % from June to November (P?<?0.0001). Concurrently, bio-oil [N] declined from 0.51 % in June to 0.17 % by November (P?<?0.0001). Significant reductions in ash concentration were also observed in biomass and char. Finally, we show for the first time that the [N] of switchgrass biomass is a strong predictor of the [N] of bio-oil, char, and non-condensable gas with R ² values of 0.89, 0.94, and 0.88, respectively.     

Microwave pyrolysis of distillers dried grain with solubles (DDGS) for biofuel production

Microwave pyrolysis of distillers dried grain with solubles (DDGS) was investigated to determine the effects of pyrolytic conditions on the yields of bio-oil, syngas, and biochar. Pyrolysis process variables included reaction temperature, time, and power input. Microwave pyrolysis of DDGS was analyzed using response surface methodology to find out the effect of process variables on the biofuel (bio-oil and syngas) conversion yield and establish prediction models. Bio-oil recovery was in the range of 26.5-50.3 wt.% of the biomass. Biochar yields were 23.5-62.2% depending on the pyrolysis conditions. The energy content of DDGS bio-oils was 28 MJ/kg obtained at the 650 °C and 8 min, which was about 66.7% of the heating value of gasoline. GC/MS analysis indicated that the biooil contained a series of important and useful chemical compounds: aliphatic and aromatic hydrocarbons. At least 13% of DDGS bio-oil was the same hydrocarbon compounds found in regular unleaded gasoline.     

Fast Pyrolysis Behavior of Banagrass as a Function of Temperature and Volatiles Residence Time in a Fluidized Bed Reactor

A reactor was designed and commissioned to study the fast pyrolysis behavior of banagrass as a function of temperature and volatiles residence time. Four temperatures between 400 and 600°C were examined as well as four residence times between ~1.0 and 10 seconds. Pyrolysis product distributions of bio-oil, char and permanent gases were determined at each reaction condition. The elemental composition of the bio-oils and chars was also assessed. The greatest bio-oil yield was recorded when working at 450°C with a volatiles residence time of 1.4 s, ~37 wt% relative to the dry ash free feedstock (excluding pyrolysis water). The amounts of char (organic fraction) and permanent gases under these conditions are ~4 wt% and 8 wt% respectively. The bio-oil yield stated above is for ''dry'' bio-oil after rotary evaporation to remove solvent, which results in volatiles and pyrolysis water being removed from the bio-oil. The material removed during drying accounts for the remainder of the pyrolysis products. The ''dry'' bio-oil produced under these conditions contains ~56 wt% carbon which is ~40 wt% of the carbon present in the feedstock. The oxygen content of the 450°C, 1.4 s ''dry'' bio-oil is ~38 wt%, which accounts for ~33 wt% of the oxygen in the feedstock. At higher temperature or longer residence time less bio-oil and char is recovered and more gas and light volatiles are produced. Increasing the temperature has a more significant effect on product yields and composition than increasing the volatiles residence time. At 600°C and a volatiles residence time of 1.2 seconds the bio-oil yield is ~21 wt% of the daf feedstock, with a carbon content of 64 wt% of the bio-oil. The bio-oil yield from banagrass is significantly lower than from woody biomass or grasses such as switchgrass or miscanthus, but is similar to barley straw. The reason for the low bio-oil yield from banagrass is thought to be related to its high ash content (8.5 wt% dry basis) and high concentration of alkali and alkali earth metals (totaling ~2.8 wt% relative to the dry feedstock) which are catalytic and increase cracking reactions during pyrolysis.