Transformation Characteristics of Hydrogen-Donor Solvent Tetralin in the Process of Direct Coal Liquefaction

被引:14
作者
Chang, Hai-zhou [1 ]
Li, Jun-qi [1 ]
Du, Shuai [2 ]
Shen, Kai-yuan [1 ]
Yang, Qun [3 ]
Yi, Han [1 ]
Zhang, Ji-wei [1 ]
机构
[1] Univ Shanghai Sci & Technol, Coll Sci, Shanghai, Peoples R China
[2] SGS CSTC Stand Tech Serv Co Ltd, Shenzhen, Guangdong, Peoples R China
[3] Univ Shanghai Sci & Technol, Sch Mech Engn, Shanghai, Peoples R China
基金
中国国家自然科学基金;
关键词
coal liquefaction; tetralin; oil analysis; Gas analysis; transformation (of products); PRODUCT DISTRIBUTION; STRUCTURAL-CHANGE; PREHEATING STAGE; THERMOLYSIS; MECHANISM;
D O I
10.3389/fchem.2019.00737
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The aim of this study is to investigate the transformation of hydrogen-donor solvent tetralin in the direct liquefaction process of coal. Pure tetralin liquid as well as mixture of tetralin and Wucaiwan coal (WCW) were separately reacted under a liquefaction condition, and constituents of liquid product were analyzed by GC-MS. The results show that after the tetralin liquid reacts with high-pressure hydrogen, 90% of the reaction product is in liquid state, the gaseous products mainly include alkane gas and COx gas. When the reaction temperatures were set at 380 and 420 degrees C, respectively, the corresponding transformation rates of tetralin can be 34.72 and 52.74%. At 380 degrees C, the tetralin mainly plays a role of passing active hydrogen, while at 420 degrees C, it mainly occurs dehydrogenation transformation to provide active hydrogen, as well as generate naphthalene, methyl indan, and substituted benzene, etc. Taking tetralin as the hydrogen-donor solvent, the WCW was performed liquefaction reaction, and the obtained results show that the transformation rates of tetralin are 69.76 and 83.86% at liquefaction temperatures of 380 and 420 degrees C, respectively. Tetralin mainly occur to dehydrogenation transformation to generate naphthalene, followed by methyl indan, where contents order of main constituents of the liquefaction products were: naphthalene> tetralin > methyl indan.
引用
收藏
页数:6
相关论文
共 18 条
[1]   Effect of solvent and atmosphere on product distribution, hydrogen consumption and coal structural change during preheating stage in direct coal liquefaction [J].
Hao, Pan ;
Bai, Zongqing ;
Hou, Ranran ;
Xu, Junli ;
Bai, Jin ;
Guo, Zhenxing ;
Kong, Lingxue ;
Li, Wen .
FUEL, 2018, 211 :783-788
[2]   Study on the preheating stage of low rank coals liquefaction: Product distribution, chemical structural change of coal and hydrogen transfer [J].
Hao, Pan ;
Bai, Zong-Qing ;
Zhao, Zhi-Tong ;
Yan, Jing-Chong ;
Li, Xiao ;
Guo, Zhen-Xing ;
Xu, Jun-Li ;
Bai, Jin ;
Li, Wen .
FUEL PROCESSING TECHNOLOGY, 2017, 159 :153-159
[3]   Rational Design of Hydrogen-Donor Solvents for Direct Coal Liquefaction [J].
Hou, Peidong ;
Zhou, Yuwei ;
Guo, Wenping ;
Ren, Pengju ;
Guo, Qiang ;
Xiang, Hongwei ;
Li, Yong-Wang ;
Wen, Xiao-Dong ;
Yang, Yong .
ENERGY & FUELS, 2018, 32 (04) :4715-4723
[4]   Elucidation of hydrogen transfer between coal and tritiated organic solvent [J].
Ishihara, A ;
Sutrisna, IP ;
Miura, T ;
Saito, M ;
Qian, EW ;
Kabe, T .
ENERGY & FUELS, 2002, 16 (06) :1490-1498
[5]  
Li G., 2007, CLEAN COAL TECHNOL, V37, P22, DOI [10.3321/j.issn:0253-9993.2007.09.018, DOI 10.3321/J.ISSN:0253-9993.2007.09.018]
[6]   HYDROGEN-TRANSFERRING LIQUEFACTION OF AN AUSTRALIAN BROWN COAL WITH POLYHYDROGENATED CONDENSED AROMATICS - ROLES OF DONOR IN THE LIQUEFACTION [J].
MOCHIDA, I ;
TAKAYAMA, A ;
SAKATA, R ;
SAKANISHI, K .
ENERGY & FUELS, 1990, 4 (01) :81-84
[7]   LIQUEFACTION OF COAL IN HYDROGEN-DONOR AND NON-DONOR VEHICLES [J].
NEAVEL, RC .
FUEL, 1976, 55 (03) :237-242
[8]  
[任相坤 REN Xiangkun], 2010, [化工进展, Chemical Industry and Engineering Progress], V29, P198
[9]  
Shu G, 2003, COAL LIQUEFACTION TE
[10]   Recent Advances in Direct Coal Liquefaction [J].
Shui, Hengfu ;
Cai, Zhenyi ;
Xu, Chunbao .
ENERGIES, 2010, 3 (02) :155-170