用户名: 密码: 验证码:
流化床热解液化及生物油品质的分析研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
生物质是唯一可以液化的清洁的可再生能源,利用生物质快速热解制取的生物油便于运输和储存。作为液态燃料的生物油在替代化石燃料方面具有相当广阔的前景。但是,生物油的高粘度、高含水量、强酸性、低热值和热不稳定等性质严重影响了生物油的品质,阻碍了生物油作为燃料的应用。因此,为提高生物油的品质,增强生物油燃料的应用性,本文在自行设计建造的流化床热解液化系统上完成制取生物油的实验,一方面探求生物质原料和热解反应条件在热解过程中对生物物油产率和品质的影响规律,另一方面利用微波对生物质进行干燥,通过研究微波干燥对生物质原料以及对热解产物的影响规律,揭示微波干燥预处理对生物质热解过程的影响机理。本文研究的目的是实现生物质热解液化的控制转化,优化反应参数,揭示微波干燥的预处理工艺对生物质热解液化的积极意义。
     首先,对世界能源背景、生物质能及生物质热解液化技术进行了简单介绍,强调了液化产物生物油的特性及其应用难点,引出本文研究的目的和主要内容。
     其次,介绍了国内外流化床热解液化系统,描述了本文流化床热解液化系统的结构和工艺流程,选择了合适的试验参数,概括了试验操作方法和步骤。
     然后,通过试验研究了生物质原料种类、粒径和热解温度、气相停留时间对生物油产率和品质的影响规律。试验研究表明:原料的种类、热解温度和气相停留时间是影响生物油产率和品质最重要的参数:①、原料中纤维素、木质素和灰分的含量是主要影响因素。松木屑最适合生产高产率高品质的生物油。②、基于松木屑油的研究发现,450~550℃是生产高产率高品质松木屑油的最佳温度范围。③、热解蒸气的停留时间决定二次反应的发生几率,从而影响生物油的产率和品质。
     最后,试验研究微波干燥对生物质原料以及对生物质热解机制的影响。研究发现:微波干燥能迅速降低生物质原料的含水率,功率越大,干燥速率越快;微波干燥能扩大生物质的孔隙结构,有效增大原料的比表面积;微波干燥更有利于挥发分在热解过程中迅速析出,提高热解速率;微波干燥明显抑制了热解产物的二次反应,提高了生物油和焦炭的产率,减少了不凝气体的产率,同时减少了热解过程中水分的生成,提高了生物油的品质。
Biomass is the only clean renewable energy resource that can be liquefied. Bio-oil made from fast pyrolysis of biomass is convenient for being stored and transported with potential to be used as a fossil oil substitute. However, higher viscosity, higher moisture, higher acidity, lower heating value and heat instability are unbeneficial properties of bio-oil to be used as liquid fuel. Thus in this paper, experimental studies were carried out in a bench-scaled fluidized bed reactor. On the one hand, the influences of the parameters such as raw material characteristics and pyrolysis conditions on the yield and quality of bio-oil were studied, on the other hand, the influences of microwave drying on biomass and its pyrolysis products were investigated. The purpose of these studies was to optimize reaction parameters for improving the bio-oil quality and enlarging the application of bio-oil as liquid fuel.
     At first, the background of energy all over the world, the bio-energy and the fast pyrolysis technique were introduced. As liquid product, the properties of bio-oil and the difficulties on its application were emphasized.
     Secondly, the system of the bench-scaled fluidized bed and the choices of trial parameters were described, followed by the description of the experimental process.
     Thirdly, experimental studies on the influences of raw material and the pyrolysis conditions on the yield and quality of bio-oil were performed, which indicated that the raw material sorts, reaction temperature and vapor residence time were key factors. At the same time, the content of cellulose and lignin as well as the ash in biomass were critical parameters, and the pine was most suitable raw material for bio-oil. For getting high quality pine-oil, the favourable reaction temperature was between 450℃and 550℃. The residence time affected the secondary reaction of the vapor, which was important for the yield and the water content of bio-oil.
     Finally, compared with heated air drying, the influence of microwave drying on raw material characteristics and the mechanism of biomass fast pyrolysis were studied. It was found that microwave drying rate was far faster, moreover, greater the microwave power level was, faster the dehydration rate was. The biomass dried by microwave had greater surface area and more inner paths, which was benefited for the release of volatiles, meanwhile the secondary reaction of pyrolysis products was suppressed because of the shorter contacting time between vapors and char. As a result, the yields of bio-oil and char increased while the yield of gas decreased. The bio-oil from biomass dried by microwave has lower water content and higher heating value, which was good for used as fuel.
引文
[1]李瑞阳.21世纪的重要能源——生物质能[J].世界科学,1999,(10):25-27.
    [2] McKendry, P. Energy production from biomass (part 1): overview of biomass. Bioresource Technology, 2002, 83(1): 37-46.
    [3]渡边治人.木材应用基础.上海:上海科学技术出版社,1986
    [4]杨胜.饲料分析及饲料质量检测技术.北京:北京农业大学出版社,1993
    [5] NREL. Renewable Data Overview Renewable Energy Annual 1997,Volumel,October 1997
    [6]中国农业部/美国能源部项目专家组.中国生物质能转换技术发展与评价.北京:中国环境科学出版社,1998
    [7]马隆龙,吴创之,孙立.生物质气化技术及应用,北京:化学工业出版社,2003
    [8] Bridgewater A V. Principles and practice of biomass fast pyrolysis processes for liquids[J]. Journal of Analytical and Applied Pyrolysis, 1999, (51):3-22.
    [9] Demirbas A. Mechanisms of liquefaction and pyrolysis reactions of biomass. Energy Conversion & Management, 2000, 41: 633-646.
    [10] Rrichard C, Bailie. Results from Commercial-Demonstration Pyrolysis Facilities extended to producing Synfuels from Biomass,Energy from Biomass and Wastes. Symposium papers, 1981:584-569.
    [11] Sensoz S, Angn D, Yorgun S. Influence of particle size on the pyrolysis of rapeseed: fuel properties of bio-oil. Biomass and Bioenergy, 2000,(19): 271–279.
    [12] Meier D, Faix O. State of the art of applied fast pyrolysis of lignocellulosic materials a review[J]. Bioresource Technology, 1998,(68):71-77.
    [13] Scott D S, Piskorz J, Bergougnou M A, Graham R, et al. The Role of Temperature in the Fast Pyrolysis of Cellulose and Wood[J].Ind. Eng. Chem. Res. 1988:27:8-17.
    [14] Demirbas A. An overview of biomass pyrolysis [J].Energy Sources, 2002,(24):471-482.
    [15]徐保江.生物质热裂解机理及产物特性分析的研究:[博士学位论文].沈阳:沈阳农业大学,1998:38-49.
    [16] D.C.Elliott. Water, alkali and char in flash pyrolysis oils. Biomass and bioenergy, 1994, 7(1-6),179-185.
    [17]郭艳,王垚,魏飞.生物质快速裂解液化技术的研究进展.化工进展,2001,20(8):13-17.
    [18]何芳,易维明,柏雪源.国外利用热解生产生物油的装置.山东工程学院学报,1999, 13(3):61-64.
    [19]廖艳芬,王树荣,谭洪.生物质热解制取液体燃料技术的发展.能源工程,2002:1-5.
    [20]吴创之,马隆龙.生物质能现代化利用技术.北京:化学工业出版社,2003:202-203.
    [21] Bridgwater A V, Meier D and Radlein D. An overview of fast pyrolysis of biomass[J]. Organic Geochemistry, 1999, 30 (12): 1479-1493.
    [22] Underwood G. Commercialisation of fast pyrolysis products. In: Hogan E, Robert J, Bridgewater A V, editors. Biomass Termal Processing—Proceeding of the First Cnada/European Community R&D Contractors Meeting. CPL Scientific Press, 1992, p.226-228.
    [23] Graham R G and Huffman D R. Commercial Aspects of Rapid Thermal Processing(RPTTM), Presented at“The Seminar on Power Production from Biomass”, Espoo, Finland, 1995.3
    [24]刘荣厚,鲁楠,曹玉瑞等.旋转锥反应器生物质热裂解工艺过程及实验.沈阳农业大学学报,1997,28(4):307-311.
    [25]廖艳芬,王树荣,洪军等.生物质热裂解制取液体燃料的实验研究.能源工程,2002:1-3.
    [26]杨海平.油棕废弃物热解的实验及机理研究:[博士学位论文].武汉:华中科技大学,2005
    [27]戴先文,吴创之,周肇秋等.循环流化床反应器固体生物质的热解液化.太阳能学报, 2001,22(2):124-130.
    [28]郭艳,魏飞.应用裂解气相色谱对生物质快速热解规律的研究.太阳能学报,2001, 22(3): 280-285.
    [29]任铮伟,徐清,陈明强等.流化床生物质快速裂解制液体燃料.太阳能学报, 2002,23(4): 462-466.
    [30]易维明,柏雪源,何芳等.利用热等离子体进行生物质液化技术的研究.山东工程学院学报,2000,14(1):9-12.
    [31] Sipila K, Kuoppala E, Fagernas L, et al. Characterization of Biomass-Based Flash Pyrolysis Oils. Biomass and Bioenergy, 1998,14(2):103-113.
    [32] Coutinho A R, Rocha J D,Luengo C A,Preparing and characterizing biocaborn electrodes[J]. Fuel Processing Technology, 2000,67(1):93-102.
    [33] Gust S. Combustion experiences of flash pyrolysis fuel in intermediate size boilers. In:Bridgwater A V, Boocock D. Developments in Thermochemical Biomass Conversion; Blackie Academic & Professional: London, 1997,481-488.
    [34] Andrews R, Patnaik P C, Liu Q. Firing fast pyrolysis oil in turbines, In: Proceedings of the Symposium: Biomass Pyrolysis Oils-Properties and Combustion Meeting. Estes Park, CO, 1994,383–391.
    [35] Bandi A, Baumgart F. Stirling Engine with Flox Burner Fuelled with Fast Pyrolysis Liquid. In : Bridgwater,A V. Progress in Thermochemical Biomass Conversion;Blackwell Science: Oxford,2001,1459-1467.
    [36] Svitolo, Pghetti. Physical and combustion characterization of pyrolytic oils derived from biomass material upgraded by catalytic hydrogenation[J]. Fuel, 1994,73(11): 1810-1812.
    [37] Janse A M, Westerhout R, Prins W. Modelling of a single wood particle[J].Chemical Engineering and Processing,2000,39(3):239-252.
    [38] Radlein D, Piskorz J, Majerski P. Methord of producing slow-release nitrogenous organic fertilizer from biomass[P].US Patent,5676727,1997.10-14.
    [39] Oehr K H. et al. Simultaneous SOx/NOx emission control with Bio-LimeTM derived from biomass pyrolysis oil. Dev. Thermochem. Biomass Convers. [M]. Edited by Bridgwater A V and Boocock D G B, Blackie, London, UK. 1997, 2: 1477-1481.
    [40]唐汝江,陈汉平,王贤华等.生物质油应用技术.能源技术,2005,26(2):66-69.
    [41] Gust S. Pyrolysis oil as a heating fuel. [J]. VTT Symp. 1999, 192: 301-308.
    [42] Juste G L, Monfort J S. Preliminary test on combustion of wood deriver fast pyrolysis oils in a gas turbine combustor[J].Biomass and bioenergy, 2000,19(2):119-128.
    [43] Solantausta, Y.; Nylund, N.-O.; Westerholm, M.; Koljonen, T.;Oasmaa, A. Wood pyrolysis oil as fuel in a diesel power plant. Bioresour. Technol. 1993, 46, 177-188.
    [44] Scott D S, Piskorz J, et al. Liquid products from the continuous flash pyrolysis biomass[J]. Ind Eng Chem Process Des Dev.1985, 22:581-588.
    [45]陈明强,王君,王新运等.喷动流化床生物质裂解液体产物的组成和燃烧特性分析.见:吴创之等. 2005年中国生物质能技术与可持续发展研讨会论文集.济南:中国太阳能协会,2005.121-133.
    [46]刘荣厚,王华,栾敬德.红松木屑在流化床中热裂解温度对生物油产率及性质的影响.见:吴创之等. 2005年中国生物质能技术与可持续发展研讨会论文集.济南:中国太阳能协会,2005:155-159.
    [47] Soltes E J. Of biomass pyrolysis and liquids therefrom[A].In: Soltes E J. Pyrolysis oils from biomass, producing, analyzing and upgrading[c].American Chemical Society, 1988:1-7.
    [48]辛芬,陈汉平,王贤华等.生物质预处理实验研究.内部资料
    [49]王树荣,骆仲泱,董良杰等.生物质闪速热裂解制取生物油的试验研究.太阳能学报,2002,23(1):4-10.
    [50]庄慧颖,鲍亦令,王磊等.稻壳在流化床中的快速热解研究.新能源,1997,19(4):15-19.
    [51] Scott D S,Piskorz J. The flash pyrolysis of aspen-poplar wood. Canadian journal engineering, 1982,60: 666-674.
    [52] Maschio G, Koufopanos C and Lucchesi A. Pyrolysis, a promising route for biomass utilization. Biosource Technology, 1994, 42: 218-230.
    [53] Peacocke G V C, Russell P A, Jenkins J D, et al. Physical properties of flash pyrolysis liquids. Biomass and energy, 1994,7(1-6):169-177.
    [54]王丽红,柏雪源,易维明等.玉米秸秆热解生物油特性的研究.农业工程学报, 2006, 22(3): 108-111.
    [55] Rick F, Vix U. Product Standards for Pyrolysis Products for Use as Fuel in Industrial Firing Plant. In:Biomass Pyrolysis Liquuids Upgrading and Utilization,ed.Bridgwater A V,Grassi G.. London: Elsevier Applied Science, 1991,177-218.
    [56]张光全,董海山.生物质闪速热裂解制备生物质油.能源研究与利用, 2005,(5): 48-52.
    [57] Czernik S, Bridgwater A V. Overview of Applications of Biomass Fast Pyrolysis Oil. Energy & Fuels, 2004, 18(2): 590-598.
    [58] Oasmaa A, Leppamaki E, Koponen P, et al. Physical application of standard fuel oil analysis[A].Application of standard fuel oil analysis[C]. Espoo:VTT, 1997:13-15.
    [59] Czernik S, Johnson D K, Black S. Stability of wood fast pyrolysis oil. Biomass and Bioenergy 1994,7(1–6):187–192.
    [60] Britta Scholze. Long-term stability, catalytic, upgrading and application of pyrolysis oils-improving the properities of a potential substitute for fossil fuels[D]. Hamburg:Hamburg University,2002
    [61]张琦,常杰,王铁军等.生物质裂解油的性质及精制研究进展.石油化工,2006, 35(5): 493-498.
    [62]董良杰.流化床内生物质热裂解制取生物油的研究:[博士后士论文].杭州:浙江大学,1999
    [63] Teng H and Wei Y. Thermogravimetric studies on the kinetics of rice hull pyrolysis and the influence of water treatment. Ind.Eng.Chem.Res, 1998,37:3806-3811.
    [64] Drummond A F, Drummond I W. Pyrolysis of sugar cane bagasse in a wire-mesh reactor. Ind. Eng. Chem, 1996,35:1263-1268.
    [65] Soltes E, Wiley A, Lin S C K. Biomass pyrolysis-towards an understanding of its versatility and potentials. Biotech and bioengineering symposium, 1981,11:125-136
    [66]谭洪,王树荣,骆仲泱等.木质素快速热裂解试验研究.浙江大学学报(工学版), 2005.5,39(5):710-714.
    [67]廖艳芬,王树荣,骆仲泱等.纤维素快速热裂解试验研究及分析.浙江大学学报(工学版),2003.9,37(5):582-587.
    [68] Paolo Ghetti, Leandro Ricaa and Luciana Angelini. Thernal analysis of biomass and corresponding pyrolysis products. Fuel, 1996,75(5):565-573.
    [69] Scott D S, Piskorz J, Bergougnou M A, et al. The role of temperature in the fast pyrolysis of cellulose and wood[J]. Industrial & Engineering Chemistry Research,1989, (27): 8-17.
    [70]郭胜利,张宝林.微波干燥技术的应用进展.河南化工,2002,(4):1-3.
    [71]熊永森,王金双,王俊.物料特性对微波干燥影响的研究.金华职业技术学院学报, 2001,(3):18-19.
    [72]刘思峰,党耀国.灰色系统理论及其应用.北京:科学出版社
    [73]史雪荣.灰色系统模型及其在应力集中问题中的应用:[硕士学位论文].镇江:江苏大学,2003
    [74]陈茗.污泥真空干燥特性研究:[硕士学位论文].沈阳:沈阳航空工业学院,2006
    [75] Ren G, Chen F. Drying of American ginseng roots by microwave-hot air combination. Journal of Food Engineering, 1998,35,433-443.
    [76]曹小红,常学东.板栗的微波干燥特性及其对干后品质的影响.食品工业科技,2005,26(1):63-65.
    [77] Maskan M. Microwave/air and microwave finish drying of banana. Journal of Food Enginerring, 2000,44,71-78.
    [78] Branca, C.; Giudicianni, P.; Di Blasi, C., GC/MS characterization of liquids generated from low-temperature pyrolysis of wood. Industrial & Engineering Chemistry Research 2003, 42, (14), 3190-3202.
    [79] Ucar, G.; Meier, D.; Faix, O.; Wegener, G., Analytical pyrolysis and FTIR spectroscopy of fossil Sequoiadendron giganteum (Lindl.) wood and MWLs isolated hereof. Holz Als Roh-Und Werkstoff 2005, 63, (1), 57-63.

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700