Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts

Catalytic conversion of palm oil to gasoline was performed over H-ZSM-5 zeolite catalyst. Palm oil was converted in a down flow fixed bed reactor at atmospheric pressure and weight hourly space velocity (WHSV) of 2.5 h-1. Temperature was varied in the range of 450-525°C and hydrogen flow rate for a...

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Autores principales: Siregar, Tirena Bahnur, Saidina Amin, Nor Aishah, Abdul Karim, Siti Kartina
Formato: Conference or Workshop Item
Lenguaje:English
Publicado: 2005
Materias:
Acceso en línea:http://eprints.utm.my/5275/1/TirenaBahnurSiregar2005_CatalyticConversionOfPalmOilToGasoline.pdf
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author Siregar, Tirena Bahnur
Saidina Amin, Nor Aishah
Abdul Karim, Siti Kartina
author_facet Siregar, Tirena Bahnur
Saidina Amin, Nor Aishah
Abdul Karim, Siti Kartina
author_sort Siregar, Tirena Bahnur
collection ePrints
description Catalytic conversion of palm oil to gasoline was performed over H-ZSM-5 zeolite catalyst. Palm oil was converted in a down flow fixed bed reactor at atmospheric pressure and weight hourly space velocity (WHSV) of 2.5 h-1. Temperature was varied in the range of 450-525°C and hydrogen flow rate for activation of 1-2 L/h. Increasing reaction temperature to 500°C increased the conversion of palm oil. OLP yield and gasoline selectivity increased with temperature until 500°C before decreasing slightly. Hydrotreatment of catalysts increased OLP and gasoline formation while coke and gas decreased. However, increasing the hydrotreating flow rate more than 1L/h gave little effect towards palm oil cracking activity.
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spelling utm.eprints-52752017-08-30T04:57:18Z http://eprints.utm.my/5275/ Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts Siregar, Tirena Bahnur Saidina Amin, Nor Aishah Abdul Karim, Siti Kartina T Technology (General) Catalytic conversion of palm oil to gasoline was performed over H-ZSM-5 zeolite catalyst. Palm oil was converted in a down flow fixed bed reactor at atmospheric pressure and weight hourly space velocity (WHSV) of 2.5 h-1. Temperature was varied in the range of 450-525°C and hydrogen flow rate for activation of 1-2 L/h. Increasing reaction temperature to 500°C increased the conversion of palm oil. OLP yield and gasoline selectivity increased with temperature until 500°C before decreasing slightly. Hydrotreatment of catalysts increased OLP and gasoline formation while coke and gas decreased. However, increasing the hydrotreating flow rate more than 1L/h gave little effect towards palm oil cracking activity. 2005 Conference or Workshop Item PeerReviewed application/pdf en http://eprints.utm.my/5275/1/TirenaBahnurSiregar2005_CatalyticConversionOfPalmOilToGasoline.pdf Siregar, Tirena Bahnur and Saidina Amin, Nor Aishah and Abdul Karim, Siti Kartina (2005) Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts. In: Annual Fundamental Science Seminar 2005, July 4-5, 2005, Ibnu Sina Institute for Fundamental Science Studies, UTM.
spellingShingle T Technology (General)
Siregar, Tirena Bahnur
Saidina Amin, Nor Aishah
Abdul Karim, Siti Kartina
Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title_full Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title_fullStr Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title_full_unstemmed Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title_short Catalytic conversion of palm oil to gasoline over H-ZSM-5: effect of temperature and hydrotreatment of catalysts
title_sort catalytic conversion of palm oil to gasoline over h zsm 5 effect of temperature and hydrotreatment of catalysts
topic T Technology (General)
url http://eprints.utm.my/5275/1/TirenaBahnurSiregar2005_CatalyticConversionOfPalmOilToGasoline.pdf
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