Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity

The increase in demand of residue due to new production of Group III Lube Base Oil Product in Melaka Refmery required the residue plant to increase the feeding capacity of residue to the required unit. For the plant to achieve the targeted flow rate of the residue, the residue plant has upgraded...

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Main Author: Abd Rashid @ Abd Rasip, Mohd Hanafi
Format: Final Year Project
Language:English
Published: Universiti Teknologi Petronas 2009
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Online Access:http://utpedia.utp.edu.my/8817/1/2009%20Bachelor%20-%20Design%20Calculation%20Of%20The%20Upgraded%20Equipments%20For%20Residue%20Plant%20Under%20Different%20O.pdf
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spelling my-utp-utpedia.88172017-01-25T09:43:58Z http://utpedia.utp.edu.my/8817/ Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity Abd Rashid @ Abd Rasip, Mohd Hanafi TJ Mechanical engineering and machinery The increase in demand of residue due to new production of Group III Lube Base Oil Product in Melaka Refmery required the residue plant to increase the feeding capacity of residue to the required unit. For the plant to achieve the targeted flow rate of the residue, the residue plant has upgraded the existing pumping capacity and cooling capacity by installing one unit of centrifugal pump PI I 12C and one unit of air fin cooler Eli29A to support the existing cooling system for the tempered water. The analyses are focusing on the mathematical modelling of the pump and heat exchanger to determine the right specification for the new equipments that are required for the new operating design. The hydraulic work covered the pipelines system from crude column CliO! to storage tank T72211 in order to determine the total head losses along the pipelines and through the equipments connected along the loop. The head of pump and pump-system operating curve at different operating capacity Q has been plotted to determine the operating point for the pump. For thermal capacity analysis of heat exchanger, ratio (old design/new design) for coolant flow has been determined. The analysis for air fin cooler Ell29 and Ell29A involves some calculations on the internal tube side and also finned tube side. Universiti Teknologi Petronas 2009-11 Final Year Project NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/8817/1/2009%20Bachelor%20-%20Design%20Calculation%20Of%20The%20Upgraded%20Equipments%20For%20Residue%20Plant%20Under%20Different%20O.pdf Abd Rashid @ Abd Rasip, Mohd Hanafi (2009) Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity. Universiti Teknologi Petronas. (Unpublished)
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Electronic and Digitized Intellectual Asset
url_provider http://utpedia.utp.edu.my/
language English
topic TJ Mechanical engineering and machinery
spellingShingle TJ Mechanical engineering and machinery
Abd Rashid @ Abd Rasip, Mohd Hanafi
Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
description The increase in demand of residue due to new production of Group III Lube Base Oil Product in Melaka Refmery required the residue plant to increase the feeding capacity of residue to the required unit. For the plant to achieve the targeted flow rate of the residue, the residue plant has upgraded the existing pumping capacity and cooling capacity by installing one unit of centrifugal pump PI I 12C and one unit of air fin cooler Eli29A to support the existing cooling system for the tempered water. The analyses are focusing on the mathematical modelling of the pump and heat exchanger to determine the right specification for the new equipments that are required for the new operating design. The hydraulic work covered the pipelines system from crude column CliO! to storage tank T72211 in order to determine the total head losses along the pipelines and through the equipments connected along the loop. The head of pump and pump-system operating curve at different operating capacity Q has been plotted to determine the operating point for the pump. For thermal capacity analysis of heat exchanger, ratio (old design/new design) for coolant flow has been determined. The analysis for air fin cooler Ell29 and Ell29A involves some calculations on the internal tube side and also finned tube side.
format Final Year Project
author Abd Rashid @ Abd Rasip, Mohd Hanafi
author_facet Abd Rashid @ Abd Rasip, Mohd Hanafi
author_sort Abd Rashid @ Abd Rasip, Mohd Hanafi
title Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
title_short Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
title_full Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
title_fullStr Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
title_full_unstemmed Design Calculation ofthe Upgraded Equipments for Residue Plant Under Different Operating Capacity
title_sort design calculation ofthe upgraded equipments for residue plant under different operating capacity
publisher Universiti Teknologi Petronas
publishDate 2009
url http://utpedia.utp.edu.my/8817/1/2009%20Bachelor%20-%20Design%20Calculation%20Of%20The%20Upgraded%20Equipments%20For%20Residue%20Plant%20Under%20Different%20O.pdf
http://utpedia.utp.edu.my/8817/
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score 13.160551