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1.
热解温度对酸沉淀工业木质素快速热解液体产物的影响 总被引:1,自引:0,他引:1
利用快速热解和气质联用技术,研究了酸沉淀工业木质素在400℃~700℃下快速热解液体产物的主要组分及其含量的变化。酸沉淀工业木质素快速热解液体产物中主要包括,与木质素的三种苯丙烷结构单元结构相似的苯酚、愈疮木酚和2,6 二甲氧基苯酚等酚类化合物,以及它们的甲基、乙基或丙基的单取代或多取代衍生物。在400℃~600℃,热解液体产物的组分及其相对含量的变化不显著;而在600℃~700℃,芳环上含甲氧基的酚类物质的相对含量急剧减少甚至消失,而苯酚的相对含量却急剧增加,达到27.81%,比400℃的增加了近2.5倍,同时芳烃化合物的相对含量增加,并出现苯丙呋喃、茚和萘等芳环化合物。 相似文献
2.
采用热裂解-气相色谱/质谱仪联用技术,研究毛竹酶解/温和酸水解木质素(简称EMAL)的热解特性和热解产物的分布与形成规律.以温度为重要因素,研究其对木质素快速热裂解产物的影响,并通过主要的热解产物推断热解反应途径.研究结果表明,EMAL的热解产物主要是2,3-二氢苯并呋喃、酚类、脂类和少量乙酸.热解温度对热解产物组分的相对含量有显著影响,250~400 ℃时,产物主要是2,3-二氢苯并呋喃,320 ℃时其相对含量最高,达到66.26%;400~800 ℃时,热解产物主要是酚类,600 ℃时其相对含量最高,达到62.58%;800 ℃时出现了少量的乙酸. 相似文献
3.
利用快速升温固定床进行了霍林河褐煤在CO气氛下快速热解反应行为的研究,考察了热解半焦的产率、性质和气体产物的分布特点。半焦的红外光谱图、元素含量和表面结构性质分析表明,CO参与并改变了褐煤的热解行为。与N2气氛相比,热解温度低于600 ℃时,带孤对电子的极性CO容易诱发半焦结构中芳香环的开裂,侧链、醚键和脂肪链的断裂,促进小分子片段和自由基的生成,自由基稳定了煤热解生成的碎片,导致挥发分的生成和逸出量增加,H2、CH4、CO和CO2的产率增大,半焦产率降低,半焦的比表面积和孔容增大。热解温度高于700 ℃时,CO的歧化反应程度增大,产生的积碳附着于半焦的表面,阻塞了孔道,导致半焦的比表面积和孔容减小,从而抑制了CO在半焦孔隙结构内部的扩散,限制了CO与煤中有机大分子结构的接触和反应,导致H2、CH4和CO产率减小,而CO2产率因CO歧化反应而增大。 相似文献
4.
Cornstalk lignin was hydrothermally depolymerized at mild conditions in ethanol–water for producing value-added phenolics. The effects of residence time (from 30 min to 180 min), reaction temperature (from 498 K to 573 K) and concentration of ethanol (from 0% to 95% vol.) on yields of liquid products and phenolic compounds were studied in detail. The optimal conditions of 523 K, 90 min and 65% vol. ethanol–water resulted in the highest yield of liquid products (∼70 wt.%). The liquid products were analyzed by gas chromatography–mass spectrometry (GC–MS) to confirm the presence of primarily heterocycle (2,3-dihydrobenzofuran) and phenolics (such as ethylphenol, guaiacol, ethylguaiacol and syringol). Reaction conditions had significant effects on yield and composition of liquid products. 相似文献
5.
In the research, thermogravimetry (TG), a combination of thermogravimetry and Fourier transform infrared spectrometer (TG–FTIR) and X-ray diffraction (XRD) were used to investigate pyrolysis characteristics of moso bamboo (Phyllostachys pubescens). The Flynn–Wall–Ozawa and Coats–Redfern (modified) methods were used to determine the apparent activation energy (Ea). The TG curve indicated that the pyrolysis process of moso bamboo included three steps and the main pyrolysis occurred in the second steps with temperature range from 450 K to 650 K and over 68.69% mass was degraded. TG–FTIR analysis showed that the main pyrolysis products included absorbed water (H2O), methane gas (CH4), carbon dioxide (CO2), acids and aldehydes, ammonia gas (NH3), etc. XRD analysis expressed that the index and width crystallinity of moso bamboo gradually increased from 273 K to 538 K and cellulose gradually degraded from amorphous region to crystalline region. The Ea values of moso bamboo increased with conversion rate increase from 10 to 70. The Ea values were, respectively 153.37–198.55 kJ/mol and 152.14–197.87 kJ/mol based on Flynn–Wall–Ozawa and Coats–Redfern (modified) methods. The information was very helpful and significant to design manufacturing process of bio-energy, made from moso bamboo, using gasification or pyrolysis methods. 相似文献
6.
竹材非等温热解动力学 总被引:1,自引:0,他引:1
利用热重分析技术对竹材在高纯N2条件下,从室温至1273K进行了非等温热解分析,研究了升温速率(5、10、20和40K/min)对热解过程的影响,探讨了其热解机理。研究表明,竹材非等温热解过程主要分为失水干燥、快速热解和缓慢分解三个阶段组成,其中第二阶段是整个过程的主要阶段,析出大量挥发分造成明显失重。升温速率对热解过程有显著影响,随着升温速率的增加,最大热解速度增大,对应的峰值温度升高,热滞后现象加重,热解各阶段向高温侧移动。热解机理满足一维扩散Parabolic法则,反应机理函数为g(α)=α2。不同升温速率下活化能为75.32-82.99kJ.mol-1,指前因子为1.17×105-1.12×106min-1。 相似文献
7.
氧还原反应是燃料电池及金属空气电池中极其重要的电化学反应之一,贵金属铂基催化剂被认为是最有效的氧还原反应电催化剂.然而,贵金属铂的资源稀缺以及高成本问题阻碍了相关技术的大规模应用,探索发展廉价高效的贵金属替代型催化剂是推动燃料电池发展的根本解决方案.近年来,人们在非贵金属催化剂开发方面取得了显著进展,其中新型纳米结构掺杂炭材料研究尤为活跃.氮杂有序介孔炭材料由于其高比表面积和独特的孔结构,在燃料电池技术上具有广泛的应用前景.在氮杂有序介孔炭材料的制备过程中,热解条件对炭材料组成、结构及电催化性能有着重要影响.然而,目前尚未见对氮杂炭材料制备过程中热解条件的影响进行系统研究.
本文采用我们发展的蒸汽化-毛细管冷凝法,以SBA-15为硬模板浸渍前驱体吡咯,制备出具有高比表面积和独特孔结构的氮杂有序介孔炭材料,系统研究了热解条件(包括热解温度、热解时间和升温速率)对炭材料组成、结构及电催化性能的影响,采用N2吸附-脱附等温线、X射线光电子能谱(XPS)及Raman光谱等方法考察了氮杂有序介孔炭材料的结构和组成,采用循环伏安法与旋转环盘电极研究了其电化学行为与氧还原反应电催化活性及选择性.
N2吸附-脱附等温线显示,氮杂炭材料对应IV型吸附-脱附等温线,孔径主要分布在2–10 nm,表明所制材料具有介孔结构.随着热处理温度升高,氮杂有序介孔炭材料比表面积先增加而后降低,热处理时间的延长有利于比表面积增大,但升温速率对所制炭材料比表面积没有明显影响,当升温速率为30 oC/min,900 oC焙烧3 h时,氮杂有序介孔炭材料的比表面积达到最大值888 m2/g. XPS测试结果表明,随着热处理温度升高,氮杂有序介孔炭材料中含氮基团的分解进一步加深,使N含量逐渐降低.延长热处理时间亦然,而升温速率的改变对N含量无明显影响.在热处理温度较低时(600 oC),所得材料中N主要以吡咯氮和吡啶氮的形式存在;当温度达到800 oC以上,吡咯氮转化为吡啶氮和骨架氮,且主要以骨架氮形式存在,说明氮杂有序介孔炭材料的石墨化程度逐渐升高. Raman光谱结果显示,随着热处理温度升高, ID/IG逐渐降低,进一步印证了温度对石墨化程度的影响.
电化学测试结果表明,随着热处理温度升高,氮杂有序介孔炭材料的氧还原反应电催化活性逐渐升高,但是当热处理温度从900 oC升至1000 oC时,氧还原反应活性增加很小;升温速率与热处理时间对氧还原反应电催化活性的影响均不明显.与商品Pt/C催化剂相比,900 oC以上所制催化剂均表现出更优异的氧还原电催化活性与选择性.由此可见,热处理温度是决定碳源热化学行为的关键因素,进而决定炭材料表面组成与结构.电化学研究结果表明,800 oC以上进行热处理碳化,所生成石墨化微晶可有效促进电子传递,降低欧姆极化损失,同时,较高的处理温度可促进骨架氮掺杂,从而构建出高效氧还原反应活性位点.因此,氮杂型炭催化剂的组成、结构与电化学性能更多地受控于热处理过程中的热力学,而非热解动力学过程. 相似文献
本文采用我们发展的蒸汽化-毛细管冷凝法,以SBA-15为硬模板浸渍前驱体吡咯,制备出具有高比表面积和独特孔结构的氮杂有序介孔炭材料,系统研究了热解条件(包括热解温度、热解时间和升温速率)对炭材料组成、结构及电催化性能的影响,采用N2吸附-脱附等温线、X射线光电子能谱(XPS)及Raman光谱等方法考察了氮杂有序介孔炭材料的结构和组成,采用循环伏安法与旋转环盘电极研究了其电化学行为与氧还原反应电催化活性及选择性.
N2吸附-脱附等温线显示,氮杂炭材料对应IV型吸附-脱附等温线,孔径主要分布在2–10 nm,表明所制材料具有介孔结构.随着热处理温度升高,氮杂有序介孔炭材料比表面积先增加而后降低,热处理时间的延长有利于比表面积增大,但升温速率对所制炭材料比表面积没有明显影响,当升温速率为30 oC/min,900 oC焙烧3 h时,氮杂有序介孔炭材料的比表面积达到最大值888 m2/g. XPS测试结果表明,随着热处理温度升高,氮杂有序介孔炭材料中含氮基团的分解进一步加深,使N含量逐渐降低.延长热处理时间亦然,而升温速率的改变对N含量无明显影响.在热处理温度较低时(600 oC),所得材料中N主要以吡咯氮和吡啶氮的形式存在;当温度达到800 oC以上,吡咯氮转化为吡啶氮和骨架氮,且主要以骨架氮形式存在,说明氮杂有序介孔炭材料的石墨化程度逐渐升高. Raman光谱结果显示,随着热处理温度升高, ID/IG逐渐降低,进一步印证了温度对石墨化程度的影响.
电化学测试结果表明,随着热处理温度升高,氮杂有序介孔炭材料的氧还原反应电催化活性逐渐升高,但是当热处理温度从900 oC升至1000 oC时,氧还原反应活性增加很小;升温速率与热处理时间对氧还原反应电催化活性的影响均不明显.与商品Pt/C催化剂相比,900 oC以上所制催化剂均表现出更优异的氧还原电催化活性与选择性.由此可见,热处理温度是决定碳源热化学行为的关键因素,进而决定炭材料表面组成与结构.电化学研究结果表明,800 oC以上进行热处理碳化,所生成石墨化微晶可有效促进电子传递,降低欧姆极化损失,同时,较高的处理温度可促进骨架氮掺杂,从而构建出高效氧还原反应活性位点.因此,氮杂型炭催化剂的组成、结构与电化学性能更多地受控于热处理过程中的热力学,而非热解动力学过程. 相似文献
8.
《Journal of Analytical and Applied Pyrolysis》2009,86(1-2):226-230
The pyrolytic conversion of pure lignin at 600 °C in flowing helium over five catalysts is described and compared to the control bed material, sand. Product distribution as char, liquid, and gas are described as well as the composition of the liquid and gas fractions. The catalysts examined were HZSM-5, KZSM-5, Al-MCM-41, solid phosphoric acid, and a hydrotreating catalyst, (Co/Mo/Al2O3). The sand yielded a liquid phase that was 97% oxygenated aromatics and a gas phase that was CO (18 vol%), CO2 (16 vol%), and CH4 (12 vol%). HZSM-5 was the best catalyst for producing a deoxygenated liquid fraction yielded almost equal amounts of simple aromatics (46.7%) and naphthalenic ring compounds (46.2%). The gas phase over this catalyst consisted of CO (22 vol%), CO2 (14 vol%), H2 (12 vol%), and CH4 (10 vol%). The Co/Mo/Al2O3 hydrotreating catalyst yielded a liquid consisting of 21% aromatics, 4% naphthalenics, and 75% oxygenated aromatics and a gas phase that was rich in hydrogen: H2 (18 vol%), CO2 (16 vol%), CO (12 vol%), and CH4 (8 vol%). 相似文献
9.
The flash vacuum pyrolysis (FVP) of methoxy-substituted beta-O-4 lignin model compounds has been studied at 500 degrees C to provide mechanistic insight into the primary reaction pathways that occur under conditions of fast pyrolysis. FVP of PhCH(2)CH(2)OPh (PPE), a model of the dominant beta-O-4 linkage in lignin, proceeds by C-O and C-C cleavage, in a 37:1 ratio, to produce styrene plus phenol as the dominant products and minor amounts of toluene, bibenzyl, and benzaldehyde. From the deuterium isotope effect in the FVP of PhCD(2)CH(2)OPh, it was shown that C-O cleavage occurs by homolysis and by 1,2-elimination in a ratio of 1.4:1, respectively. Methoxy substituents enhance the homolysis of the beta-O-4 linkage, relative to PPE, in o-CH(3)O-C(6)H(4)OCH(2)CH(2)Ph (o-CH(3)O-PPE) and (o-CH(3)O)(2)-C(6)H(3)OCH(2)CH(2)Ph ((o-CH(3)O)(2)-PPE) by a factor of 7.4 and 21, respectively. The methoxy-substituted phenoxy radicals undergo a complex series of reactions, which are dominated by 1,5-, 1,6-, and 1,4-intramolecular hydrogen abstraction, rearrangement, and beta-scission reactions. In the FVP of o-CH(3)O-PPE, the dominant product, salicylaldehyde, forms from the methoxyphenoxy radical by a 1,5-hydrogen shift to form 2-hydroxyphenoxymethyl radical, 1,2-phenyl shift, and beta-scission of a hydrogen atom. The 2-hydroxyphenoxymethyl radical can also cleave to form formaldehyde and phenol in which the ratio of 1, 2-phenyl shift to beta-scission is ca. 4:1. In the FVP of o-CH(3)O-PPE and (o-CH(3)O)(2)-PPE, products (ca. 20 mol %) are also formed by C-O homolysis of the methoxy group. The resulting phenoxy radicals undergo 1,5- and 1,6-hydrogen shifts in a ratio of ca. 2:1 to the aliphatic or benzylic carbon, respectively, of the phenethyl chain. In the FVP of (o-CH(3)O)(2)-PPE, o-cresol was the dominant product. It was formed by decomposition of 2-hydroxy-3-hydroxymethylbenzaldehyde and 2-hydroxybenzyl alcohol, which are formed from a complex series of reactions from the 2, 6-dimethoxyphenoxy radical. The key step in this reaction sequence was the rapid 1,5-hydrogen shift from 2-hydroxy-3-methoxybenzyloxy radical to 2-hydroxymethyl-6-methoxyphenoxy radical before beta-scission of a hydrogen atom to give the substituted benzaldehyde. The 2-hydroxybenzyl alcohols rapidly decompose under the reaction conditions to o-benzoquinone methide and pick up hydrogen from the reactor walls to form o-cresol. 相似文献
10.
生物质焦制备条件对其燃烧反应特性的影响 总被引:1,自引:0,他引:1
在热重分析仪上,研究了生物质焦的制备条件对其燃烧反应特性的影响。生物质焦由闪速裂解技术制得,裂解温度为 748 K、773 K和823 K;原料含水质量分数为0、7.0%和11.3%。研究发现,生物质焦中挥发性物质的质量分数和H/C质量比随裂解温度的增加而降低,其燃烧反应性随裂解温度的增加而降低;与高裂解温度条件下制得的生物质焦相比,低裂解温度条件下制得的生物质焦具有较高的反应活化能和对燃烧温度更敏感。原料含水量对生物质焦的燃烧反应特性影响很小;但对高裂解温度条件下制得的生物质焦中的挥发性组分含量有较大的影响。简化的生物质焦本征燃烧反应幂函数动力学模型可以很好地描述其燃烧行为。 相似文献
11.
木质素二聚体模型化合物热解机理的量子化学研究 总被引:1,自引:0,他引:1
木质素二聚体模型化合物热解机理的量子化学研究 《燃料化学学报》2015,43(11):1334-1343
β-O-4连接是木质素主体结构单元之间的主要联结方式。采用密度泛函理论方法B3LYP,在6-31G (d, p)基组水平上,对β-O-4型木质素二聚体模型化合物(1-愈创木基-2-(2-甲氧基苯氧基)-1,3丙二醇)的热解反应机理进行了研究。提出了三种热解反应途径:Cβ-O键均裂的后续反应、Cα-Cβ键均裂的后续反应以及协同反应。对各种反应的反应物、产物、中间体和过渡态的结构进行了能量梯度全优化,计算了各热解反应途径的标准动力学参数。分析了各种主要热解产物的形成演化机理以及热解过程中温度对热解机理的影响。计算结果表明,Cβ-O键的均裂反应和协同反应路径(1)和(3)是木质素二聚体热解过程中主要的反应路径,而Cα-Cβ键的均裂反应和协同反应路径(2)和(5)是主要的竞争反应路径;热解的主要产物是酚类化合物如愈创木酚、1-愈创木基-3-羟基丙酮、3-愈创木基-3-羟基丙醛、愈创木基甲醛和乙烯等。在热解低温阶段协同反应是热解过程中的主要反应形式,而在高温阶段自由基均裂反应是热解过程的主要反应形式。 相似文献
12.
In this work, the decomposition behaviors of jatropha wastes (husk, seed shell and branch) have been examined in order to get desired liquid organic compounds, but not undesired inorganic compounds such as CO, CO2, water and coke. The jatropha wastes exhibit a stepwise degradation pathway which has a slight difference in between samples before and after milling. In the preliminary pyrolysis using quartz reactor and H-ZSM-5(30) catalyst, the liquid products selectivity was seed shell > blanch > husk > seed shell (no catalyst). In the absence of catalyst, the Py-GC/MS analyses for pyrolysis of jatropha wastes show a range of aromatic hydrocarbons, phenols, alcohols and ketones, acids and esters, ethers and aldehydes. Aromatics are predominantly formed above 90% of area percentage by use of catalyst. Of aromatic compounds, xylenes, naphthalenes and toluene are mainly produced. The product selectivity is dependent on both the size of the catalyst pores and the nature of the active sites and one candidate is H-ZSM-5 and the other candidate is β-zeolite. The reaction pathway involves dehydrogenation and dehydroaromatization of aliphatic oxygenates such as alkylcyclohexanol and higher carboxylic acids to form phenol derivatives, which undergo hydrodeoxygenation into toluene and xylenes, followed by dehydroaromatization to give naphthalenes. 相似文献
13.
采用碱性条件下"后处理"脱硅的方法,制备了一系列多级孔Hβ分子筛,考察了Na OH浓度对Hβ分子筛上木质素催化热解性能的影响。结果表明,当Na OH浓度小于0.2 mol/L时,碱处理后的多级孔Hβ分子筛的介孔数量增加,木质素热解液体产物的收率随着Na OH浓度提高而显著增加。当Na OH浓度小于0.5 mol/L时,碱处理可以保持多级孔Hβ分子筛的微孔结构基本不被破坏,木质素催化热解具有较好的脱氧效果;产物以芳烃为主,含氧化合物的收率始终小于3%。当Na OH的浓度增加到1 mol/L时,会造成Hβ分子筛过度脱硅,骨架坍塌;由于Hβ分子筛的多级孔结构被破坏,此时不仅木质素热解液体产物的收率降低,而且脱氧效果变差。 相似文献
14.
A kinetic study on pyrolysis and combustion characteristics of oil cakes: Effect of cellulose and lignin content 总被引:3,自引:0,他引:3
Pyrolysis and combustion characteristics of three different oil cakes such as Pongamia(Pongamia Pinnata),Madhuca(Madhuca Indica),and Jatropha(Jatropha curcas) were investigated in this study.The cellulose and lignin contents of oil cakes play very important role in pyrolysis and combustion processes.A kinetic investigation of three oil cakes was carried out and major part of the samples decomposed between 210℃ and 500℃.Pyrolysis and combustion were carried out with the mixtures of cellulose and lignin chemi... 相似文献
15.
《Journal of Analytical and Applied Pyrolysis》2009,86(1-2):98-107
Various wet chemical and spectroscopic methods used in lignin chemistry as well as pyrolysis-gas chromatography/mass spectrometry were applied to elucidate the structure of pyrolytic lignins (PLs) with the help of previously obtained data on molecular weight distribution and laser desorption ionization-time of flight-mass spectrometry. PL from beech wood (Fagus sylvatica L.) was used as reference and in addition results from elemental analysis of carbon and hydrogen were used as basis for proposing five chemical structures, ranging from a tetramer to an octamer. The oligomers are typically characterized by biphenyl, phenyl coumaran, diphenyl ethers, stilbene and resinol structures. The results were used to speculate the formation of the pyrolytic lignin. It is concluded that pyrolytic lignin emerges as result of both recombination reactions and thermal ejection of intact lignin fragments. 相似文献
16.
生物质热解液化与美拉德反应 总被引:3,自引:0,他引:3
对生物质热解液化和美拉德反应进行了介绍,指出美拉德反应不仅存在于生物质热解液化过程中,而且通过引入适量氨等调控措施,可以促进美拉德反应有选择性地生成吡嗪类杂环化合物等高值化学品,然后再通过分级冷凝将生物油分为化工生物油和燃料生物油,前者用于分离提取高值化学品,后者用于锅炉和窑炉的燃料.引入美拉德反应后,生物质热解液化技术经济性将会得到根本性的改善. 相似文献
17.
《Journal of Analytical and Applied Pyrolysis》1986,9(3):207-236
The primary pyrolysis of lignins derived from different types of biomass and by the major separation methods has been investigated by molecular-beam sampling mass spectrometry. The lignins separated by the steam-explosion and kraft processes have altered pyrolysis characteristics while ball-milled lignins yield nearly the same product slate as observed in native biomass samples. The predominant and first-formed products, as determined by mass spectrometry, appear to be the precursor monomers, coniferyl and sinapyl alcohol. There is a distinct lack of higher-molecular-weight oligomers as is commonly observed in the pyrolysis of other types of natural and synthetic polymers. A group of peaks, with the most predominant being m/z 272, appear at masses greater than the monomer masses, but are significantly below the dimer mass range. A third group of predominant peaks are present at masses lighter than the monomers and consist of methoxyphenols that have double bonds and carbonyl groups in the alkyl side chains that are in conjugation with the aromatic ring, enhancing thermal stability. The results indicate that the thermolysis of the alkyl-aryl ether linkage, which is the major bonding unit in lignin, and the limited availability of transferable hydrogen, are the major factors that lead to the predominance of these products. The observed product distributions are indicative of specific, sterically favored rearrangement reactions, which allow devolatilization from the hydrogen deficient, solid matrix and favor double bond formation in the alkyl side chain of the products. A discussion of possible mechanisms of formation is given based on these results and the results of other workers in lignin pyrolysis. 相似文献
18.
19.
木质素模化物紫丁香酚热解机理的量子化学研究 总被引:3,自引:0,他引:3
采用密度泛函理论方法B3LYP/6-31G++(d,p),对木质素模化物紫丁香酚的热解反应机理进行了量子化学理论研究。提出了三种可能的热解反应途径,对各种反应的反应物、产物、中间体和过渡态的结构进行了能量梯度全优化。计算了各热解反应途径的标准动力学参数,分析了各种主要热解产物的形成演化机理。键离解能计算结果表明,紫丁香酚中CH3-O键的键离解能最小,各种键离解能的大小顺序为CH3-O < O-H < CH3O-Caromatic < CH2-H < HO-Caromatic < Caromatic-H。在反应路径(1)中,主要热解产物是3-甲氧基邻苯二酚,其形成反应的总能垒为366.6 kJ/mol;在反应路径(2)中主要热解产物是2-甲氧基-6-甲基苯酚,其形成反应的总能垒为474.8 kJ/mol;在反应路径(3)中形成邻甲氧基苯酚的总能垒很低,为21.4 kJ/mol,这表明,在连接甲氧基的碳原子上加氢后能够有效地降低木质素芳环模化物紫丁香酚去甲氧基反应的反应能垒。 相似文献
20.
《Journal of Analytical and Applied Pyrolysis》2009,84(2):205-212
Maize stalk was fast pyrolysed at temperatures between 420 °C and 580 °C in a fluidized-bed, and the main product of pyrolysis oil was obtained. The experimental results showed that the highest pyrolysis oil yield of 66 wt.% was obtained at 500 °C for maize stalk. Chemical composition of the pyrolysis oil acquired was analyzed by GC–MS and its heat value, stability, miscibility and corrosion characteristics were determined. These results showed that the pyrolysis oil could be directly used as a fuel oil for combustion in a boiler or a furnace without any upgrading. Alternatively, the fuel could be refined to be used by vehicles. 相似文献