Modelling and optimization for an operating giant gas plant in Egypt

An Egyptian gas-producing plant located in the north of Egypt on the coast of the Mediterranean Sea near Port Said city is designed mainly to receive and treat natural gas produced from offshore wells. The plant designed capacity is around 2800 million standard cubic feet per day (MMSCFD), which giv...

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Main Authors: Mohamed G. Shebl, Abdulaziz M. Abdulaziz, Mai K. Fouad, Nessren M. Farrag
Format: Article
Language:English
Published: Elsevier 2023-06-01
Series:Case Studies in Chemical and Environmental Engineering
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2666016423000282
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author Mohamed G. Shebl
Abdulaziz M. Abdulaziz
Mai K. Fouad
Nessren M. Farrag
author_facet Mohamed G. Shebl
Abdulaziz M. Abdulaziz
Mai K. Fouad
Nessren M. Farrag
author_sort Mohamed G. Shebl
collection DOAJ
description An Egyptian gas-producing plant located in the north of Egypt on the coast of the Mediterranean Sea near Port Said city is designed mainly to receive and treat natural gas produced from offshore wells. The plant designed capacity is around 2800 million standard cubic feet per day (MMSCFD), which gives it a highly appreciated strategic importance. The primary plant process is removing H2S associated with the produced gas using amine solutions. The plant contains seven units called gas trains, which use packed columns for the removal. An additional acid gas removal unit was involved in the early production facility, which uses trays column. This study presented a comprehensive comparison study for the columns, packed versus trays, at different operating conditions, including gas flow rate, gas temperature, lean amine concentration, lean amine flow rate, and lean amine temperature. Two models simulating these systems were built using ASPEN HYSYS V12.1 simulation software. The reliability of the two models was verified by comparing the results with plant actual data. The results showed similar behavior trends with changes in operating conditions to optimize the production capacity. For the early production facility unit, the gas to contactor temperatures has been optimized at 29.5 °C, lean amine temperature at 52 °C with 44.5% concentration. The lean amine temperature for the gas train unit has been optimized at 41.5 °C with a concentration of 36%. Both units were compared under the same operating conditions to determine the economically practical unit.
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spelling doaj.art-fe5c5fa1087d404ea32ea813c811f3822023-05-08T04:09:50ZengElsevierCase Studies in Chemical and Environmental Engineering2666-01642023-06-017100323Modelling and optimization for an operating giant gas plant in EgyptMohamed G. Shebl0Abdulaziz M. Abdulaziz1Mai K. Fouad2Nessren M. Farrag3Cairo University, Faculty of Engineering, Mining, Petroleum, and Metallurgical Engineering Department, EgyptCairo University, Faculty of Engineering, Mining, Petroleum, and Metallurgical Engineering Department, EgyptCairo University, Faculty of Engineering, Chemical Engineering Department, EgyptThe British University in Egypt, Faculty of Engineering, Chemical Engineering Department, Egypt; Corresponding author. El Sherouk City, Cairo, Suez Desert Road, 11837, Egypt.An Egyptian gas-producing plant located in the north of Egypt on the coast of the Mediterranean Sea near Port Said city is designed mainly to receive and treat natural gas produced from offshore wells. The plant designed capacity is around 2800 million standard cubic feet per day (MMSCFD), which gives it a highly appreciated strategic importance. The primary plant process is removing H2S associated with the produced gas using amine solutions. The plant contains seven units called gas trains, which use packed columns for the removal. An additional acid gas removal unit was involved in the early production facility, which uses trays column. This study presented a comprehensive comparison study for the columns, packed versus trays, at different operating conditions, including gas flow rate, gas temperature, lean amine concentration, lean amine flow rate, and lean amine temperature. Two models simulating these systems were built using ASPEN HYSYS V12.1 simulation software. The reliability of the two models was verified by comparing the results with plant actual data. The results showed similar behavior trends with changes in operating conditions to optimize the production capacity. For the early production facility unit, the gas to contactor temperatures has been optimized at 29.5 °C, lean amine temperature at 52 °C with 44.5% concentration. The lean amine temperature for the gas train unit has been optimized at 41.5 °C with a concentration of 36%. Both units were compared under the same operating conditions to determine the economically practical unit.http://www.sciencedirect.com/science/article/pii/S2666016423000282Gas plantPacked columnTray columnASPEN HYSYSEgypt
spellingShingle Mohamed G. Shebl
Abdulaziz M. Abdulaziz
Mai K. Fouad
Nessren M. Farrag
Modelling and optimization for an operating giant gas plant in Egypt
Case Studies in Chemical and Environmental Engineering
Gas plant
Packed column
Tray column
ASPEN HYSYS
Egypt
title Modelling and optimization for an operating giant gas plant in Egypt
title_full Modelling and optimization for an operating giant gas plant in Egypt
title_fullStr Modelling and optimization for an operating giant gas plant in Egypt
title_full_unstemmed Modelling and optimization for an operating giant gas plant in Egypt
title_short Modelling and optimization for an operating giant gas plant in Egypt
title_sort modelling and optimization for an operating giant gas plant in egypt
topic Gas plant
Packed column
Tray column
ASPEN HYSYS
Egypt
url http://www.sciencedirect.com/science/article/pii/S2666016423000282
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AT maikfouad modellingandoptimizationforanoperatinggiantgasplantinegypt
AT nessrenmfarrag modellingandoptimizationforanoperatinggiantgasplantinegypt