Metal sulfide-based process analysis for hydrogen generation from hydrogen sulfide conversion

被引:27
作者
Reddy, Sharath [1 ]
Nadgouda, Sourabh G. [1 ]
Tong, Andrew [1 ]
Fan, L. -S. [1 ]
机构
[1] Ohio State Univ, William G Lowrie Dept Chem & Biomol Engn, 340 A Koffolt Labs,151 West Woodruff Ave, Columbus, OH 43210 USA
关键词
Sulfur recovery; Iron sulfide-based chemical looping; H-2; production; Exergy analysis; Energy analysis; Staged H-2 separation; CHEMICAL-LOOPING COMBUSTION; CATALYTIC DECOMPOSITION; THERMAL-DECOMPOSITION; SYNGAS PRODUCTION; H2S; SULFUR; METHANE; FATE; GAS; DESULFURIZATION;
D O I
10.1016/j.ijhydene.2019.06.180
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Fossil fuel power plants often generate sulfur species such as hydrogen sulfide or sulfur dioxide due to the sulfur content of the raw feedstocks. To combat the associated environmental, processing, and corrosion issues, facilities commonly utilize a Claus process to convert hydrogen sulfide (H2S) to elemental sulfur. Unfortunately, the potential for H-2 production from H2S is lost in the Claus process. In this study, two chemical looping process configurations utilizing metal sulfides as chemical intermediates for sulfur recovery are investigated: (1) sulfur recovery (SR) system for sulfur production; (2) sulfur and hydrogen (H-2) recovery (SHR) system for sulfur and H-2 and production utilizing staged H-2 separation. Since, H-2 yield and sulfur recovery in a single thermal decomposition reactor is limited by low H2S equilibrium conversion, a staged H-2 separation approach is used to increase H2S conversion to H-2 using the SHR system. Steady-state simulations and optimization of process conditions are conducted in Aspen Plus (v10) simulation software for the chemical looping process configurations and the Claus process. An energy and exergy analysis are done for the Claus and chemical looping processes to demonstrate the relative contribution to exergy destruction from different unit operations as well as overall exergy and energy efficiency. The two chemical looping process configurations are compared against the conventional Claus process for similar sulfur recovery in a 629 MWe integrated gasification combined cycle power plant. The SHR system is found to be the most efficient option due to a 97.11% exergy efficiency with 99.31% H-2 recovery. The overall energy and exergy efficiencies of this chemical looping system are 14.74% and 21.54% points higher than the Claus process, respectively, suggesting more efficient use of total input energy. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21336 / 21350
页数:15
相关论文
共 54 条
[1]   Syn-gas from waste: the reduction of CO2 with H2S [J].
Alderman, Nicholas P. ;
Peneau, Virginie ;
Viasus, Camilo J. ;
Korobkov, Ilia ;
Vidjayacoumar, Balamurugan ;
Albahily, Khalid ;
Gambarotta, Sandro .
REACTION CHEMISTRY & ENGINEERING, 2019, 4 (04) :763-771
[2]   Environmental impact of a coal combustion-desulphurisation plant:: Abatement capacity of desulphurisation process and environmental characterisation of combustion by-products [J].
Alvarez-Ayuso, E. ;
Querol, X. ;
Tomas, A. .
CHEMOSPHERE, 2006, 65 (11) :2009-2017
[3]  
[Anonymous], 2013, Cost and performance baseline for fossil energy plants volume 1: Bituminous coal and natural gas to electricity, V1
[4]  
Appendix A, 1985, The exergy method of thermal plant analysis, P236
[5]   Catalytic transformation of H2S for H2 production [J].
Burra, Kiran Raj G. ;
Bassioni, Ghada ;
Gupta, Ashwani K. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (51) :22852-22860
[6]   Thermodynamic Analysis of Alternative Approaches to Chemical Looping Combustion [J].
Chakravarthy, V. Kalyana ;
Daw, C. Stuart ;
Pihl, Josh A. .
ENERGY & FUELS, 2011, 25 (02) :656-669
[7]   THE THERMAL-DECOMPOSITION OF HYDROGEN-SULFIDE OVER TRANSITION-METAL SULFIDES [J].
CHIVERS, T ;
HYNE, JB ;
LAU, C .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1980, 5 (05) :499-506
[9]   Fate of sulfur in coal-direct chemical looping systems [J].
Chung, Cheng ;
Pottimurthy, Yaswanth ;
Xu, Mingyuan ;
Hsieh, Tien -Lin ;
Xu, Dikai ;
Zhang, Yitao ;
Chen, Yu -Yen ;
He, Pengfei ;
Pickarts, Marshall ;
Fan, Liang-Shih ;
Tong, Andrew .
APPLIED ENERGY, 2017, 208 :678-690
[10]   Economics of thermal dissociation of H2S to produce hydrogen [J].
Cox, BG ;
Clarke, PF ;
Pruden, BB .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1998, 23 (07) :531-544