生物质焦油燃烧动力学及其燃料特性实验研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
本文研究工作是国家十五“863”高技术研究计划项目(编号:2003AA514012)“生物质燃气焦油净化器研制”的部分研究内容,主要开展生物质焦油净化蒸馏、组成分析、燃料性质、动力学以及内燃机负荷及排放特性等实验研究,为生物质焦油替代石油燃料进行了有益的探索。研究工作取得以下主要结论:
     (1)根据生物质焦油蒸馏实验,本文提出了各试样不同温度段的确定范围,即﹤105℃、105℃~145℃、145℃~205℃和205℃~220℃,并定义和分析了各试样的燃料性质。
     (2)生物质焦油的可燃性与柴油及水的溶解性有直接关系,即与柴油不能够互溶、与水互溶的试样具有不可燃特性,与柴油能够互溶、与水不溶的试样都具有直接可燃特性。
     (3)通过生物质焦油的可燃特性实验,发现试样二、四没有闪点,不具备可燃性;而试样一、三、五、六均存在闪点,具有一定的可燃性,且蒸馏温度越高,闪点也越高。试样一、三、五、六与柴油的化学成分比较接近,均具有碳氢含量高,氧含量低等特点,可以作为液体燃料使用。试样二和试样四中芳香族化合物含量很低,不具备液体燃料的使用价值,但是可作为化工原料。
     (4)不同气氛和升温速率下的燃烧动力学实验结果表明:生物质焦油、试样一、试样三、试样五、试样六、试样一、三、五混合液以及它们与0~#柴油的混合液都具有挥发份含量高、挥发特性强、着火温度低、燃烧比较稳定、燃烧后灰分很少等特点,具备液体燃料的基本性质,可作为常规能源的替代燃料使用。
     (5)本文根据燃烧实验数据进行了动力学参数的回归分析,拟合结果表明生物质焦油燃烧过程可在不同温度区间用一级动力学模型来反映,并得出低温区间的活化能较低,高温区间的活化能较大。
     (6)本文利用不同比例混合油在内燃机上燃烧实验结果表明:混合油均具有良好的动力性、经济性和排放性。0号柴油与生物质焦油试样按9:1比例配置的混合油要比8:2时节油效果显著,不同比例的混合油均具有CO_2减排显著、尾气排放烟度和CO降低明显等优点,有效减少了单一0号柴油燃烧时对环境污染的影响。
This paper is focused on partial content of Development of Biomass Gas Tar Purifier , a“863”high-tech research program (No.:2003AA514012) in National Tenth Five-Year. It mainly involves experimental studies of biomass tar purification and distillation, composition analysis, fuel performance, dynamics as well as load and emission characteristics of internal combustion engine. A helpful exploration for substitution of petroleum fuel by biomass tar is made. Main conclusions are achieved as follows:
     (1) According to biomass tar distillation test, this paper gives specific range of different temperature interval for each test specimen, i.e. up to 105℃, 105℃to 145℃, 145℃to 205℃and 205℃to 220℃. This paper also provides definition and analysis of fuel performance for each test specimen.
     (2) The flammability of the biomass tar has a direct relation with the solubility of diesel oil and water. Test specimens that are mutually insoluble in the oil and soluble in the water have noncombustible property, and test specimens that are mutually soluble in the oil but insoluble in the water have direct combustible property.
     (3) From combustibility test for biomass tar, Specimens 2 and 4 are found noncombustible without flash points, while Specimens 1, 3, 5, and 6 are found combustible with flash points. In addition, the flash point will be higher with the increase of distillation temperature. Chemical compositions of Specimena 1, 3, 5, and 6 are similar with those of the oil, with high carbon and hydrogen content and low oxygen content. The compositions can be used as liquid fuel. With a very low content of aromatic compounds, Specimens 2 and 4 have no value in use of liquid fuel, but they can be used as chemical materials.
     (4) Results of combustion dynamics experiments under different atmospherea and temperature-rise rates demonstrate that, biomass tar, Specimen 1, Specimen 3, Specimen 5, Specimen 6, mixture of Specimens 1, 3 and 5, as well as the mixture of them and 0~# diesel oil possess the features such as high volatile content, strong volatility, low ignition temperature, relatively stable combustion, and very low ash content after combustion, etc. They have basic nature of liquid fuel, and can be used as alternative fuel for conventional energy.
     (5) Regression analysis for dynamical parameters has been conducted in the paper according to the data from combustion experiments. The fitting results demonstrate that the combustion process of biomass tar can be reflected by the first-order dynamic model in different temperature intevals. Also it is concluded that the activation energy of low temperature interval is relatively low and that of high temperature interval is relatively high.
     (6) Results of the combustion test performed in internal combustion engine with oil mixture of different proportion demonstrate that all of the oil mixtures have good power, economical efficiency and emission performance. The oil mixture of 0# diesel oil and biomass tar specimens with the ratio of 9:1 has a more significant fuel-saving effect than that of oil mixture with the ratio of 8:2. Oil mixtures with different ratios possess advantages such as significant reduction of CO_2 emission, as well as obvious reduction of exhaust emission intensity and CO content, effectively reducing the pollution effect on environment in case of the combustion of single 0# diesel oil.
引文
[1] W Palz.新能源与可再生能源在未来能源系统中的地位[J].能源过程,1997,1:35-38.
    [2]Fatih Birol,Maria Argiri,World energy prospects to 2020.Energy,1999,24:905-918
    [3]董良杰.生物质热裂解制取生物油的研究:(博士学位论文).杭州:浙江大学,1999.
    [4]袁振宏,吴创之,马隆龙.生物质能利用原理与技术[M].北京:化学工业出版社,2005.
    [5]张素平,颜涌捷.生物质制液体燃料的研究:(博士学位论文).上海:华东理工大学,2002.
    [6]吴创之.生物质能现代化利用技术[M].北京:化学工业出版社,2003.
    [7] Serder Yaman. Pyrolysis of Biomass to Produce Fuels and Chemical Feedstocks. Energy Conversion and Management, 2004, 45 (5) :651-672.
    [8]杨立忠,杨钧锡,别义勋.新能源技术[M].北京:中国科学技术出版社,1994.
    [9]盛奎川,蒋成球,钟建立.农林废弃物热解的实验研究[J].农业工程学报,1997,13(1):149~153.
    [10]米铁.生物质气化过程的综合实验研究:(博士学位论文).武汉:华中科技大学,2002.
    [11]Ekstrom C. Fundamental of Thermochemical Biomass Conversion,Elsevier Applied Science,London and New York,1985:601.
    [12]Claes Brage,Krister Sjostrom,Separation of phenols and aromatic hydrocarbons from biomass tar using aminopropylsilane normal-phase liquid chromatography,Journal of Chromatography,1991,538(2):303-310.
    [13]姚福生,易维明,柏雪源,何芳,李永军.生物质快速热解液化技术[J].中国工程科学, 2001,3(4):63-68.
    [14]李滨,王述洋,谭文英.转锥式闪速热解反应器结构安全性设计理论研究[J].林业劳动安全, 2002,15(2):26-29.
    [15]Mathew S.Mendis,Biomass gasification:past experiences and future prospects in developing countries,Pyrolysis and gasification,Elsevier Applied Science,London and New York,1998:7-13.
    [16]Jaime M.Faundez,Ximena A.Garcia,Alfredo L.Gordon,Akinetic approach to catalytic of tars,Fuel Processing Technology,2001,69(3):239-259.
    [17]郭艳等.杨木快速裂解过程机理研究[J].高校化学工程学报,2001,15(3):440~445.
    [18]P.Hasler. Gas cleaning for IC engine application from fixed bed biomass gasification, Biomass and Bioenergy[J],1999, 16:385-395.
    [19] A V Bridgwater, S A Bridge. A Review of Biomass and Pyrolysis Technologies. Commission of the European Communities Biomass Pyrolysis Liquids Upgrading and Utilisation, 1991:11-33.
    [20] Esteban Churin, Rosana Maggi. Characterization and Upgrading of a Bio-oil Produced by Pyrolysis of Biomass. Research in Thermochemical Biomass Conversion, 1988,4:896-901
    [21] B Buran, L Butler, Currano et al. Environmental Benefits of Implementing Alternative Energy Technologies in Developing Countries. Applied Energy,2003, 76(2) :89-100.
    [22]Ian Narvaez. Fresh Tar Elimination over a Commercial Steam-Reform Catalyst:Kinetics and Effect of Different Variable of Operation[J].Ind.Eng.Chem.Res.1997,36:243-354.
    [23]K.Raveendran. Pyrolysis characteristics of biomass and biomass components[J].Fuel,1996,75(8):987-998.
    [24] Miguel A. Biomass gasification with air in fluidized bed (Hot gas cleanup with selected commercial and full-size neckl-based catalysts[J]. Ind.Eng.Chem.Res., 2000,39:1143-1154.
    [25]王树荣,廖艳芬,骆仲泱.生物质热裂解制油的动力学及技术研究[J].燃烧科学与技术, 2002,8 (2):176-181.
    [26]王树荣,骆仲泱,董良杰.生物质闪速热裂解制取生物油的试验研究[J].太阳能学报,2002,23(1):4-11.
    [27]刘荣厚,鲁楠.旋转锥反应器生物质热裂解工艺过程及实验[J].沈阳农业大学学报,1997,28(4):307-311.
    [28]任铮伟,徐清,陈明强等.流化床生物质快速裂解制液体燃料[J].太阳能学报,2002,23(4):462-467.
    [29]赖艳华,吕明新,马春元等.秸秆类生物质热解特性及其动力学研究[J].太阳能学报,2002,23(2):203-207.
    [30]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[J].太阳能学报,2001,22(2):124-131.
    [31]李在峰,雷廷宙,王磊.生物质干馏制炭制气系统研究[C],中国生物质能技术与可持续发展研讨会论文集,中国太阳能学会学会,郑州,2004,8:186-190.
    [32]雷群.生物质固化与炭化技术的现状与发展[J].山东能源,1996(3),23-25.
    [33]马孝琴,生物质成型燃料燃烧动力学特性及液压成型机改进设计研究:(博士学位论文).郑州:河南农业大学,2002.
    [34]邹吉华,王志伟等.热解法处理生物质废渣的最新技术[J].北方环境,2000(4):58-60.
    [35]张全国等.生物质焦油热物理特性研究[J].华中农业大学学报,2001,20(5):493-496.
    [36] Lopamudra Devi, Krzysztof J. Ptasinski, Frans J. J. G. Janssen. A Review of the Primary Measures for Tar Elimination in Biomass Gasification Processes[J]. Biomass and Bioenergy, 2003,24:125-140.
    [37]Corella J,Aznar M. The deactivation of tar cracking stones and commercial methane steam reforming catalysts in the upgrading of exit gas from steam FB gasifiers of biomass and organic wastes [C]. Catalyst Deactivation, Elsevier,1991:249-253.
    [38]Perez P, Alden H. Hot gas cleaning and upgrading with a calcined dolomite located downstream from a biomass FB gasifiers operation with steam-oxygen mixture [J].Energy & Fuels,1997,11:988-992.
    [39]Claes Brage, Krister Sjostrom.Tar evolution profiles obtained from gasification of biomass[J]. Biomass and Bioenergy, 2000,18:81-97.
    [40]Pekka A.Catalytic purification of tarry fuel gas with carbonate rocks and ferrous material[J], Fuel.1992,71(2):211-218.
    [41]Ian Narvaez. Fresh Tar Elimination over a Commercial Steam-Reform Catalyst:Kinetics and Effect of Different Variable of Operation[J].Ind.Eng.Chem.Res.1997,36:2630-2635.
    [42]Peacocke G V C,Bridgwater A V,Ablative plate pyrolysis of biomass for liquids[J],Biomass and Bioenergy,1994,7:147-154.
    [43]Ekstron C,Lindman N,Pettersson R,Catalytic conversion of tars,carbon black and methane from pyrolysis/gasification from biomass,in:Fundamentals of Thermochemical Biomass Conversion,Overend R.P.,Milne T.A.,Mudeg L.Elsevier Science Ltd.,Oxford,UK,1985:60-618.
    [44]L Fagbemi. Pyrolysis products from different biomasses:application to the thermal cracking of tar[J], Applied Energy,2001,69(4):293-306.
    [45]L Fagbemi. Pyrolysis products from different biomasses:application to the thermal cracking of tar, Applied Energy[J],1990,36(4):317-327.
    [46]Pekka A Simell,Jukka K Leppalahhi,Esa A.Kurkela,Tar-decomposition activity of carbonate rocks under high CO2 partial pressure[J],Fuel,1995,74(6),938-945.
    [47]Alden H,Espenas B G,Rensfelt E,Conversion of tar in pyrolysis gas from wood using a fixed dolomite bed,in:Research in Thermochemical Biomass Conversion[M], Elsevier Applied Science,London,1988:987-1001.
    [48]Simell P,Kurkela E,Stahlberg P, Formation and catalytic decomposition of tars from fluidized-bed gasfication.In:AdvancesinThemochemical biomass Conversion[M], Blackie Academic & Professional, London,1993,l(1):265-279.
    [49]Donnot A,Magne P,Deglise X,Kinetic parameters of the cracking reaction of tar from wood pyrolysis.Comparision of dolomite with industrial catalysts[J], J.Anal.Pyrolysis,1991,22:132-138.
    [50]V Vassilators,G Taralas,K Sjostrom,E Rjornbom,Catalytic cracking of tar in biomass pyrolysis gas in the presence of calcined dolomite[J],Can.J.Chem.Eng.,1992,70:1008-1013.
    [51]董玉平,孙玉泉.湿式净化秸秆热解气化机组研制[J].农业机械学报,2000,31(5):48-51.
    [52]许崇庆,孙立,胡浩等.XFF秸秆气化机组的改进[J].山东科学,1999,12(4):35-39.
    [53]张全国,孔书轩,刘圣勇等.生物质燃气净化技术及其装置研究[J].中国沼气,2000,18(1):43-48.
    [54]王素兰.生物质焦油热物理特性与燃气净化装置的研究:(硕士学位论文).郑州:河南农业大学,2000.
    [55]杨秀山,赵军,骆海鹏等.微生物降解生物质气化洗焦废水和焦油的研究[J].中国环境科学2001,21(2) 109-111.
    [56]马隆龙,肖艳京,任永志等.生物质气化供气系统研制[J].农村能源2001, (1) :18-21.
    [57]张素平,颜涌捷.生物质裂解焦油的燃烧特性及动力学模型[J].华东理工大学学报,2002,28(1):104-106.
    [58]王树荣等.生物质热裂解油的动力学及技术研究[J].燃烧科学与技术,2002,8(2):176-180.
    [59]吴创之.生物质焦油裂解技术[J].可再生能源,2003,3:54-57.
    [60]吴创之.生物质燃气净化技术[J].可再生能源,2003,4:55-56.
    [61].王铁柱,生物质焦油催化裂解试研研究:(博士学位论文).杭州:浙江大学,2003.
    [62]蒋旭光.造纸污泥流化床燃烧特性及燃烧过程数学模型[J].燃烧科学与技术,1999,5(4):394-402.
    [63]易维明,柏雪源.山楂籽热挥发特性的实验研究[J].农业机械学报,1998,29(4):72-76.
    [64]于海龙,姜秀民.升温速率对油页岩燃烧特性与动力学参数的影响[J].燃烧科学与技术,2003,9(1):54-57.
    [65]李云清.单滴碳氢燃料的燃烧特性[J].燃烧科学与技术,2000,6(4):320-325.
    [66]寥强.城市生活垃圾着火特性研究[J].燃烧科学与技术,2002,8(2):185-187.
    [67]葛阳等.单颗粒燃料滴在高温氧化环境中着火规律的研究[J].燃烧科学与技术,1997,3(2):126-134.
    [68]李余增.热分析[M].北京:清华大学出版社,1987.
    [69]汪正范,杨树民等.色谱联用技术[M].北京:化学工业出版社2001.
    [70]候一斌.煤焦油成分的气相色谱-质谱法分析[J].质谱学报,1996,17(4):60-63.
    [71]张全国,刘圣勇.燃烧理论及其应用[M].郑州:河南科学技术出版社,1993.
    [72]李宝山.中国新能源和可再生能源的发展[J].中国能源,1996, (3):46-48.
    [73] Streets D G,Waldhoeff S T. Biofuel Use in Asia and Acidifying Emissions[J]. Energy, 1998,23(12):1029-1042.
    [74] Li Junfeng, Hu Runqing. Sustainable Biomass Production for Energy in China[J]. Biomass and Bioenergy, 2003,25:483-499.
    [75]郭艳,王垚,魏飞等.杨木快速裂解过程机理研究[J].高校化学工程学报,2001,15(3):440-445.
    [76] Yaman,Serdar. Pyrolysis of Biomass to Produce Fuels and Chemical feedstocks [J]. Energy Conversion and Management, Mar 2004,45(5):651-671.
    [77]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,1999.
    [78] D Chiaramonti, M Bonini, E Fratini, G Tondi et al. Development of Emulsions from Biomass Pyrolysis Liquid and Diesel and Their Use in Engines—Part 1:Emulsion Production[J]. Biomass and Bioenergy, 2003,25:85-99.
    [79] Esteban Churin, Rosana Maggi. Characterization and Upgrading of a Bio-oil Produced by Pyrolysis of Biomass[C]. Research in Thermochemical Biomass Conversion, 1988:896-901.
    [80] J P Diebold, A V Bridgwater. Overview of Fast Pyrolysis of Biomass for the Production of Liquid Fuels[M]. Developments in Thermochemical Biomass Conversion,1997:5-23.
    [81] T Milne, F Agblevor, M Davis et al. A Review of the Chemical Composition of Fast-Pyrolysis Oils From Biomass[M]. Developments in Thermochemical Biomass Conversion,1997:409-424.
    [82] C P Mitchell, A V Bridgwater, K L Mackie. Bioenergy Systems[M]. Developments in Thermochemical Biomass Conversion,1997:1509-1525.
    [83] Douglas C. Elliott. Upgrading Liquid Products: Notes From the Workshop at the International Conference[R].Research in Thermochemical Biomass Conversion,1988:1170-1176.
    [84] A V Bridgwater, S A Bridge. A Review of Biomass and Pyrolysis Technologies[R]. Commission of the European Communities. Biomass Pyrolysis Liquids Upgrading and Utilisation, 1991:11-33.
    [85] R Gambles, L Zsuffe. The International Energy Agency—Cooperative Research on Biomass for Energy[R]. Research in Thermochemical Biomass Conversion, April 1988:1-9.
    [86]雷群.生物质固化与炭化技术的现状与发展[J].山东能源,1996,(3):23-25.
    [87] Monique Hoogwijk. Exploration of the Range of the Global Potential of Biomass for Energy[J]. Biomass and Bioenergy, 2003,24:119-133.
    [88] Lopamudra Devi, Krzysztof J. Ptasinski, Frans J. J. G. Janssen. A Review of the Primary Measures for Tar Elimination in Biomass Gasification Processes[J]. Biomass and Bioenergy, 2003,24:125-140.
    [89]张全国.生物质气化副产物(焦油)的能源特性实验研究[J].太阳能学报,2002,23(3):392-397.
    [90]许明.生物质中热值热解制气技术与应用研究:(博士学位论文).杭州:浙江大学,2002.
    [91] X T Li, J R Grace, et al. Biomass Gasification in a Circulating Fluidized Bed[J]. Biomass and Bioenergy, 2004,26:171-193.
    [92] Myren, Carin, et al. Catalytic Tar Decomposition of Biomass Pyrolysis Gas with a Combination of Dolomite and Silica[J]. Biomass and Bioenergy, 2002,23:217-227.
    [93] Martin Rupp. Utilisation of Pyrolysis Liquids in Refineries[C]. Commission of the European Communities—Biomass Pyrolysis Liquids Upgrading and Utilisation, 1991:219-227.
    [94]赖艳华.生物质热解过程的传热传质及低焦油气化技术研究:(博士学位论文).南京:东南大学,2002.
    [95] Richard L Bain, Ralph P Overend. Biomass for Heat and Power. Forest Products Journal, 52(2002):12-19.
    [96] Provisional Report of the Findings Prepared by the EU Partners[C]. Joint EU-China Project to Encourage Biomass Uptake and Assist Technology Transfer of EU Biomass/Biomass Waste Utilisation Technologies to China, June 2003.
    [97]马隆龙,吴创之,孙立.生物质气化技术及其应用[M].北京:化学工业出版社,2003.
    [98]赖艳华,吕新明,董玉平.生物质热解气化气中焦油生成机理及其脱除研究[J].农村能源2001,98(4):16~19
    [99]候斌,吕子安,李晓辉等.生物质热解产物中焦油的催化裂解[J].燃料化学学报,2001,29(1):70-75.
    [100]蒋德明.内燃机燃烧与排放学[M].西安:西安交通大学出版社,2002.
    [101] F. N. ANI, R. ZAILANI. Characteristics of Pyrolysis Oil and Char From Oil Palm Shells[M]. Developments in Thermochemical Biomass Conversion, 1997, (1):425-461.
    [102]候一斌,杜庆新,梁振芬等.煤焦油成分的气相色谱-质谱法分析[J].质谱学报,1995,17(4):60-63.
    [103]罗坚,张秋花,吴家珍.高温煤焦油抽提物的色谱-质谱联用分析[J].分析化学,1994,22(12):1248-1251.
    [104] Brage, C., Yu, Q. and Sjostrom, K. Characteristics of evolution of tar from wood pyrolysis in a fixed-bed reacter[J]. Fuel, 1996,75(2):213-219.
    [105]汪正范,杨树民,吴侔天,岳卫华.色谱联用技术[M].北京:化学工业出版社2001.
    [106]周良模.气相色谱新技术[M].北京:科学出版社,1994.
    [107]丛浦珠.质谱学在天然有机化学中的应用[M].北京:科学出版社,1987.
    [108] L.A.科特.有机质谱法导论[M].北京:科学出版社,1982.
    [109]高鸿宾,任贵忠,王绳武,林吉文等.实用有机化学辞典[M].北京:高等教育出版社,1997.
    [110]李继红.生物质焦油及其馏分的热动力学研究(硕士学位论文).郑州:河南农业大学,2005.
    [112]王树荣,廖艳芬,骆仲泱等.生物质裂解制油的动力学及技术研究[J].燃烧科学与技术,2002,8(2):176-180.
    [113]于海龙,姜秀民.升温速率对油页岩燃烧特性与动力学参数的影响[J].燃烧科学与技术,2003,9(1):54-57.
    [114]秦宏,姜秀民等.油页岩燃烧特性的热天平试验研究[J].热能动力工程,2000,15(6):644-646.
    [115] D K Lee, A Boe. Biomass Production of Switchgrass in Central South Dakota[J].Crop Science,2005,45(6): 2583-2592.
    [116] Yang, Yao Bin,Ryu et al.Effect of fuel properties on biomass combustion. Part II. Modelling approach—identification of the controlling factors[J]. Fuel,2005, 84 (16) :2116-2130.
    [117] Sheng, Changdong, Azevedo, J L T.Estimating the higher heating value of biomass fuels from basic analysis data[J]. Biomass & Bioenergy, 2005, 28 (5):499-507.
    [118] Zhang uping, Yan Yongjie, Li Tingchen.Upgrading of liquid fuel from the pyrolysis of biomass[J]. Bioresource Technology, 2005, 96(5):545-550
    [119] Ayhan Demirba. A Renewable Motor Fuel from Biomass[J].Energy Sources, 2005, 27 (4):327-337.
    [120] Parikka, Matti.Global biomass fuel resources[J]. Biomass & Bioenergy,2004, 27(6):613-620.
    [121] Obernberger Ingwald,Thek Gerold.Physical characterisation and chemical composition of densified biomass fuels with regard to their combustion behaviour[J]. Biomass & Bioenergy, 2004, 27(6):653-669.
    [122] Dem&idot,rba?, Ayhan.Utilization of Biomass as Alternative Fuel for External Combustion Engines[J].Energy Sources, 2004, 26(13):1219-1226.
    [123] Cuiping Liao, Chuangzhi Wu, Yanyongjie et al. Chemical elemental characteristics of biomass fuels in China[J]. Biomass & Bioenergy,2004,27(2):119-131.
    [124]张全国,雷廷宙.农业废弃物气化技术[M].北京:化学工业出版社,2006.
    [125]中国汽车工业总公司.中华人民共和国机械工业部标准.北京:机械工业出版社:1991.
    [126]高连兴.拖拉机与汽车.上册(发动机).北京:中国农业出版社:2000.
    [127]张红梅.生物质燃油做柴油机代用燃料的研究(硕士学位论文).郑州:河南农业大学,2004.
    [128]施得铭.柴油机代用燃料-生物柴油的试验研究.农业工程学报[J].1991(2):93.
    [129]周允.发动机燃用代用燃料排放特性的研究.天然气汽车信息[J].1997(4)18-22.
    [130]陈军.S195柴油机燃用菜籽油的试验.西北农林科技大学学报[J].2001(2)126-127.
    [131]周一鸣.汽车拖拉机学[M].北京:中国农业大学出版社:2000.
    [132]北京市地方标准:柴油车加载减速烟度排放标准.
    [133]李照美.汽车检测与诊断技术[M].北京:中国农业出版社:1996.
    [134]程宏.汽车发动机原理[M].北京:学术期刊出版社:1988.
    [135] [美]S.D.哈达德.柴油机原理及运用性能[M].北京:人民交通出版社:1991.
    [136]王建昕.汽车排放污染治理及催化转化器.北京:化学出版社:2000.

© 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