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

Abstract 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 CO 2 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 CO 2 into alternative fuels and valuable chemicals, will be a long-lasting solution to alleviate CO 2 emissions. In this paper, a process simulation showing the synthesis of dimethyl ether (DME) from CO 2 hydrogenation (CO 2 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.

Authors

Institutions

Publication Details

Journal
Arabian Journal for Science and Engineering
Published
2024-09-13
DOI
https://doi.org/10.1007/s13369-024-09530-4
Citations
1
Primary Topic
Catalysts for Methane Reforming
Type
article
Field-Weighted Citation Impact
0.11

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

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

Dina Aboelela, Nour Abouseada, M.A. Soliman, Mohamed Essam et al.
1 citations
Arabian Journal for Science and Engineering
Catalysts for Methane Reforming
0.11
article

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

Dina Aboelela, Nour Abouseada, M.A. Soliman, Mohamed Essam, Fatma Gad
article en
1 citations

Abstract

Abstract 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 CO 2 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 CO 2 into alternative fuels and valuable chemicals, will be a long-lasting solution to alleviate CO 2 emissions. In this paper, a process simulation showing the synthesis of dimethyl ether (DME) from CO 2 hydrogenation (CO 2 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.

Arabian Journal for Science and EngineeringVol. 50(6)
Suez University (EG), British University in Egypt (EG)
British University in Egypt
Affordable and clean energy
Openalex Percentile: Top 67%
Catalysts for Methane Reforming
0.11
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.