Volume 46 Issue 2
Feb.  2018
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LIN Jun-heng, YANG Wen-shen, YIN Xiu-li, WU Chuang-zhi. Release of HCl and H2S during pyrolysis of aged refuse derived-fuels[J]. Journal of Fuel Chemistry and Technology, 2018, 46(2): 152-160.
Citation: LIN Jun-heng, YANG Wen-shen, YIN Xiu-li, WU Chuang-zhi. Release of HCl and H2S during pyrolysis of aged refuse derived-fuels[J]. Journal of Fuel Chemistry and Technology, 2018, 46(2): 152-160.

Release of HCl and H2S during pyrolysis of aged refuse derived-fuels

Funds:

the National Key R&D Program of China 2016YFE0203300

the Guangdong Natural Science Foundation 2017B030308002

the Science and Technology Program of Guangzhou 201707010242

More Information
  • Corresponding author: YANG Wen-shen, E-mail: yangws@ms.giec.ac.cn
  • Received Date: 2017-11-19
  • Rev Recd Date: 2018-01-09
  • Available Online: 2021-01-23
  • Publish Date: 2018-02-10
  • Based on the horizontal tubular reactor-chemical absorption together with TG-FTIR-MS methods, release characteristics of corrosive gases, viz., HCl and H2S, during pyrolysis of refuse derived-fuels were investigated. The effects of pyrolysis temperature and pyrolysis type on their release behaviors for the aged (ARDF) and normal (NRDF) categories were compared. Meanwhile, the occurrence properties of corrosive elements (Cl and S) in solid products were also explored. The results indicate that the release of each corrosive gas has similar characteristic temperature range for slow pyrolysis of two categories. The release of HCl occurs at 200-400 and 420-500℃, respectively, while the emission of H2S is observed at 230-370 and 380-670℃, respectively. In addition, ARDF has a lower emission amounts of both HCl and H2S compared to NRDF under this condition. With regard to fast pyrolysis, the release of corrosive gases show different regularities, which largely depends on pyrolysis temperature. With increasing temperature, the emission of HCl and H2S present a nonlinear and an increasing trends, respectively, reaching peak values at 850℃; It is 48.8% (ARDF) and 29.4% (NRDF) for HCl, 6.8% (ARDF) and 44.6% (NRDF) for H2S. Subsequently, due to the distinctive release characteristics of corrosive gases, the occurrence of corrosive elements in solid phase relating to temperature differs in two categories. The retained amounts of Cl and S reach to 59.4% (450℃) and 84.3% (750℃) for ARDF, respectively. But for NRDF, that is 36.7% (850℃) and 15.2% (650℃), repetitively. It can be inferred that ARDF has the more stable corrosive elements difficult to be released into gases, which could provide some guidelines on thermal utilization of refuse derived-fuels.
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  • [1]
    "十三五"全国城镇生活垃圾无害化处理设施建设规划[R]. 北京: 国家发展改革委住房城乡建设部, 2016.

    "The 13th Five-Year Plan" construction planning for harmless treatment facilities of national municipal wastes[R]. Beijing: Ministry of Housing and Urban-Rural Development of the People's Republic of China, 2016.
    [2]
    李华, 赵由才.填埋场稳定化垃圾的开采、利用及填埋场土地利用分析[J].环境卫生工程, 2000, 8(2):56-57+61. https://www.wenkuxiazai.com/doc/4d54630dcc175527072208b6.html

    LI Hua, ZHAO You-cai. The exploitation of stabilizing solid waste and the utilization analysis for the land of landfill site[J]. Environ Sanit Eng, 2000, 8(2):56-57+61. https://www.wenkuxiazai.com/doc/4d54630dcc175527072208b6.html
    [3]
    赵由才, 柴晓利, 牛冬杰.矿化垃圾基本特性研究[J].同济大学学报(自然科学版), 2006, 34(10):1360-1364. doi: 10.3321/j.issn:0253-374X.2006.10.017

    ZHAO You-cai, CHAI Xiao-li, NIU Dong-jie. Characteristics of aged refuse in closed refuse landfill in Shanghai[J]. J Tongji Univ (Nat Sci), 2006, 34(10):1360-1364. doi: 10.3321/j.issn:0253-374X.2006.10.017
    [4]
    ZHAO Y C, WANG L C, HUA R H, XU D M, GU G W. A comparison of refuse attenuation in laboratory and field scale lysimeters[J]. Waste Manage, 2002, 22(1):29-35. doi: 10.1016/S0956-053X(01)00028-9
    [5]
    COMMISSION E. Council Directive 99/31/EC of 26 April 1999 on the landfill of waste (Landfill Directive)[EB]. 1999.
    [6]
    BOSMANS A, VANDERREYDT I, GEYSEN D, HELSEN L. The crucial role of Waste-to-Energy technologies in enhanced landfill mining:a technology review[J]. J Clean Prod, 2013, 55(14):10-23. https://www.researchgate.net/publication/271615996_The_crucial_role_of_Waste-to-Energy_technologies_in_enhanced_landfill_mining_A_technology_review
    [7]
    ROTHEUT M, QUICKER P. Energetic utilisation of refuse derived fuels from landfill mining[J]. Waste Manage, 2017, 62:101-117. doi: 10.1016/j.wasman.2017.02.002
    [8]
    CHALERMCHAROENRAT S, LAOHALIDANOND K, KERDSUWAN S. Optimization of combustion behavior and producer gas quality from reclaimed landfill through highly densify RDF-gasification[J]. Energy Procedia, 2015, 79:321-326. https://www.sciencedirect.com/science/article/pii/S1876610215022286
    [9]
    KAEWPENGKROW P, ATONG D, SRICHAROENCHAIKUL V. Pyrolysis and gasification of landfilled plastic wastes with Ni-Mg-La/Al2O3 catalyst[J]. Environ Technol, 2012, 33(22/24):2489-2495. https://www.researchgate.net/publication/235727392_Pyrolysis_and_gasification_of_landfilled_plastic_wastes_with_Ni-Mg-LaAl2O3_catalyst
    [10]
    袁浩然, 鲁涛, 熊祖鸿, 黄宏宇, 小林敬幸, 陈勇, 黎志强.城市生活垃圾热解气化技术研究进展[J].化工进展, 2012, 31(2):421-427. http://www.hgjz.com.cn/CN/abstract/abstract11827.shtml

    YUAN Hao-ran, LU Tao, XIONG Zu-hong, HUANG Hong-yu, KOBAYASHI Noriyuki, CHEN Yong, LI Zhi-qiang. Advance in pyrolysis and gasification of municipal solid waste study[J]. Chem Ind Eng Prog, 2012, 31(2):421-427. http://www.hgjz.com.cn/CN/abstract/abstract11827.shtml
    [11]
    PAN T J, GESMUNDO F, NIU Y. Corrosion behavior of three iron-based model alloys in reducing atmospheres containing HCl and H2S at 600℃[J]. Corros Sci, 2007, 49(3):1362-1377. doi: 10.1016/j.corsci.2006.06.014
    [12]
    HU H, FANG Y, LIU H, YU R, LUO G, LIU W, LI A, YAO H. The fate of sulfur during rapid pyrolysis of scrap tires[J]. Chemosphere, 2014, 97(1):102-107. https://www.sciencedirect.com/science/article/pii/S0045653513014380
    [13]
    YUAN G, CHEN D, YIN L, WANG Z, ZHAO L, WANG J Y. High efficiency chlorine removal from polyvinyl chloride (PVC) pyrolysis with a gas-liquid fluidized bed reactor[J]. Waste Manage, 2014, 34(6):1045-1050. doi: 10.1016/j.wasman.2013.08.021
    [14]
    ZHU H M, JIANG X G, YAN J H, CHI Y, CEN K F. TG-FTIR analysis of PVC thermal degradation and HCl removal[J]. J Anal Appl Pyrolysis, 2008, 82(1):1-9. https://www.sciencedirect.com/science/article/pii/S0165237007001623
    [15]
    LANE D J, VAN EYK P J, ASHMAN P J, KWONG C W, DE NYS R, ROBERTS D A, COLE A J, LEWIS D M. Release of Cl, S, P, K, and Na during thermal conversion of algal biomass[J]. Energy Fuels, 2015, 29(4):2542-2554. doi: 10.1021/acs.energyfuels.5b00279
    [16]
    WILLIAMS E A, WILLIAMS P T. The pyrolysis of individual plastics and a plastic mixture in a fixed bed reactor[J]. J Chem Technol Biot, 1997, 70(1):9-20. doi: 10.1002/(ISSN)1097-4660
    [17]
    YU J, SUN L, MA C, QIAO Y, YAO H. Thermal degradation of PVC:A review[J]. Waste Manage, 2016, 48:300-314. doi: 10.1016/j.wasman.2015.11.041
    [18]
    ZHOU H, WU C, ONWUDILI J A, MENG A, ZHANG Y, WILLIAMS P T. Influence of process conditions on the formation of 2-4 ring polycyclic aromatic hydrocarbons from the pyrolysis of polyvinyl chloride[J]. Fuel Process Technol, 2016, 144(Supplement C):299-304. https://www.sciencedirect.com/science/article/pii/S037838201630011X
    [19]
    MENG N, JIANG D, LIU Y, GAO Z, CAO Y, ZHANG J, GU J, HAN Y. Sulfur transformation in coal during supercritical water gasification[J]. Fuel, 2016, 186:394-404. doi: 10.1016/j.fuel.2016.08.097
    [20]
    XU L, YANG J L, LI Y M, LIU Z Y. Behavior of organic sulfur model compounds in pyrolysis under coal-like environment[J]. Fuel Process Technol, 2004, 85(8/10):1013-1024. https://www.sciencedirect.com/science/article/pii/S0378382003003011
    [21]
    阮松宾.广西县级城镇生活垃圾处理方式和工艺探讨[J].环境卫生工程, 2008, 16(1):27-30. http://d.old.wanfangdata.com.cn/Periodical/hjwsgc200801008

    RUAN Song-bin. Discussion about means and process of country towns domestic waste treatment in Guangxi[J]. Environ Sanit Eng, 2008, 16(1):27-30. http://d.old.wanfangdata.com.cn/Periodical/hjwsgc200801008
    [22]
    SINGH S, WU C, WILLIAMS P T. Pyrolysis of waste materials using TGA-MS and TGA-FTIR as complementary characterisation techniques[J]. J Anal Appl Pyrolysis, 2012, 94:99-107. doi: 10.1016/j.jaap.2011.11.011
    [23]
    HOTOV G, SLOV K V. Quantitative TG-MS analysis of evolved gases during the thermal decomposition of carbon containing solids[J]. Thermochim Acta, 2016, 632(Supplement C):23-28. https://www.sciencedirect.com/science/article/pii/S0040603115002282
    [24]
    GUO X E, YANG X L, LI H, WU C Z, CHEN Y, LI F, XIE K C. Release of hydrogen chloride from combustibles in municipal solid waste[J]. Environ Sci Technol, 2001, 35(10):2001-2005. doi: 10.1021/es991208r
    [25]
    钱小青, 牛东杰, 楼紫阳, 赵由才.填埋场矿化垃圾资源综合利用研究进展[J].环境卫生工程, 2006, 14(2):62-64. http://www.docin.com/p-6197017.html

    QIAN Xiao-qing, NIU Dong-jie, LOU Zi-yang, ZHAO You-cai. Development of resource comprehensive application study on mineralized waste in landfill Site[J]. Environ Sanit Eng, 2006, 14(2):62-64. http://www.docin.com/p-6197017.html
    [26]
    S RUM L, GR NLI M G, HUSTAD J E. Pyrolysis characteristics and kinetics of municipal solid wastes[J]. Fuel, 2001, 80(9):1217-1227. https://www.sciencedirect.com/science/article/pii/S0016236100002180
    [27]
    WANG X, SI J, TAN H, MA L, POURKASHANIAN M, XU T. Nitrogen, sulfur, and chlorine transformations during the pyrolysis of straw[J]. Energy Fuels, 2010, 24(9):5215-5221. doi: 10.1021/ef1007215
    [28]
    EFIKA E C, ONWUDILI J A, WILLIAMS P T. Products from the high temperature pyrolysis of RDF at slow and rapid heating rates[J]. J Anal Appl Pyrolysis, 2015, 112(Supplement C):14-22. https://www.sciencedirect.com/science/article/pii/S0165237015000054
    [29]
    杜胜磊, 陈汉平, 杨海平, 胥广富, 王贤华, 张世红.生物质热解过程中F和Cl的迁徙行为研究[J].中国电机工程学报, 2010, 30(14):115-120.

    DU Sheng-Lei, CHEN Hai-ping, XU Guang-fu, WNAG Xian-hua, ZHANG Shi-hong. Transformation behavior of F and Cl during biomass pyrolysis[J]. Proc CSEE, 2010, 30(14):115-120.
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