煤中低温热解挥发分和硫脱除研究进展
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  • 英文篇名:Research progress on volatiles and sulfur removal during low temperature pyrolysis of coal
  • 作者:杨凤玲 ; 任磊 ; 贾阳杰 ; 吴海滨 ; 狄子琛 ; 程芳琴
  • 英文作者:YANG Fengling;REN Lei;JIA Yangjie;WU Haibing;DI Zichen;CHENG fangqin;Collaborative Innovation Center of High Value-added Utilization of Coal-related Wastes,State Environmental Protection Key Laboratory of Efficient Utilization Technology of Coal Waste Resources,Shanxi University;Shanxi Rui En Ze Technology Co.,Ltd.;
  • 关键词:煤热解 ; ; 干馏工艺 ; 成型热解 ; 挥发分
  • 英文关键词:coal pyrolysis;;sulfur;;distillation process;;molding pyrolysis;;volatiles
  • 中文刊名:JJMS
  • 英文刊名:Clean Coal Technology
  • 机构:山西大学国家环境保护煤炭废弃物资源化高效利用技术重点实验室低附加值煤基资源高值利用协同创新中心;山西瑞恩泽科技有限公司;
  • 出版日期:2019-01-15
  • 出版单位:洁净煤技术
  • 年:2019
  • 期:v.25;No.119
  • 基金:国家重点研发计划资助项目(2017YFC0211401);; 国家科技惠民计划资助项目(2012GS140202)
  • 语种:中文;
  • 页:JJMS201901007
  • 页数:10
  • CN:01
  • ISSN:11-3676/TD
  • 分类号:50-59
摘要
针对目前我国民用燃煤煤质较差,污染物无法集中处理,污染环境等问题,基于煤热解原理和硫的赋存形态,分析了气氛、添加剂、升温速率对煤热解过程的影响,论述了国内外目前较为成熟的粉煤干馏工艺,分析了粉煤干馏和块煤干馏的优缺点,提出了粉煤成型热解的工艺思路。重点介绍了目前山西大学和山西领君重工集团联合开发的无烟碳化型煤热解工艺路线,提出了一种洁净煤清洁燃烧多联产工艺系统。粉煤干馏工艺都以粉煤和粒煤为原料,易造成粉尘沉积和堵塞,无法高效分离。块煤可提高焦与油的分离效率,但非胶黏性煤热解过程中会粉化,效率不高。以半焦为热载体会降低半焦利用效率,产生大量焦粉,焦粉民用燃烧需成型,且难以黏结成型,鉴于此,提出了配煤成型热解的思路。热解后半焦粉末经成型可提高油、气产率,强度较好,与焦油高效分离,其产品可根据工艺控制挥发分供民用。煤成型热解联产无烟碳化型煤工艺生产的型煤整体利用率高,产生的污染物提取可制成高附加值副产品,有效控制粉尘污染,提高煤炭的品质和价值。无烟型碳挥发分和发热量高于无烟煤,强度高,用于民用燃烧完全符合国家标准。洁净煤清洁燃烧多联产工艺将循环流化床发电、洁净煤生产和粉煤灰陶粒制作有机结合,可有效利用电厂预热作为热源,并将干馏型煤生产的干馏气用于陶粒烧结的气源,得到洁净型煤产品,实现了固废综合利用和洁净燃烧。
        Aiming at the problem of serious air pollution caused by poor quality of coal and inability to centralize the treatment of pollutants in China's civil combustion at present,effects of atmosphere,additives and heating rate on coal pyrolysis was analyzed based on the principle of coal pyrolysis and the occurrence form of sulfur.The relatively mature dry distillation process of pulverized coal at home and abroad was discussed,the advantages and disadvantages of dry distillation of pulverized coal and lump coal were analyzed,and the technological thinking of briquette pyrolysis of pulverized coal was put forward.The pyrolysis process route of anthracite-carbonized briquette jointly developed by Shanxi University and Shanxi Lingjun Heavy Industry Group was introduced. Clean coal clean combustion multi-production process system was proposed.The dry distillation process of pulverized coal takes pulverized coal and granular coal as raw materials,which is easy to cause dust deposition and blockage,and can't be separated efficiently.Lump coal can improve the separation efficiency of tar and oil,but non-sticky coal will be pulverized in the pyrolysis process,and the efficiency is not high.Using semi-coke as heat carrier will reduce the utilization efficiency of semi-coke and produce a large number of coke powder. Civil combustion of coke powder needs to be shaped,and it is difficult to bond.In view of this,the idea of coal blending forming pyrolysis is put forward.The briquette of semi-coke powder after pyrolysis can increase the yield of oil and gas,and has good strength.It can be separated from tar efficiently,and its products can be controlled for civil use according to the process.Coal briquette produced by coal briquetting pyrolysis combined with anthracite-carbonized briquette jointly has a high overall utilization rate.The pollutants produced can be extracted into high value-added by-products,which can effectively control dust pollution and improve the quality and value of coal.The volatile matter and calorific value of smokeless carbon are higher than those of anthracite coal,and the intensity of smokeless carbon is high.The smokeless carbon used in civil combustion fully conforms to the national standards.Clean coal clean combustion multi-production process system combines circulating fluidized bed power generation,clean coal production and fly ash ceramsite production.It can effectively use preheating of power plant as heat source,and use dry distillation gas produced by dry distillation briquette as gas source for ceramsite sintering to obtain clean briquette products,realizing comprehensive utilization of solid waste and clean combustion.
引文
[1]王宝凤.煤热处理过程中硫及砷、汞、铅的迁移行为[M].北京:中国原子能出版社,2014.
    [2]高晋生.煤的热解、炼焦和煤焦油加工[M].北京:化学工业出版社,2010.
    [3]雷佳莉,严东.煤热解过程中硫的析出规律研究进展[J].煤炭与化工,2012,35(2):10-12.LEI Jiali,YAN Dong. Research development of sulfur releasefrom coal in pyrolysis process[J]. Coal and Chemical Industry,2012,35(2):10-12.
    [4]徐丽,文干湘.江西省煤炭质量总体状况调查[J].江西煤炭科技,2003(4):6-7.
    [5] BLOCK S S,SHARP J B,DARLAGE L J.Effectiveness of gases indesulphurization of coal[J].Fuel,1975,54(2):113-120.
    [6]徐龙,杨建丽,李允梅,等.兖州煤热解预脱硫行为(Ⅰ)热解过程中硫的迁移[J].化工学报,2003,54(10):1430-1435.XU Long,YANG Jianli,LI Yunmei,et al. Desulfurization behaviorof yanzhou coal through pyrolysis(Ⅰ):Sulfur transfer during py-rolysis[J]. Journal of Chemical Industry&Engineering,2003,54(10):1430-1435.
    [7] MIURA K,MAE K,SHIMADA M,et al.Analysis of formation ratesof sulfur-containing gases during the pyrolysis of various coals[J].Energy&Fuels,2001,15(3):92.
    [8] GRA Z·YNA Gryglewicz.Sulfur transformations during pyrolysis of ahigh sulfur Polish coking coal[J].Fuel,1995,74(3):356-361.
    [9] GRA Z·YNA Gryglewicz.Effectiveness of high temperature pyrolysisin sulfur removal from coal[J].Fuel Processing Technology,1996,46(3):217-226.
    [10]吴宽鸿,陈亚飞,于海兵.我国炼焦煤与无烟煤的资源和生产能力[J].中国冶金,2005,15(7):22-25,28.WU Kuanhong,CHEN Yafei,YU Haibing.Resources and produc-tion of coking coal and anthracite in China[J].China Metallurgy,2005,15(7):22-25,28.
    [11]刘诗薇,邹冲,赵俊学,等.不同焦煤中硫的赋存形态及热解气体逸出分析[J].煤炭转化,2018,41(2):24-30.LIU Shiwei,ZOU Chong,ZHAO Junxue,et al.Speciation of sulfurand regularity of pyrolysis gas evolution in different coking coals[J].Coal Conversion,2018,41(2):24-30.
    [12]郭慧卿,付琦,王鑫龙,等.CO2气氛对煤热解过程中硫逸出的影响[J].燃料化学学报,2017,45(5):523-528.GUO Huiqing,FU Qi,WANG Xinlong,et al.Effect of CO2atmos-phere on sulfur release during coal pyrolysis[J]. Journal of FuelChemistry&Technology,2017,45(5):523-528.
    [13]刘粉荣,李文,李保庆,等.氧化性气氛下流化床中煤的热解脱硫及硫的分布[J].燃料化学学报,2006,34(4):404-407.LIU Fenrong,LI Wen,LI Baoqing,et al. Sulfur removal and itsdistribution during coal pyrolysis in fluidized bed reactor underoxidative atmospheres[J].Journal of Fuel Chemistry and Technol-ogy,2006,34(4):404-407.
    [14]张成,曹娜,邱建荣,等.煤燃烧前温和热解汞和硫的释放特性研究[J].中国电机工程学报,2009,29(20):35-40.ZHANG Cheng,CAO Na,QIU Jianrong,et al. Study on mercuryand sulfur releasing characteristics during mild thermal upgradingbefore coal combustion[J]. Proceedings of the CSEE,2009,29(20):35-40.
    [15]张成,李婷婷,夏季,等.高硫煤不同气氛温和热解过程中含硫组分释放规律的实验研究[J].中国电机工程学报,2011,31(14):24-31.ZHANG Cheng,LI Tingting,XIA Ji,et al. Experimental researchon the releasing characteristics of sulfur-containing gases inhigh-sulfur coal under different atmospheres during mnd thermalupgrading[J].Proceedings of the CSEE,2011,31(14):24-31.
    [16]郭慧卿,赵丽红,马青兰,等.霍州煤氧化性气氛下热解预脱硫及硫的变迁[J].煤炭转化,2007,30(2):10-13.GUO Huiqing,ZHAO Lihong,MA Qinglan,et al. Sulfur removaland transformation of huozhou coal during pyrolysis under oxida-tive atmosphere[J].Coal Conversion,2007,30(2):10-13.
    [17] ZHANG G,DU Y,ZHANG Y,et al.Desulfurization reaction modeland experimental analysis of high sulfur coal under hydrogen at-mosphere[J]. Journal of Industrial&Engineering Chemistry,2014,20(2):487-493.
    [18]王素珍,王利花,赵炜.还原性气氛下煤中硫热解迁移规律(Ⅱ)氢气气氛与煤半焦中有机硫反应的动力学研究[J].煤炭转化,2009,32(2):5-9.WANG Suzhen,WANG Lihua,ZHAO Wei. Migration of sulfurin coal under the reductive pyrolysis part(Ⅱ):The kinetics studyon the reaction of hydrogen and organic sulfur in coal char[J].Coal Conversion,2009,32(2):5-9.
    [19]王利花,王素珍,赵炜.还原性气氛下煤中硫热解迁移规律(Ⅰ)H2和N2气氛下煤中硫热解释出规律的比较[J].煤炭转化,2009,32(1):10-13.WANG Lihua,WANG Suzhen,ZHAO Wei. Migration of sulfurin coal under the reductive pyrolysis part(Ⅰ):Comparison of ex-perimental results under H2and N2atmosphere[J].Coal Conver-sion,2009,32(1):10-13.
    [20]常丽萍,秦政,王美君,等.Fe Cl3的负载对褐煤热解提质中有机硫迁移转化的影响[J].太原理工大学学报,2012,43(4):406-410.CHANG Liping,QIN Zheng,WANG Meijun,et al. Effects ofFe Cl3addition on transformation of organic sulfur during the py-rolysis upgrading of Ximeng brown coal[J]. Journal of TaiyuanUniversity of Technology,2012,43(4):406-410.
    [21]黄吉庆,白宗庆,白进,等.过渡金属添加剂对煤热解脱硫的影响[J].燃料化学学报,2012,40(6):641-647.HUANG Jiqing,BAI Zongqing,BAI Jin,et al. Effects of transi-tion metal additives on desulfurization of coal in pyrolysis[J].Journal of Fuel Chemistry&Technology,2012,40(6):641-647.
    [22] WEN L,WANG K,ZHANG S,et al. Effect of additives oncoke metallurgical property and sulfide phase[C]//InternationalConference on Remote Sensing.[S.I.]:IEEE,2011.
    [23]管志超,胡艳军,钟英杰.不同升温速率下城市污水污泥热解特性及动力学研究[J].环境污染与防治,2012,34(3):35-39.GUAN Zhichao,HU Yanjun,ZHONG Yingjie.Pyrolysis character-istics of municipal wastewater sewage sludge under different heat-ing rate[J]. Environmental Pollution&Control,2012,34(3):35-39.
    [24]王辉,姜秀民,刘建国,等.不同升温速率下水煤浆的热解特性分析[J].动力工程学报,2007,27(2):263-266.WANG Hui,JIANG Xiumin,LIU Jianguo,et al. Analysis of pyro-lytic properties of coal-water slurry under various heating rates[J].Journal of Power Engineering,2007,27(2):263-266.
    [25]李少华,柏静儒,孙佰仲,等.升温速率对油页岩热解特性的影响[J].化学工程,2007,35(1):64-67.LI Shaohua,BAI Jingru,SUN Baizhong,et al. Effect of heatingrate on the pyrolysis characteristics of oil shales[J].Chemical En-gineering,2007,35(1):64-67.
    [26]常娜,甘艳萍,陈延信.升温速率及热解温度对煤热解过程的影响[J].煤炭转化,2012,35(3):1-5.CHANG Na,GAN Yanping,CHEN Yanxin.Study on the effects ofheating rate and temperature to coal pyrolysis[J]. Coal Conver-sion,2012,35(3):1-5.
    [27]李文英,邓靖,喻长连.褐煤固体热载体热解提质工艺进展[J].煤化工,2012,40(1):1-5.LI Wenying,DENG Jing,YU Changlian. Development of lignitepyrolysis with solid heat carrier[J]. Coal Chemical Industry,2012,40(1):1-5.
    [28]戴和武,谢可玉.褐煤利用技术[M].北京:煤炭工业出版社,1999.
    [29] CARLSON F B,HARDUMIAN L H,ATWOOD M T.Coal gasifi-cation:The TOSCOAL process for low temperature coal pyrolysis[J].Chemical Engineering Progress,1973,69:50.
    [30] CORTEX D H,LADELFA C J.Production of synthetic crude oilfrom coal using the TOSCOAL pyrolysis process[C]//16th Inter-society Energy Conversion Engineering Conference.United States:[s.n.],1981.
    [31]梁鹏,巩志坚,田原宇,等.固体热载体煤热解工艺的开发与进展[J].山东科技大学学报(自然科学版),2007,26(3):32-36.LIANG Peng,GONG Zhijian,TIAN Yuanyu,et al. Developmentand progress about coal pyrolysis with solid heat carrier[J].Jour-nal of Shandong University of Science and Technology(Natu-ral Science),2007,26(3):32-36.
    [32]关珺,何德民,张秋民.褐煤热解提质技术与多联产构想[J].煤化工,2011,39(6):1-4.GUAN Jun,HE Demin,ZHANG Qiumin. Feasibility analysis ofpoly-generation processes based on MCSG coal gasification cou-pling low-temperature carbonization of coal[J]. Coal ChemicalIndustry,2011,39(6):1-4.
    [33]王其成,吴道洪.无热载体蓄热式旋转床褐煤热解提质技术[J].煤炭加工与综合利用,2014(6):55-57.
    [34]霍威.抚顺式和桦甸式油页岩干馏工艺的比较[J].图书情报导刊,2012,22(10):122-124.HUO Wei.The comparison of oil shale's dry distillation processeswith fushun type distiller and huadian type distiller[J].Sci-TechInformation Development&Economy,2012,22(10):122-124.
    [35]肇永辉.抚顺油页岩干馏炉全循环工艺开发研究[J].中国高新技术企业,2012(9):28-30.
    [36]郭树才,刘恒韫.褐煤固体热载体干馏新技术工业性试验[J].大连理工大学学报,1995,35(1):46-50.GUO Shucai,LIU Hengyun.Experiment in pilot plant of new tech-nology for lignite retorting using solid heat carrier[J]. Journal ofDalian University of Technology,1995,35(1):46-50.
    [37]郭树才.褐煤新法干馏[J].煤化工,2000(3):6-8.GUO Shucai. Lignite retorting using solid heat carrier[J]. CoalChemical Industry,2000(3):6-8.
    [38]刘彦强.褐煤低温干馏原理及工艺分析[J].河南科技,2015(12):63-64.LIU Yanqiang.Analysis on lignite low-temperature dry distillationprinciple and technology[J]. Journal of Henan Science&Tech-nology,2015(12):63-64.
    [39]曾凡虎,陈钢,李泽海,等.我国低阶煤热解提质技术进展[J].化肥设计,2013,51(2):1-7.ZENG Fanhu,CHEN Gang,LI Zehai,et al.Technical progress forpyrolysis upgrade of low rank coal in China[J].Chemical Fertiliz-er Design,2013,51(2):1-7.
    [40]方梦祥,曾伟强,岑建孟,等.循环流化床煤分级转化多联产技术的开发及应用[J].广东电力,2011,24(9):1-7.FANG Mengxiang,ZENG Weiqiang,CEN Jianmeng,et al. Devel-opment and application of CFB-based polygeneration techniqueof coal grading conversion[J]. Guangdong Electric Power,2011,24(9):1-7.
    [41]方梦祥,骆仲泱.循环流化床热,电,气三联产装置的开发和应用前景分析[J].动力工程学报,1997(4):21-27.FANG Mengxiang,LUO Zhongyang. Development of circulatingfluidized bed gas steam electricity tri generation system and itsapplication prospect analyses[J]. Power Engineering,1997(4):21-27.
    [42] FANG M,LUO Z,LI X,et al.A multi-product cogeneration sys-tem using combined coal gasification and combustion[J].Energy,2014,23(3):203-212.
    [43]余德麒,施正伦,肖文丁,等.石煤灰渣二次焙烧稀酸浸出提钒工艺条件[J].过程工程学报,2010,10(4):673-678.YU Deqi,SHI Zhenglun,XIAO Wending,et al. Influential factorsof vanadium extraction by reburning and dilute sulfuric acid leac-hing of ash of stone coal[J].Chinese Journal of Process Engineer-ing,2010,10(4):673-678.
    [44]曾帅,周怀荣,钱宇.煤热解制油和油页岩制油技术评述与比较分析[J].化工学报,2017,68(10):3658-3668.ZENG Shuai,ZHOU Huairong,QIAN Yu,et al. Review and tech-no-economic analysis of coal pyrolysis to liquid and oil shale toliquid processes[J].CIESC Journal,2017,68(10):3658-3668.
    [45]张庆军,张长安,刘继华,等.块煤干馏技术研究进展与发展趋势[J].煤炭科学技术,2016,44(10):179-187.ZHANG Qingjun,ZHANG Changan,LIU Jihua,et al. Researchprogress and developing trend of lump coal dry distillation tech-nology[J].Coal Science&Technology,2016,44(10):179-187.
    [46]兰玉顺,陈文文.煤热解技术研究与开发进展[J].煤化工,2017,45(2):66-70.LAN Yushun,CHEN Wenwen. Research and development pro-gress of coal pyrolysis technology[J]. Coal Chemical Industry,2017,45(2):66-70.
    [47]王向辉,门卓武,许明,等.低阶煤粉煤热解提质技术研究现状及发展建议[J].洁净煤技术,2014,20(6):36-41.WANG Xianghui,MEN Zhuowu,XU Ming,et al. Research statusand development proposals on pyrolisis techniques of low rankpulverized coal[J].Clean Coal Technology,2014,20(6):36-41.

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