Improvements to the biodiesel process

Biodiesel (fatty acid methyl ester, FAME) is a renewable diesel fuel made from vegetable oil and methanol. The two main problems with the process are disposal of waste streams and product purity. This thesis studies biodiesel process improvements, especially glycerol conversion to hydrogen and impro...

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Main Author: Slinn, Matthew
Published: University of Birmingham 2008
Subjects:
630
Online Access:https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.556773
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spelling ndltd-bl.uk-oai-ethos.bl.uk-5567732019-04-03T06:27:12ZImprovements to the biodiesel processSlinn, Matthew2008Biodiesel (fatty acid methyl ester, FAME) is a renewable diesel fuel made from vegetable oil and methanol. The two main problems with the process are disposal of waste streams and product purity. This thesis studies biodiesel process improvements, especially glycerol conversion to hydrogen and improved mass transfer to increase ester yield. Experiments on steam reforming with glycerol and waste water over a platinum alumina catalyst were used to convert the combined waste product streams of a biodiesel plant. Mass spectroscopy with internal standard was chosen to measure reformer gas yield and conversion. The glycerol steam reforming was shown to depend on several reaction variables. Therefore a solid oxide fuel cell was used as a sensor to measure the effects. The results showed that good syngas yield, conversion and reformer life could be obtained using this process. The purity of the biodiesel product was examined using real-time optical microscopy and gas chromatography to fit the FAME standard EN14214. It was observed that droplet size had a major influence on reaction end point and that the reaction was mass-transfer limited. This observation was confirmed by developing a mass-transfer based reaction model using the data from the batch reactor which agreed with results from other researchers. The model predicted better conversion with more mixing intensity. Finally, on the basis of these results, a high mixing intensity continuous reactor was developed which achieved the 96.5% standard with high flow rate and short reactor length. The conclusion was that significant cost effective improvements could be made to the conventional FAME process.630TP Chemical technologyUniversity of Birminghamhttps://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.556773http://etheses.bham.ac.uk//id/eprint/675/Electronic Thesis or Dissertation
collection NDLTD
sources NDLTD
topic 630
TP Chemical technology
spellingShingle 630
TP Chemical technology
Slinn, Matthew
Improvements to the biodiesel process
description Biodiesel (fatty acid methyl ester, FAME) is a renewable diesel fuel made from vegetable oil and methanol. The two main problems with the process are disposal of waste streams and product purity. This thesis studies biodiesel process improvements, especially glycerol conversion to hydrogen and improved mass transfer to increase ester yield. Experiments on steam reforming with glycerol and waste water over a platinum alumina catalyst were used to convert the combined waste product streams of a biodiesel plant. Mass spectroscopy with internal standard was chosen to measure reformer gas yield and conversion. The glycerol steam reforming was shown to depend on several reaction variables. Therefore a solid oxide fuel cell was used as a sensor to measure the effects. The results showed that good syngas yield, conversion and reformer life could be obtained using this process. The purity of the biodiesel product was examined using real-time optical microscopy and gas chromatography to fit the FAME standard EN14214. It was observed that droplet size had a major influence on reaction end point and that the reaction was mass-transfer limited. This observation was confirmed by developing a mass-transfer based reaction model using the data from the batch reactor which agreed with results from other researchers. The model predicted better conversion with more mixing intensity. Finally, on the basis of these results, a high mixing intensity continuous reactor was developed which achieved the 96.5% standard with high flow rate and short reactor length. The conclusion was that significant cost effective improvements could be made to the conventional FAME process.
author Slinn, Matthew
author_facet Slinn, Matthew
author_sort Slinn, Matthew
title Improvements to the biodiesel process
title_short Improvements to the biodiesel process
title_full Improvements to the biodiesel process
title_fullStr Improvements to the biodiesel process
title_full_unstemmed Improvements to the biodiesel process
title_sort improvements to the biodiesel process
publisher University of Birmingham
publishDate 2008
url https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.556773
work_keys_str_mv AT slinnmatthew improvementstothebiodieselprocess
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