Continuous transesterification for tubular reactor

Biodiesel production has been use for transportation to replace the petro diesel in Europe country since end of twenty century due to the gasoline and petroleum limitation. Biodiesel are produce from the waste cooking oil through the process of transesterification reaction and assisted by microwave....

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Main Author:	Lau, Kun Lu
Format:	Undergraduates Project Papers
Language:	English English English
Published:	2015
Subjects:	TP Chemical technology
Online Access:	http://umpir.ump.edu.my/id/eprint/12455/ http://umpir.ump.edu.my/id/eprint/12455/ http://umpir.ump.edu.my/id/eprint/12455/1/FKKSA%20-%20LAU%20KUN%20LU.PDF http://umpir.ump.edu.my/id/eprint/12455/2/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%201.PDF http://umpir.ump.edu.my/id/eprint/12455/8/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%203.PDF

id	ump-12455
recordtype	eprints
spelling	ump-124552016-03-28T02:56:52Z http://umpir.ump.edu.my/id/eprint/12455/ Continuous transesterification for tubular reactor Lau, Kun Lu TP Chemical technology Biodiesel production has been use for transportation to replace the petro diesel in Europe country since end of twenty century due to the gasoline and petroleum limitation. Biodiesel are produce from the waste cooking oil through the process of transesterification reaction and assisted by microwave. Transesterification is the most comment process for produce the biodiesel whereby microwave assisted to change the triglyceride(vegetable oil) to biofuel by adding the activated cement clinker (catalyst) and methanol in the condition 60°C with 6 minutes reaction time.The heterogeneous base catalystactivated cement clinker is chosen to use with several advantage such as reusable, environmental friendly and low costs. The microwave assisted in transesterification can reduce the reaction time and also increase the product yield. The catalyst made from cement clinker is activated by potassium hydroxide solution which characterized by several type of test such as Thermogravimetric Analysis, Brunauer-Emmett-Teller test, X-ray Diffraction test and Gas Pyrometer test. The parameter was determiningfor produce the biodiesel by using the activated cement clinker catalyst with the weight ratio(2, 3, 4, 5 and 6% wt.). The result was analysed by using gas chromatography (GCMS) showed that 5% wt. of activated cement clinker use are the optimum amount which having 92.85% conversion and 85.26% yield. For the conventional method by using activated cement clinker and pure calcium oxide obtained 92.63% and 85.37% yield respectively. Based on the yield result, transesterification assisted by microwave method is the best method for the reaction compare with conventional method. 2015-01 Undergraduates Project Papers NonPeerReviewed application/pdf en http://umpir.ump.edu.my/id/eprint/12455/1/FKKSA%20-%20LAU%20KUN%20LU.PDF application/pdf en http://umpir.ump.edu.my/id/eprint/12455/2/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%201.PDF application/pdf en http://umpir.ump.edu.my/id/eprint/12455/8/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%203.PDF Lau, Kun Lu (2015) Continuous transesterification for tubular reactor. Faculty of Chemical & Natural Resources Engineering, Universiti Malaysia Pahang. http://iportal.ump.edu.my/lib/item?id=chamo:91206&theme=UMP2
repository_type	Digital Repository
institution_category	Local University
institution	Universiti Malaysia Pahang
building	UMP Institutional Repository
collection	Online Access
language	English English English
topic	TP Chemical technology
spellingShingle	TP Chemical technology Lau, Kun Lu Continuous transesterification for tubular reactor
description	Biodiesel production has been use for transportation to replace the petro diesel in Europe country since end of twenty century due to the gasoline and petroleum limitation. Biodiesel are produce from the waste cooking oil through the process of transesterification reaction and assisted by microwave. Transesterification is the most comment process for produce the biodiesel whereby microwave assisted to change the triglyceride(vegetable oil) to biofuel by adding the activated cement clinker (catalyst) and methanol in the condition 60°C with 6 minutes reaction time.The heterogeneous base catalystactivated cement clinker is chosen to use with several advantage such as reusable, environmental friendly and low costs. The microwave assisted in transesterification can reduce the reaction time and also increase the product yield. The catalyst made from cement clinker is activated by potassium hydroxide solution which characterized by several type of test such as Thermogravimetric Analysis, Brunauer-Emmett-Teller test, X-ray Diffraction test and Gas Pyrometer test. The parameter was determiningfor produce the biodiesel by using the activated cement clinker catalyst with the weight ratio(2, 3, 4, 5 and 6% wt.). The result was analysed by using gas chromatography (GCMS) showed that 5% wt. of activated cement clinker use are the optimum amount which having 92.85% conversion and 85.26% yield. For the conventional method by using activated cement clinker and pure calcium oxide obtained 92.63% and 85.37% yield respectively. Based on the yield result, transesterification assisted by microwave method is the best method for the reaction compare with conventional method.
format	Undergraduates Project Papers
author	Lau, Kun Lu
author_facet	Lau, Kun Lu
author_sort	Lau, Kun Lu
title	Continuous transesterification for tubular reactor
title_short	Continuous transesterification for tubular reactor
title_full	Continuous transesterification for tubular reactor
title_fullStr	Continuous transesterification for tubular reactor
title_full_unstemmed	Continuous transesterification for tubular reactor
title_sort	continuous transesterification for tubular reactor
publishDate	2015
url	http://umpir.ump.edu.my/id/eprint/12455/ http://umpir.ump.edu.my/id/eprint/12455/ http://umpir.ump.edu.my/id/eprint/12455/1/FKKSA%20-%20LAU%20KUN%20LU.PDF http://umpir.ump.edu.my/id/eprint/12455/2/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%201.PDF http://umpir.ump.edu.my/id/eprint/12455/8/FKKSA%20-%20LAU%20KUN%20LU%20-%20CHAP%203.PDF
first_indexed	2023-09-18T22:14:07Z
last_indexed	2023-09-18T22:14:07Z
_version_	1777415223195467776

Continuous transesterification for tubular reactor

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