Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina

Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina

Hydrocracking process of Butonian asphalt derived asphaltene using Mo-Ni/γ-alumina catalyst has been investigated. The processes were carried out in 1L stainless steel autoclave reactor. The reaction temperatures were 250, 300, 350 and 400C, initial pressure was 10 atm and catalyst/feed ratio was 1...

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Main Authors: Rahmad Nuryanto, Wega Trisunaryanti, M. Utoro Yahya
Format: Article
Language:English
Published: Chemistry Department, Faculty of Sciences and Mathematics, Diponegoro University 2009-04-01
Series:Jurnal Kimia Sains dan Aplikasi
Subjects:
hidrorengkah
aspal
katalis mo-ni/γ-alumina
Online Access:https://ejournal.undip.ac.id/index.php/ksa/article/view/3552
id doaj-6e952e2a014b45e9b3d39864f26a700a
record_format Article
spelling doaj-6e952e2a014b45e9b3d39864f26a700a2020-11-25T03:25:56ZengChemistry Department, Faculty of Sciences and Mathematics, Diponegoro UniversityJurnal Kimia Sains dan Aplikasi1410-89172597-99142009-04-01121141610.14710/jksa.12.1.14-163188Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-AluminaRahmad Nuryanto0Wega Trisunaryanti1M. Utoro Yahya2Chemistry Department, Faculty of Sciences and Mathematics, Diponegoro University Jl. Prof. Soedarto, SH., Tembalang, SemarangChemistry Department, Faculty of Mathematics and Natural Sciences, Gadjah Mada UniversityChemistry Department, Faculty of Mathematics and Natural Sciences, Gadjah Mada UniversityHydrocracking process of Butonian asphalt derived asphaltene using Mo-Ni/γ-alumina catalyst has been investigated. The processes were carried out in 1L stainless steel autoclave reactor. The reaction temperatures were 250, 300, 350 and 400C, initial pressure was 10 atm and catalyst/feed ratio was 1/2. The asphaltene was a pentane insoluble-benzene soluble (PI-BS) fraction of Butonian asphalt.The results of hydrocracking processes showed the conversion by means of 100% - coke (wt %) was followed equation konversi % (w/w) = 0,306 t (C) - 41,29Key words: hydrocracking, asphaltene, Mo-Ni/γ-alumina catalysthttps://ejournal.undip.ac.id/index.php/ksa/article/view/3552hidrorengkahaspalkatalis mo-ni/γ-alumina
collection DOAJ
language English
format Article
sources DOAJ
author Rahmad Nuryanto
Wega Trisunaryanti
M. Utoro Yahya
spellingShingle Rahmad Nuryanto
Wega Trisunaryanti
M. Utoro Yahya
Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
Jurnal Kimia Sains dan Aplikasi
hidrorengkah
aspal
katalis mo-ni/γ-alumina
author_facet Rahmad Nuryanto
Wega Trisunaryanti
M. Utoro Yahya
author_sort Rahmad Nuryanto
title Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
title_short Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
title_full Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
title_fullStr Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
title_full_unstemmed Pengaruh Temperatur terhadap Jumlah Produk Hidrorengkah Fraksi Aspalten dari Aspal Buton dengan Katalis Mo-Ni/γ-Alumina
title_sort pengaruh temperatur terhadap jumlah produk hidrorengkah fraksi aspalten dari aspal buton dengan katalis mo-ni/γ-alumina
publisher Chemistry Department, Faculty of Sciences and Mathematics, Diponegoro University
series Jurnal Kimia Sains dan Aplikasi
issn 1410-8917
2597-9914
publishDate 2009-04-01
description Hydrocracking process of Butonian asphalt derived asphaltene using Mo-Ni/γ-alumina catalyst has been investigated. The processes were carried out in 1L stainless steel autoclave reactor. The reaction temperatures were 250, 300, 350 and 400C, initial pressure was 10 atm and catalyst/feed ratio was 1/2. The asphaltene was a pentane insoluble-benzene soluble (PI-BS) fraction of Butonian asphalt.The results of hydrocracking processes showed the conversion by means of 100% - coke (wt %) was followed equation konversi % (w/w) = 0,306 t (C) - 41,29Key words: hydrocracking, asphaltene, Mo-Ni/γ-alumina catalyst
topic hidrorengkah
aspal
katalis mo-ni/γ-alumina
url https://ejournal.undip.ac.id/index.php/ksa/article/view/3552
work_keys_str_mv AT rahmadnuryanto pengaruhtemperaturterhadapjumlahprodukhidrorengkahfraksiaspaltendariaspalbutondengankatalismonigalumina
AT wegatrisunaryanti pengaruhtemperaturterhadapjumlahprodukhidrorengkahfraksiaspaltendariaspalbutondengankatalismonigalumina
AT mutoroyahya pengaruhtemperaturterhadapjumlahprodukhidrorengkahfraksiaspaltendariaspalbutondengankatalismonigalumina
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