A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production

In this paper, an integrated process for coproduction of methanol (122500 [Formula presented]), desalinated water (40.56 [Formula presented]), and oxygen (13420 [Formula presented]) using landfill gas upgrading is presented. The process embraces negative carbon dioxide (CO2) emission framework, high...

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Published in:Journal of Cleaner Production
Main Author: Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
Format: Article
Language:English
Published: Elsevier Ltd 2023
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85149325586&doi=10.1016%2fj.jclepro.2023.136224&partnerID=40&md5=1c3b6b417787fbcc998efc9fb1d11a32
id 2-s2.0-85149325586
spelling 2-s2.0-85149325586
Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
2023
Journal of Cleaner Production
393

10.1016/j.jclepro.2023.136224
https://www.scopus.com/inward/record.uri?eid=2-s2.0-85149325586&doi=10.1016%2fj.jclepro.2023.136224&partnerID=40&md5=1c3b6b417787fbcc998efc9fb1d11a32
In this paper, an integrated process for coproduction of methanol (122500 [Formula presented]), desalinated water (40.56 [Formula presented]), and oxygen (13420 [Formula presented]) using landfill gas upgrading is presented. The process embraces negative carbon dioxide (CO2) emission framework, high thermodynamic efficiency, and low product cost. The proposed process consists of nine subsystems, which are utilized for heat recovery in addition to production of electricity and desalinated water. Results showed that the total energy and exergy efficiencies of the trigeneration system are 59.19% and 48%, respectively. According to the conducted analysis, the total exergy destruction rate equals 973291 kW in which the biogas upgrading unit has an 80% contribution. In addition, it is demonstrated that the combustor of the biogas upgrading unit is responsible for 57.96% of the total exergy destruction rate. Moreover, the sensitivity analysis illustrates that the increase in the [Formula presented] ratio is an important factor in increasing the carbon efficiency and total energy efficiency, and decreasing the CO2 emission. From the environmental perspective, it is deduced that the total net emission of the proposed process is −0.6773 [Formula presented], which is significantly lower than other methanol production technologies. Economic analysis is performed for the integrated structure and its results showed that the total annual cost and methanol production cost rate are 124,660,373 $ and 0.124 [Formula presented], respectively. This value is 91.68% lower than the renewable methanol production technology. © 2023
Elsevier Ltd
09596526
English
Article

author Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
spellingShingle Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
author_facet Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
author_sort Hai T.; Lin H.; Albdeiri M.S.; Alsenani T.R.; Elattar S.; Abed A.M.; Tian R.
title A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
title_short A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
title_full A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
title_fullStr A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
title_full_unstemmed A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
title_sort A novel trigeneration model using landfill gas upgrading process and waste heat recovery: Application of methanol, desalinated water, and oxygen production
publishDate 2023
container_title Journal of Cleaner Production
container_volume 393
container_issue
doi_str_mv 10.1016/j.jclepro.2023.136224
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85149325586&doi=10.1016%2fj.jclepro.2023.136224&partnerID=40&md5=1c3b6b417787fbcc998efc9fb1d11a32
description In this paper, an integrated process for coproduction of methanol (122500 [Formula presented]), desalinated water (40.56 [Formula presented]), and oxygen (13420 [Formula presented]) using landfill gas upgrading is presented. The process embraces negative carbon dioxide (CO2) emission framework, high thermodynamic efficiency, and low product cost. The proposed process consists of nine subsystems, which are utilized for heat recovery in addition to production of electricity and desalinated water. Results showed that the total energy and exergy efficiencies of the trigeneration system are 59.19% and 48%, respectively. According to the conducted analysis, the total exergy destruction rate equals 973291 kW in which the biogas upgrading unit has an 80% contribution. In addition, it is demonstrated that the combustor of the biogas upgrading unit is responsible for 57.96% of the total exergy destruction rate. Moreover, the sensitivity analysis illustrates that the increase in the [Formula presented] ratio is an important factor in increasing the carbon efficiency and total energy efficiency, and decreasing the CO2 emission. From the environmental perspective, it is deduced that the total net emission of the proposed process is −0.6773 [Formula presented], which is significantly lower than other methanol production technologies. Economic analysis is performed for the integrated structure and its results showed that the total annual cost and methanol production cost rate are 124,660,373 $ and 0.124 [Formula presented], respectively. This value is 91.68% lower than the renewable methanol production technology. © 2023
publisher Elsevier Ltd
issn 09596526
language English
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