Optimal Design and Energy-Saving Investigation of the Triple CO2 Feeds for Methanol Production System by Combining Steam and Dry Methane Reforming

被引:18
作者
Wang, Hong [1 ]
Su, Yang [1 ]
Wang, Dan [1 ]
Jin, Saimeng [1 ]
Wei, Shun'an [1 ]
Shen, Weifeng [1 ]
机构
[1] Chongqing Univ, Chongqing, Peoples R China
基金
中国国家自然科学基金;
关键词
HEAT-EXCHANGER NETWORKS; DIVIDING WALL COLUMN; CARBON-DIOXIDE; EXTRACTIVE DISTILLATION; EXERGY ANALYSIS; GAS; OPTIMIZATION; EFFICIENCY; CATALYSTS; MEMBRANE;
D O I
10.1021/acs.iecr.9b05296
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The process of synthesizing syngas with the triple CO2 feeds is proposed to achieve an efficient use of CO2 that mitigates climate warming. Also, the amount of CO2 added in three locations as the variables of the process is optimized based on the CO2 conversion rate and the energy consumption per unit product (ECP) output flow rate by the genetic algorithm. The performances of the triple CO2 feeds in the methanol synthesis process had been evaluated by comparing with the traditional methanol production processes. To further reduce energy consumption, the irreversibility of each component and the locations of the inefficiency in the overall selected production process are studied on the basis of the exergy analysis. Pinch analysis is further used to find the optimal matching scheme. Compared with those of the proposed process, the energy consumption and the total exergy loss of the heat-integrated process are significantly reduced by 33.1 and 6.65%, respectively. Besides, the overall total annual cost is reduced by 10.1% and the cost of utilities is saved by 36.4%, which results in energy-saving.
引用
收藏
页码:1596 / 1606
页数:11
相关论文
共 49 条
[1]  
Abashar MEE, 2004, INT J HYDROGEN ENERG, V29, P799, DOI [10.1016/j.ijhydene.2003.09.010, 10.1016/j.jjhydene.2003.09.010]
[2]  
Alizadeh A, 2007, INT J CHEM REACT ENG, V5
[3]   Methane Conversion to Syngas for Gas-to-Liquids (GTL): Is Sustainable CO2 Reuse via Dry Methane Reforming (DMR) Cost Competitive with SMR and AIR Processes? [J].
Baltrusaitis, Jonas ;
Luyben, William L. .
ACS SUSTAINABLE CHEMISTRY & ENGINEERING, 2015, 3 (09) :2100-2111
[4]  
Blumberg T., 2018, THESIS
[5]   CO2-utilization in the synthesis of methanol: Potential analysis and exergetic assessment [J].
Blumberg, Timo ;
Morosuk, Tatiana ;
Tsatsaronis, George .
ENERGY, 2019, 175 :730-744
[6]   Exergy-based evaluation of methanol production from natural gas with CO2 utilization [J].
Blumberg, Timo ;
Morosuk, Tatiana ;
Tsatsaronis, George .
ENERGY, 2017, 141 :2528-2539
[7]   Exergoenvironmental analysis of a steam methane reforming process for hydrogen production [J].
Boyano, A. ;
Blanco-Marigorta, A. M. ;
Morosuk, T. ;
Tsatsaronis, G. .
ENERGY, 2011, 36 (04) :2202-2214
[8]   Reducing the cost, environmental impact and energy consumption of biofuel processes through heat integration [J].
Brunet, Robert ;
Boer, Dieter ;
Guillen-Gosalbez, Gonzalo ;
Jimenez, Laureano .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 93 :203-212
[9]   Process integration of dimethyl carbonate and ethylene glycol production from biomass and heat exchanger network design [J].
Choomwattana, Chayanit ;
Chaianong, Aksornchan ;
Kiatkittipong, Worapon ;
Kongpanna, Pichayapan ;
Quitain, Armando T. ;
Assabumrungrat, Suttichai .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2016, 107 :80-93
[10]   Low temperature dry methane reforming over Ce, Zr and CeZr promoted Ni-Mg-Al hydrotalcite-derived catalysts [J].
Debek, Radoslaw ;
Galvez, Maria Elena ;
Launay, Franck ;
Motak, Monika ;
Grzybek, Teresa ;
Da Costa, Patrick .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (27) :11616-11623