[1]孙立,张晓东. 生物质热解气化原理与技术[M]. 北京:化学工业出版社,2013.
[2]SCARLAT N, DALLEMAND J F, MONFORTIFERRARIO F, et al. The role of biomass and bioenergy in a future bioeconomy: Policies and facts[J]. Environmental Development, 2015, 15: 334.
[3]李新禹, 苏文. 生物质能用于热电冷三联供系统的可行性[J]. 能源工程, 2005(4): 1416.
[4]FABRY F, REHMET C, ROHANI V, et al. Waste gasification by thermal plasma: A review[J]. Waste & Biomass Valorization, 2013, 4(3): 421439.
[5]孙立, 张晓东. 生物质发电产业化技术[M]. 北京: 化学工业出版社, 2011.
[6]肖艳京, 马隆龙.生物质在流化床中的气化实验[J]. 节能, 1999 (10): 79.
[7]车德勇, 李少华, 杨文广,等.稻壳在固定床中空气气化的数值模拟[J]. 太阳能学报, 2013, 34(1): 100104.
[8]朱锡锋. 生物质热解原理与技术[M]. 合肥: 中国科技大学出版社, 2006.
[9]孟凡彬, 王贵路, 李晓伟,等. 高当量比生物质氧气气化试验研究[J]. 太阳能学报, 2013, 34(3): 377381.
[10]李斌, 陈汉平, 杨海平,等.基于Aspen Plus 平台的生物质氧气气化制备合成气的模拟研究[J]. 燃烧科学与技术, 2011, 17(5): 432436.
[11]FISHER E M, DUPONT C, DARVELL L I, et al. Combustion and gasification characteristics of chars from raw and torrefied biomass[J]. Bioresource Technology, 2012, 119: 157165.
[12]李琳娜, 应浩, 涂军令,等. 木屑高温水蒸气气化制备富氢燃气的特性研究[J]. 林产化学与工业, 2011, 31(5): 1824.
[13]肖军, 沈来宏, 邓霞,等. 秸秆类生物质加压气化特性研究[J]. 中国电机工程学报, 2009, 29(5): 103108.
[14]应浩, 涂军令, 江俊飞,等. 木屑高温水蒸气气化制备合成气研究[J]. 太阳能学报, 2014, 35(3): 379383.
[15]张建安, 刘德华. 生物质能源利用技术[M]. 北京: 化学工业出版社, 2009.
[16]BAKER G, MUDGE L K, MITCHELL D H. Oxygen/steam gasification of wood in a fixedbed gasifier[J]. Industrial and Engineering Chemistry Process Design and Development, 1984, 23(4): 725728.
[17]GIL J, AZNAR M P, CABALLERO M A.et al. Biomass gasification in fluidized bed at pilot scale with steamoxygen mixtures product distribution for very different operating conditions[J]. Energy and Fuels, 1997, 11(6): 11091118.
[18]赵先国, 常杰, 吕鹏梅, 等. 生物质富氧水蒸气气化制氢特性研究[J]. 太阳能学报, 2006, 27(7): 677681.
[19]苏德仁, 刘华财, 周肇秋, 等. 生物质流化床氧气水蒸气气化实验研究[J]. 燃料化学学报, 2012, 40(3): 309314.
[20]寇公. 煤炭气化工程[M]. 北京: 机械工业出版社, 1992.
[21]马承荣, 肖波, 杨家宽, 等. 生物质热解影响因素研究[J]. 环境技术, 2005, 23(5): 1012.
[22]SESHADRI K S, SHAMSI A. Effects of temperature, pressure and carrier gas on the cracking of coal tar over a char dolomite mixture and calcined dolomite fixed bed reactor[J]. Industrial and Engineering Chemistry Research, 1998, 37 (10): 38303837.
[23]郭飞强, 董玉平, 董磊,等. 主动配气下生物质气化焦油热裂解特性试验[J]. 农业机械学报, 2011, 42(7): 135138.
[24]ZOU W J, SONG C C, XU S P, et al. Biomass gasification in an external circulating countercurrent moving bed gasifier[J]. Fuel, 2013, 112: 635640.
[25]SUTTON D,KELLEHER B, ROSS J R H. Review of literature on catalysts for biomass gasification[J]. Fuel Processing Technology, 2001, 73(3): 155173.
[26]MUN T Y,KIM J W,KIM J S. Air gasification of railroad wood ties treated with creosote: Effects of additives and their combination on the removal of tar in a twostage gasifier[J]. Fuel, 2012, 102: 326332.
[27]孙云娟, 蒋剑春. 生物质热解气化行为的研究[J]. 林产化学与工业, 2007, 27(3): 1520.
[28]ZHAO B F, ZHANG X D, CHEN L, et al. High quality fuel gas from biomass pyrolysis with calcium oxide[J]. Bioresource Technology, 2014, 156: 7883.
[29]XUE A J, PAN J H, TIAN M C, et al. Experimental study on catalytic pyrolysis of biomass pellet[J]. Applied Mechanics and Materials, 2013,291/292/293/294: 320323.
[30]闵凡飞, 张明旭, 陈清如, 等. 新鲜生物质催化热解气化制富氢燃料气的试验研究[J]. 煤炭学报, 2006,31(5): 649653.
[31]JORDAN C A,AKAY G. Effect of CaO on tar production and dew point depression during gasification of fuel cane bagasse in a novel downdraft gasifier[J]. Fuel Processing Technology, 2013, 106: 654660.
[32]TARALAS G, KONTOMINAS M G. Kinetic modeling of VOC catalytic steam pyrolysis for tar abatement phenomena in gasification/pyrolysis technologies[J]. Fuel, 2004, 83(9): 12351245.
[33]SUTTON D, KELLEHER B, ROSS J R H. Catalytic conditioning of organic volatile products by peat pyrolysis[J]. Biomass&Bioenergy, 2002, 23(3): 209216.
[34]CABALLERO M A, AZNAR M P, GIL J, et al. Commercial steam reforming catalysts to improve biomass gasification with steamoxygen mixture.1. Hot gas upgrading by the catalytic reactor [J]. Industrial and Engineering Chemistry Research, 1997, 36(12): 52275239.
[35]LIU H B,CHEN T H, CHANG D Y, et al. Effect of preparation method of palygorskitesupported Fe and Ni catalysts on catalytic cracking of biomass tar[J]. Chemical Engineering Journal, 2012, 188: 108112.
[36]LIU H B, CHEN T H, CHANG D Y, et al. Catalytic cracking of tars derived from rice hull gasification over goethite and palygorskite[J]. Applied Clay Science, 2012, 70:5157.
[37]王铁军, 常杰, 吴创之,等. 生物质气化焦油催化裂解特性[J]. 太阳能学报, 2003, 24(3): 376379.
[38]KUMAGAI S,ALVAREZ J, BLANCO P H, et al. Novel NiMgAlCa catalyst for enhanced hydrogen production for the pyrolysisgasification of a biomass plastic mixture[J]. Journal of Analytical and Applied Pyrolysis, 2015, 113: 15-21.
[39]李斌, 韩旭, 陈义龙,等. 钙基催化吸收剂对玉米秸秆热解气化制氢特性的影响[J]. 农业机械学报, 2016,47(8): 216220.
[40]DU C M, MO J M, LI H X. Renewable hydrogen production by alcohols reforming using plasma and plasmaCatalytic technologies: challenges and opportunities[J]. Chemical Reviews, 2015, 115(3): 15031542.
[41]KIM S C, LIM M S, CHUN Y N. Hydrogenrich gas production from a biomass pyrolysis by using a plasmatron[J]. International Journal of Hydrogen Energy, 2013, 38(34): 1445814466.
[42]赵增立, 李海滨, 吴创之,等. 生物质等离子体气化研究[J]. 太阳能学报, 2005, 26(4): 468472.
[43]吴昂山, 聂勇, 孙艳朋,等. 纤维素在等离子体射流水平床内热解气化特性[J]. 化学工程, 2010, 12: 8084.
[44]BALGARANOVA J. Plasma chemical gasification of sewage sludge[J]. Waste Management & Research, 2003, 21(1): 3841.
[45]黄耕. 等离子气化技术在固体废物处理中的应用[J]. 中国环保产业, 2010(6): 4345.
[46]GUO Y, WANG S Z, XU D H, et al. Review of catalytic supercritical water gasification for hydrogen production from biomass[J]. Renewable and Sustainable Energy Reviews, 2010, 14(1): 334343.
[47]HUANG H J, YUAN X Z.Recent progress in the direct liquefaction of typical biomass[J]. Progress in Energy and Combustion Science, 2015, 49: 5980.
[48]MODELL M. Processing methods for the oxidation of organics in supercritical water: US, 4338199 [P]. 19820706.
[49]闫秋会, 郭烈锦, 吕友军. 生物质/煤超临界水气化制氢的主要影响因素[J]. 西安交通大学学报, 2008, 42(3): 368371.
[50]徐雪松. 超临界水氧化处理油性污泥工艺参数优化的研究[D]. 石河子: 石河子大学, 2016.
[51]邵瑞华, 司全印, 房平. 超临界水氧化法处理固体废物的研究进展[J]. 化工环保, 2008, 28(2): 122126.
[52]项阳阳, 周劲松, 吴何来. 超临界流体在生物质转化技术中的应用[J]. 化工进展, 2012, 31(s1): 3035. |