Process Simulation for Converting CO2 Emissions from the Cement Industry to Dimethyl Ether

被引:0
|
作者
Essam, Mohamed [1 ]
Gad, Fatma [1 ]
Abouseada, Nour [2 ]
Soliman, Moustafa Aly [2 ]
Aboelela, Dina [2 ]
机构
[1] Suez Univ, Fac Petr & Min Engn, Dept Chem & Refinery Engn, Suez, Egypt
[2] British Univ Egypt BUE, Fac Energy & Environm Engn, Cairo 11837, Egypt
关键词
Dimethyl ether; Methanol; Process simulation; Reduction of CO2; Green hydrogen; CARBON-DIOXIDE EMISSIONS; HYDROGENATION; METHANOL; REACTOR; SYNGAS; MODEL;
D O I
10.1007/s13369-024-09530-4
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
Climate change is the leading severe problem in the twenty-first century, which is associated with greenhouse gas emissions, carbon dioxide that is the foremost cause of global warming and super greenhouse effect. In this concern, to avoid hazardous problems, the steady stream of CO2 effluents existing in the atmosphere must be transformed to beneficial products for being used as an abundant chemical feedstock. Implementing a new green strategy, which is known for the catalytic hydrogenation of CO2 into alternative fuels and valuable chemicals, will be a long-lasting solution to alleviate CO2 emissions. In this paper, a process simulation showing the synthesis of dimethyl ether (DME) from CO2 hydrogenation (CO2 produced from EL-Sewedy cement industry) is performed using Aspen HYSYS V10 to attain a complete distinctive design for all equipment for producing a capacity of 475,000 tons per year, while energy integration is performed using Energy Analyzer Simulation software. In the main model, catalytic dehydration is done in a single-pass reactor, and then separation in multi-column product separations. Other configurations were tested by developing three simulation models with different reactors, a double pipe reactor and membrane reactor were with the aim of modification for higher energy efficiency and lower operating and capital costs. Moreover, an economic and environmental study was obtained for the basic & the integrated case, which showed that the total annual/capital costs based on the "base case" are estimated to be 90 million USD without heat integration while the optimum and integrated costs are found to be 100 Million USD. Finally, process optimization and integration were obtained to reduce the utilized energy of the hot & cold utilities by 90% and 60%, respectively.
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页数:12
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