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泥煤在超临界水中气化实验研究

Study on Peat Gasification in Supercritical Water
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摘要 采用间歇式超临界水气化装置对泥煤进行气化实验,系统研究了催化剂、反应温度、反应时间对泥煤气化效果的影响。结果表明:四种催化剂均可将煤转化率从79%提高到95%以上,其中以KOH为催化剂时H_2和CH_4的产率最高,分别达到了422mL/(g daf coal)和184 mL/(g daf coal)。在催化剂存在条件下,温度升高和延长反应时间均可促进H_2和CH_4的生成。温度650℃时CH_4产率是550℃时的2.6倍。当停留时间达到30 min时,H_2和CH_4的产率分别达到了555 ml/(g daf coal)和212 ml/(g daf coal)。 The gasification of peat was studied by supercritical water in a batch autoclave.The influences of four catalysts,reaction temperature and residence time on gasification of peat were investigated.The results showed that coal conversion rate can be increased from 79%to over 95%on a basis of catalyst addition.Highest yields of H 2 and CH 4 can be acquired with KOH as catalyst,reaching 422 mL/(g daf coal)and 184 mL/(g daf coal),respectively.In the presence of catalyst,the amount of H 2 and CH 4 from peat can be promoted by improving temperature and residence time.The yield of CH 4 at temperature of 650℃was 2.6 times than that of 550℃.When the residence time was 30 min,the yields of H 2 and CH 4 reached 555 mL/(g daf coal)and 212mL/(g daf coal),respectively.
作者 高志远 祖静茹 程乐明 宋成才 王青 马江山 聂俊国 GAO Zhi-yuan;ZU Jing-ru;CHENG Le-ming;SONG Cheng-cai;WANG Qing;MA Jiang-shan;NIE Jun-guo(ENN Evnirotech Corporation Ltd.,Hebei Langfang 065001;ENN Science and Technology Development Corporation Ltd.,Hebei Langfang 065001,China)
出处 《广州化工》 CAS 2018年第6期52-55,共4页 GuangZhou Chemical Industry
关键词 超临界水 泥煤 气化 催化剂 supercritical water peat gasification catalyst
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  • 1闫秋会,郭烈锦,张西民,吕友军,梁兴.超临界水中葡萄糖气化制氢的热力学分析[J].化工学报,2004,55(11):1916-1920. 被引量:10
  • 2闫秋会,郭烈锦,梁兴,张西民.煤与生物质共超临界水催化气化制氢的实验研究[J].西安交通大学学报,2005,39(5):454-457. 被引量:17
  • 3苏晓丽,赵玉龙,张荣,毕继诚.加热速率和粒径对聚乙烯在超临界水中转化的影响[J].燃料化学学报,2006,34(4):509-511. 被引量:3
  • 4Phllip E Savage,Sudhama Gopalan,Tahmid I,et al.Reaction at supercritical conditions:applications and fundamentals[J].AIChE,1995,41(7):1723-1778.
  • 5Shiying Lin,Michiaki Harada,et al.Continuous experiment regarding hydrogen production by coal/CaO reaction with steam (Ⅰ) gas products[J].Fuel,2004(83):869-874.
  • 6Shying Lin,Michiaki Harada,Yoshizo Suzuki,et al.Hydrogen production from coal by separating carbon dioxide during gasification[J].Fuel,2002,81:2079-2085.
  • 7Hong G T,Spitzer M H.Supercritical water partial oxidation[C].Proceedings of the 2002 U S DOE Hydrogen Program Review NREL/CP-610-32405.1-18.
  • 8MATSUMURA Y, NONAKA H, YOKURA H, et al. Co-liquefaction of coal and cellulose in supercritical water [J]. Fuel, 1999, 78(9): 1049-1056.
  • 9PHILLIP E S, SUDHAMA G, TAHMID I, et al. Reactions at supercritical water conditions: applications and fundamentals [J]. AIChE J, 1995, 41 (7) : 1723-1778.
  • 10郭烈锦,闫秋会,张西民.煤与生物质共超临界水催化气化制氢装置及方法:中国,10041633.8[P].2007-01-03.

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