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Production of syngas from steam gasification of three different ranks of coals and related reaction kinetics
Affiliation:1. College of Chemical Engineering, Inner Mongolia University of Technology, Inner Mongolia Key Laboratory of High-Value Functional Utilization of Low Rank Carbon Resources, Hohhot 010051, China;2. College of Chemical Engineering, Ordos Institute of Technology, Ordos 017000, China;1. Lucerne University of Applied Sciences and Arts, Technikumstrasse 21, 6048 Horw, Switzerland;2. Verenum Research, Langmauerstrasse 109, 8006 Zürich, Switzerland;3. Schmid AG Energy Solutions, Hörnlistrasse 12, 8360 Eschlikon, Switzerland;4. Schmid Energy Solutions GmbH, Austraße 10, 2871 Zöbern, Austria;1. School of Energy and Environment, Anhui University of Technology, Maanshan 243002, Anhui Province, PR China;2. Key Laboratory of Metallurgical Emission Reduction & Resources Recycling (Anhui University of Technology), Ministry of Education, Maanshan 243002, Anhui Province, PR China;3. Department of Chemical Engineering and Research Center for Circular Economy, Chung Yuan Christian University, Chung-Li District, Tao-Yuan 32023, Taiwan, Republic of China;1. Key Laboratory of Metallurgical Emission Reduction & Resources Recycling (Anhui University of Technology), Ministry of Education, Maanshan 243002, Anhui Province, PR China;2. Anhui Province Key Laboratory of Metallurgical Engineering & Resources Recycling (Anhui University of Technology), 243002 Maanshan, PR China;3. School of Energy and Environment, Anhui University of Technology, Maanshan 243002, Anhui Province, PR China;1. State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Wuhan Hubei Province, 430074, China;2. North China Power Engineering Co., Ltd, China Power Engineering Consulting Group, Beijing, 100120, China
Abstract:The steam gasification properties of three different ranks of coals, Shengli lignite (SL), Shenhua subbituminous coal (SH), and Tavan Tolgoi anthracite (TT), were investigated using a lab-scale fixed-bed reactor, and the thermodynamic equilibrium constant and kinetics of the reaction were analyzed. The results showed that the aromaticity and condensation of aromatic structures in SL, SH, and TT became higher, and the maturity of organic substance became lower. The steam gasification reaction showed that the syngas from low-rank SL had a high H2/CO molar ratio, while the syngas from high-rank TT had relatively high CO content. The direct carbon gasification reactions for these three different ranks of coals were far from in equilibrium; the water gas shift reaction of SL was near equilibrium, and the degree of reaction for SL was higher than that of SH and TT. We studied a random pore model (RPM), shrinking core model (SCM), and hybrid model (HM), and the hybrid model was found to be the most suitable model of the three for fitting the steam gasification reactions of the three types of coal. It had high fitting correlation coefficient R2 values (ranging from 0.9939 to 0.9990) and small average error θ values (ranging from 0.009 to 0.016). The apparent activation energy E values of SL, SH, and TT fitted by HM were 179.10, 48.14, and 63.06 kJ/mol, respectively, and the corresponding pre-exponential factor k0 values were 3.14 × 107, 1.01, and 1.22 min−1, respectively. This study finds that the steam gasification of SL, SH, and TT coal samples consists of homogeneous phase reaction and shrinking core reaction.
Keywords:Coal  Steam gasification  Syngas  Kinetics  SL"}  {"#name":"keyword"  "$":{"id":"kwrd0035"}  "$$":[{"#name":"text"  "_":"Shengli lignite  SH"}  {"#name":"keyword"  "$":{"id":"kwrd0045"}  "$$":[{"#name":"text"  "_":"Shenhua subbituminous coal  TT"}  {"#name":"keyword"  "$":{"id":"kwrd0055"}  "$$":[{"#name":"text"  "_":"Tavan Tolgoi anthracite  HM"}  {"#name":"keyword"  "$":{"id":"kwrd0065"}  "$$":[{"#name":"text"  "_":"hybrid model  RPM"}  {"#name":"keyword"  "$":{"id":"kwrd0075"}  "$$":[{"#name":"text"  "_":"random pore model  SCM"}  {"#name":"keyword"  "$":{"id":"kwrd0085"}  "$$":[{"#name":"text"  "_":"shrinking core model  apparent activation energy  pre-exponential factor  ad"}  {"#name":"keyword"  "$":{"id":"kwrd0115"}  "$$":[{"#name":"text"  "_":"air dried basis  d"}  {"#name":"keyword"  "$":{"id":"kwrd0125"}  "$$":[{"#name":"text"  "_":"dried basis  correlation coefficients  average errors
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