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Found results for
patents
1.
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Transesterification of vegetable oils
Application Number |
12865072 |
Grant Number |
09303233 |
Status |
In Force |
Filing Date |
2009-01-29 |
First Publication Date |
2011-01-06 |
Grant Date |
2016-04-05 |
Owner |
QS Biodiesel Limited (United Kingdom)
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Inventor |
Kovács, András
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Abstract
A method for producing diesel grade fuel of plant origin by transesterifying a refined vegetable oil with a charge of a C1-C4 alcohol in the presence of a catalyst and at least 0.2 parts by volume, related to unit volume of refined vegetable oil, of an aliphatic hydrocarbon solvent with a boiling point of −42° C. to 200° C., comprises mixing the oil, alcohol, catalyst and solvent in a single reaction vessel under homogeneous conditions which promote transesterification to 95-98% completion and which suppress reverse glycerolysis, without stopping transesterification to remove by-product polar glycerol, and without subjecting the oil/fuel mixture to a further transesterification step with a fresh charge of alcohol and catalyst.
IPC Classes ?
- C10L 1/18 - Organic compounds containing oxygen
- C11C 3/00 - Fats, oils or fatty acids obtained by chemical modification of fats, oils or fatty acids, e.g. by ozonolysis
- C10L 1/02 - Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C11C 3/06 - Fats, oils or fatty acids obtained by chemical modification of fats, oils or fatty acids, e.g. by ozonolysis by esterification of fats or fatty oils with glycerol
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2.
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TRANSESTERIFICATION OF VEGETABLE OILS
Application Number |
GB2009000246 |
Publication Number |
2009/095668 |
Status |
In Force |
Filing Date |
2009-01-29 |
Publication Date |
2009-08-06 |
Owner |
QS BIODIESEL LIMITED (United Kingdom)
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Inventor |
Kovács, András
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Abstract
A method for producing diesel grade fuel of plant origin by transesterifying a refined vegetable oil with a charge of a C1-C4 alcohol in the presence of a catalyst and at least 0.2 parts by volume, related to unit volume of refined vegetable oil, of an aliphatic hydrocarbon solvent with a boiling point of -42°C to 200°C, comprises mixing the oil, alcohol, catalyst and solvent in a single reaction vessel under homogeneous conditions which promote transesterif ication to 95-98% completion and which suppress reverse glycerolysis, without stopping transesterif ication to remove by- product polar glycerol, and without subjecting the oil/fuel mixture to a further transesterif ication step with a fresh charge of alcohol and catalyst.
IPC Classes ?
- C11C 3/00 - Fats, oils or fatty acids obtained by chemical modification of fats, oils or fatty acids, e.g. by ozonolysis
- C10L 1/02 - Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C11C 3/06 - Fats, oils or fatty acids obtained by chemical modification of fats, oils or fatty acids, e.g. by ozonolysis by esterification of fats or fatty oils with glycerol
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