Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production

Fats, oil and grease (FOG) can be recovered efficiently from grease interceptors for biodiesel production. FOG is susceptible to hydrolysis because of its inherent high moisture content and the presence of lipases associated with food residuals in the grease interceptors. This study reveals that the...

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Main Authors: Montefrio, Marvin Joseph F., Tai, Xinwen, Obbard, Jeffrey P.
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Published: Animo Repository 2010
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Online Access:https://animorepository.dlsu.edu.ph/faculty_research/8324
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Institution: De La Salle University
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spelling oai:animorepository.dlsu.edu.ph:faculty_research-88692023-02-08T05:34:05Z Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production Montefrio, Marvin Joseph F. Tai, Xinwen Obbard, Jeffrey P. Fats, oil and grease (FOG) can be recovered efficiently from grease interceptors for biodiesel production. FOG is susceptible to hydrolysis because of its inherent high moisture content and the presence of lipases associated with food residuals in the grease interceptors. This study reveals that the FFA content of FOG derived from grease interceptors did not exceed 8% (w/w) due to constant influx of fresh FOG from wastewater. However, if the FOG is allowed to hydrolyze without dilution, the FFA content can reach 15% (w/w) in more than 20 days. Experiments were conducted to optimize reaction parameters for the esterification of FOG prior to the conventional alkali-catalyzed biodiesel production process. Sulphuric acid (H2SO4) was a more efficient catalyst than Fe2(SO4)3 in reducing the acid value to ⩽1 mg KOH/g under identical reaction conditions. At reaction temperatures of ⩽50 °C, only H2SO4 was capable of reaching the recommended acid value within 24 h. The optimum methanol to FFA ratio for an H2SO4-catalyzed reaction was 20:1, whereas for Fe2(SO4)3 it was above 26:1. Esterification occurred under static, non-mixed conditions, although conversion rates were low. The rate of conversion increased with mixing speed, with a 200 rpm orbital shaking speed as optimum. 2010-01-01T08:00:00Z text https://animorepository.dlsu.edu.ph/faculty_research/8324 Faculty Research Work Animo Repository Petroleum waste—Recycling Oils and fats—Recycling Waste products as fuel Biodiesel fuels Esterification Petroleum Engineering
institution De La Salle University
building De La Salle University Library
continent Asia
country Philippines
Philippines
content_provider De La Salle University Library
collection DLSU Institutional Repository
topic Petroleum waste—Recycling
Oils and fats—Recycling
Waste products as fuel
Biodiesel fuels
Esterification
Petroleum Engineering
spellingShingle Petroleum waste—Recycling
Oils and fats—Recycling
Waste products as fuel
Biodiesel fuels
Esterification
Petroleum Engineering
Montefrio, Marvin Joseph F.
Tai, Xinwen
Obbard, Jeffrey P.
Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
description Fats, oil and grease (FOG) can be recovered efficiently from grease interceptors for biodiesel production. FOG is susceptible to hydrolysis because of its inherent high moisture content and the presence of lipases associated with food residuals in the grease interceptors. This study reveals that the FFA content of FOG derived from grease interceptors did not exceed 8% (w/w) due to constant influx of fresh FOG from wastewater. However, if the FOG is allowed to hydrolyze without dilution, the FFA content can reach 15% (w/w) in more than 20 days. Experiments were conducted to optimize reaction parameters for the esterification of FOG prior to the conventional alkali-catalyzed biodiesel production process. Sulphuric acid (H2SO4) was a more efficient catalyst than Fe2(SO4)3 in reducing the acid value to ⩽1 mg KOH/g under identical reaction conditions. At reaction temperatures of ⩽50 °C, only H2SO4 was capable of reaching the recommended acid value within 24 h. The optimum methanol to FFA ratio for an H2SO4-catalyzed reaction was 20:1, whereas for Fe2(SO4)3 it was above 26:1. Esterification occurred under static, non-mixed conditions, although conversion rates were low. The rate of conversion increased with mixing speed, with a 200 rpm orbital shaking speed as optimum.
format text
author Montefrio, Marvin Joseph F.
Tai, Xinwen
Obbard, Jeffrey P.
author_facet Montefrio, Marvin Joseph F.
Tai, Xinwen
Obbard, Jeffrey P.
author_sort Montefrio, Marvin Joseph F.
title Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
title_short Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
title_full Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
title_fullStr Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
title_full_unstemmed Recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
title_sort recovery and pre-treatment of fats, oil and grease from grease interceptors for biodiesel production
publisher Animo Repository
publishDate 2010
url https://animorepository.dlsu.edu.ph/faculty_research/8324
_version_ 1767196844285231104