Extraction of caustic potash from spent tea for biodiesel production
Biodiesel is an alternative to non-renewable fossil fuels due to its low gas emission and economical value. This study aims to extract caustic potash (KOH) from spent tea and to optimize the transesterfication process based on parameters such as amount of catalyst, reaction temperature and methanol...
Main Authors: | , , |
---|---|
Format: | Conference or Workshop Item |
Language: | English English English English |
Published: |
Institute of Physics Publishing
2018
|
Subjects: | |
Online Access: | http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/19/57744.pdf http://irep.iium.edu.my/57744/25/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_Conference%20article.pdf http://irep.iium.edu.my/57744/26/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_scopus.pdf http://irep.iium.edu.my/57744/37/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea%20for%20biodiesel%20Production_WoS.pdf |
id |
iium-57744 |
---|---|
recordtype |
eprints |
spelling |
iium-577442018-10-18T01:52:05Z http://irep.iium.edu.my/57744/ Extraction of caustic potash from spent tea for biodiesel production Sulaiman, Sarina Che Fisol, Ahmad Faiz Mohamed Sharikh, Atikah TP315 Fuel Biodiesel is an alternative to non-renewable fossil fuels due to its low gas emission and economical value. This study aims to extract caustic potash (KOH) from spent tea and to optimize the transesterfication process based on parameters such as amount of catalyst, reaction temperature and methanol to oil ratio. The spent tea was first dried at 60°C prior to calcination at 600°C for two hours. Caustic Potash were extracted from the calcined spent tea. The transesterification process was done based on Design of Experiments (DOE) to study the effects of amount of catalyst ranging from 0.5 wt % to 2.5 wt %, reaction temperature from 55°C to 65°C and methanol to oil ratio from 6:1 to 12:1 at a constant agitation rate of 300 rpm for three hours. The calcined spent tea produced was recorded the highest at 54.3 wt % and the extracted catalyst was 2.4 wt %. The optimized biodiesel yield recorded was 56.95% at the optimal conditions of 2.5 wt % amount of catalyst, 65°C reaction temperature and 9:1 methanol to oil ratio. Institute of Physics Publishing 2018-01 Conference or Workshop Item NonPeerReviewed application/pdf en http://irep.iium.edu.my/57744/19/57744.pdf application/pdf en http://irep.iium.edu.my/57744/25/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_Conference%20article.pdf application/pdf en http://irep.iium.edu.my/57744/26/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_scopus.pdf application/pdf en http://irep.iium.edu.my/57744/37/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea%20for%20biodiesel%20Production_WoS.pdf Sulaiman, Sarina and Che Fisol, Ahmad Faiz and Mohamed Sharikh, Atikah (2018) Extraction of caustic potash from spent tea for biodiesel production. In: International Conference on Advances in Manufacturing and Materials Engineering 2017, ICAMME 2017, 8th-9th August 2017, Kuala Lumpur, Malaysia. http://iopscience.iop.org/article/10.1088/1757-899X/290/1/012062/meta 10.1088/1757-899X/290/1/012062 |
repository_type |
Digital Repository |
institution_category |
Local University |
institution |
International Islamic University Malaysia |
building |
IIUM Repository |
collection |
Online Access |
language |
English English English English |
topic |
TP315 Fuel |
spellingShingle |
TP315 Fuel Sulaiman, Sarina Che Fisol, Ahmad Faiz Mohamed Sharikh, Atikah Extraction of caustic potash from spent tea for biodiesel production |
description |
Biodiesel is an alternative to non-renewable fossil fuels due to its low gas emission and economical value. This study aims to extract caustic potash (KOH) from spent tea and to optimize the transesterfication process based on parameters such as amount of catalyst, reaction temperature and methanol to oil ratio. The spent tea was first dried at 60°C prior to calcination at 600°C for two hours. Caustic Potash were extracted from the calcined spent tea. The transesterification process was done based on Design of Experiments (DOE) to study the effects of amount of catalyst ranging from 0.5 wt % to 2.5 wt %, reaction temperature from 55°C to 65°C and methanol to oil ratio from 6:1 to 12:1 at a constant agitation rate of 300 rpm for three hours. The calcined spent tea produced was recorded the highest at 54.3 wt % and the extracted catalyst was 2.4 wt %. The optimized biodiesel yield recorded was 56.95% at the optimal conditions of 2.5 wt % amount of catalyst, 65°C reaction temperature and 9:1 methanol to oil ratio. |
format |
Conference or Workshop Item |
author |
Sulaiman, Sarina Che Fisol, Ahmad Faiz Mohamed Sharikh, Atikah |
author_facet |
Sulaiman, Sarina Che Fisol, Ahmad Faiz Mohamed Sharikh, Atikah |
author_sort |
Sulaiman, Sarina |
title |
Extraction of caustic potash from spent tea for biodiesel production |
title_short |
Extraction of caustic potash from spent tea for biodiesel production |
title_full |
Extraction of caustic potash from spent tea for biodiesel production |
title_fullStr |
Extraction of caustic potash from spent tea for biodiesel production |
title_full_unstemmed |
Extraction of caustic potash from spent tea for biodiesel production |
title_sort |
extraction of caustic potash from spent tea for biodiesel production |
publisher |
Institute of Physics Publishing |
publishDate |
2018 |
url |
http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/ http://irep.iium.edu.my/57744/19/57744.pdf http://irep.iium.edu.my/57744/25/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_Conference%20article.pdf http://irep.iium.edu.my/57744/26/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea_scopus.pdf http://irep.iium.edu.my/57744/37/57744_Extraction%20of%20caustic%20potash%20from%20spent%20tea%20for%20biodiesel%20Production_WoS.pdf |
first_indexed |
2023-09-18T21:21:39Z |
last_indexed |
2023-09-18T21:21:39Z |
_version_ |
1777411921414193152 |