Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis

Sludge palm oil (SPO) is waste generated in the palm oil industry. The discharge of SPO together with palm oil mill effluent has created a major problem due to its difficulty in the treatment process. The feasibility of SPO as a raw material for biofuel production was investigated via catalytic pyro...

Full description

Saved in:
Bibliographic Details
Main Authors: Ali S.H., Hafriz R.S.R.M., Shamsuddin A.H., Salmiaton A.
Other Authors: 57208816736
Format: Article
Published: Tamkang University 2024
Subjects:
Tags: Add Tag
No Tags, Be the first to tag this record!
id my.uniten.dspace-34730
record_format dspace
spelling my.uniten.dspace-347302024-10-14T11:22:08Z Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis Ali S.H. Hafriz R.S.R.M. Shamsuddin A.H. Salmiaton A. 57208816736 57204588040 35779071900 57193906995 Biofuel Malaysian Dolomite Catalyst Pyro-oil Sludge Palm Oil (SPO) Biofuels Catalysts Effluent treatment Effluents Oil shale Palm oil Pyrolysis Temperature Catalytic pyrolysis Liquid biofuels Malaysian dolomite catalyst Malaysians Oil conversion Operating temperature Pyro-oil Reaction temperature Sludge palm oil ]+ catalyst Dolomite Sludge palm oil (SPO) is waste generated in the palm oil industry. The discharge of SPO together with palm oil mill effluent has created a major problem due to its difficulty in the treatment process. The feasibility of SPO as a raw material for biofuel production was investigated via catalytic pyrolysis process using heterogeneous Malaysian dolomite catalyst. The effects of operating temperatures and reaction times in the catalytic pyrolysis using Malaysian dolomite catalyst were assessed. The condition for the reaction parameters investigated is as followed: operating temperatures of 350 ?C, 400 ?C, and 450 ?C, reaction times of 30, 45 and 60 minutes, under a constant of 100 ml/min of nitrogen flow rate and 5 wt.% catalyst loading. At a reaction temperature of 350 ?C the SPO conversion was very low even at longer reaction times. The longer reaction times gave higher SPO conversion at an operating temperature of 400 �C with the range of conversion between 45.7 to 58.3 wt.%. At temperature 450 ?C the conversion achieved an average of 93.1 � 1.0 wt.%. Only a slight change at longer times was observed at this temperature. At a temperature of 400 ?C and 45 min of reaction times, the pyro-oil obtained from the process contained the highest hydrocarbon content (83.90 %) and lowest oxygenated compound content (16.10 %), even though the conversion was lower than at 450 ?C. The product selectivity was highest in the diesel range at the reaction temperature of 400 ?C. Thus, with further improvement in catalyst modification together with optimized operating conditions, SPO can be used as a feedstock in the catalytic pyrolysis for producing biofuel in the range carbon number of diesel, gasoline and kerosene. � The Author(�s). Final 2024-10-14T03:22:08Z 2024-10-14T03:22:08Z 2023 Article 10.6180/jase.202304_26(4).0009 2-s2.0-85139434063 https://www.scopus.com/inward/record.uri?eid=2-s2.0-85139434063&doi=10.6180%2fjase.202304_26%284%29.0009&partnerID=40&md5=5a478e0fa9ad0c70a0f4b51eedac1a74 https://irepository.uniten.edu.my/handle/123456789/34730 26 4 529 538 Tamkang University Scopus
institution Universiti Tenaga Nasional
building UNITEN Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Tenaga Nasional
content_source UNITEN Institutional Repository
url_provider http://dspace.uniten.edu.my/
topic Biofuel
Malaysian Dolomite Catalyst
Pyro-oil
Sludge Palm Oil (SPO)
Biofuels
Catalysts
Effluent treatment
Effluents
Oil shale
Palm oil
Pyrolysis
Temperature
Catalytic pyrolysis
Liquid biofuels
Malaysian dolomite catalyst
Malaysians
Oil conversion
Operating temperature
Pyro-oil
Reaction temperature
Sludge palm oil
]+ catalyst
Dolomite
spellingShingle Biofuel
Malaysian Dolomite Catalyst
Pyro-oil
Sludge Palm Oil (SPO)
Biofuels
Catalysts
Effluent treatment
Effluents
Oil shale
Palm oil
Pyrolysis
Temperature
Catalytic pyrolysis
Liquid biofuels
Malaysian dolomite catalyst
Malaysians
Oil conversion
Operating temperature
Pyro-oil
Reaction temperature
Sludge palm oil
]+ catalyst
Dolomite
Ali S.H.
Hafriz R.S.R.M.
Shamsuddin A.H.
Salmiaton A.
Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
description Sludge palm oil (SPO) is waste generated in the palm oil industry. The discharge of SPO together with palm oil mill effluent has created a major problem due to its difficulty in the treatment process. The feasibility of SPO as a raw material for biofuel production was investigated via catalytic pyrolysis process using heterogeneous Malaysian dolomite catalyst. The effects of operating temperatures and reaction times in the catalytic pyrolysis using Malaysian dolomite catalyst were assessed. The condition for the reaction parameters investigated is as followed: operating temperatures of 350 ?C, 400 ?C, and 450 ?C, reaction times of 30, 45 and 60 minutes, under a constant of 100 ml/min of nitrogen flow rate and 5 wt.% catalyst loading. At a reaction temperature of 350 ?C the SPO conversion was very low even at longer reaction times. The longer reaction times gave higher SPO conversion at an operating temperature of 400 �C with the range of conversion between 45.7 to 58.3 wt.%. At temperature 450 ?C the conversion achieved an average of 93.1 � 1.0 wt.%. Only a slight change at longer times was observed at this temperature. At a temperature of 400 ?C and 45 min of reaction times, the pyro-oil obtained from the process contained the highest hydrocarbon content (83.90 %) and lowest oxygenated compound content (16.10 %), even though the conversion was lower than at 450 ?C. The product selectivity was highest in the diesel range at the reaction temperature of 400 ?C. Thus, with further improvement in catalyst modification together with optimized operating conditions, SPO can be used as a feedstock in the catalytic pyrolysis for producing biofuel in the range carbon number of diesel, gasoline and kerosene. � The Author(�s).
author2 57208816736
author_facet 57208816736
Ali S.H.
Hafriz R.S.R.M.
Shamsuddin A.H.
Salmiaton A.
format Article
author Ali S.H.
Hafriz R.S.R.M.
Shamsuddin A.H.
Salmiaton A.
author_sort Ali S.H.
title Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
title_short Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
title_full Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
title_fullStr Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
title_full_unstemmed Production Of Liquid Biofuel From Sludge Palm Oil (SPO) Using Heterogeneous Catalytic Pyrolysis
title_sort production of liquid biofuel from sludge palm oil (spo) using heterogeneous catalytic pyrolysis
publisher Tamkang University
publishDate 2024
_version_ 1814061134483816448
score 13.222552