Molecular distillation and characterization of diacylglycerol-enriched palm olein

Lipase-catalyzed glycerolysis of palm olein was used to produce a mixture of acylglycerols with ∼34-wt% of DAG. The reaction conditions were 5-wt% of Lipozyme TLIM at 55°C and 8 h of reaction time. For commercial purposes, it is required to purify the product up to 80-wt% DAG and with free fatty aci...

Full description

Saved in:
Bibliographic Details
Main Authors: Yeoh, Chiou Moi, Phuah, Eng Tong, Tang, Teck Kim, Siew, Wai Lin, Abdullah, Luqman Chuah, Choong, Thomas Shean Yaw
Format: Article
Published: Wiley 2014
Online Access:http://psasir.upm.edu.my/id/eprint/34579/
http://onlinelibrary.wiley.com/doi/10.1002/ejlt.201300502/abstract
Tags: Add Tag
No Tags, Be the first to tag this record!
id my.upm.eprints.34579
record_format eprints
spelling my.upm.eprints.345792016-01-18T06:37:31Z http://psasir.upm.edu.my/id/eprint/34579/ Molecular distillation and characterization of diacylglycerol-enriched palm olein Yeoh, Chiou Moi Phuah, Eng Tong Tang, Teck Kim Siew, Wai Lin Abdullah, Luqman Chuah Choong, Thomas Shean Yaw Lipase-catalyzed glycerolysis of palm olein was used to produce a mixture of acylglycerols with ∼34-wt% of DAG. The reaction conditions were 5-wt% of Lipozyme TLIM at 55°C and 8 h of reaction time. For commercial purposes, it is required to purify the product up to 80-wt% DAG and with free fatty acids (FFA) content below 0.1-wt%. A single-step distillation process was not sufficient to meet this product requirement. Two distinct 2-step short path distillation approaches were then studied. First scheme involved the removal of TAG by initial distillation step at 250°C, followed by separation of the MAG and FFA from distillate obtained at 180°C during second distillation step at vacuum pressure of 0.1 Pa. Second scheme involved the removal of MAG and FFA in first step at 180°C prior to purification of DAG from residue at 250°C during second distillation step at vacuum achieved up to 0.1 Pa. The results suggested that the first scheme of 2-step distillation operation was able to achieve 89.9-wt% of DAG purity without exceeding the limit of 0.1-wt% of FFA. A final yield of 21.5-wt% and DAG recovery of 47.8% were obtained using the first scheme. A detailed DAG profile was identified and product characterizations such as fatty acid composition, slip melting point, and solid fat content profile were also investigated. It was observed that purified-DAG product showed lower iodine value and higher slip melting point than raw material palm olein. The final product had 1134 ± 10 ppm tocols content. Wiley 2014-12 Article PeerReviewed Yeoh, Chiou Moi and Phuah, Eng Tong and Tang, Teck Kim and Siew, Wai Lin and Abdullah, Luqman Chuah and Choong, Thomas Shean Yaw (2014) Molecular distillation and characterization of diacylglycerol-enriched palm olein. European Journal of Lipid Science and Technology , 116 (12). pp. 1654-1663. ISSN 1438-7697; ESSN: 1438-9312 http://onlinelibrary.wiley.com/doi/10.1002/ejlt.201300502/abstract 10.1002/ejlt.201300502
institution Universiti Putra Malaysia
building UPM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Putra Malaysia
content_source UPM Institutional Repository
url_provider http://psasir.upm.edu.my/
description Lipase-catalyzed glycerolysis of palm olein was used to produce a mixture of acylglycerols with ∼34-wt% of DAG. The reaction conditions were 5-wt% of Lipozyme TLIM at 55°C and 8 h of reaction time. For commercial purposes, it is required to purify the product up to 80-wt% DAG and with free fatty acids (FFA) content below 0.1-wt%. A single-step distillation process was not sufficient to meet this product requirement. Two distinct 2-step short path distillation approaches were then studied. First scheme involved the removal of TAG by initial distillation step at 250°C, followed by separation of the MAG and FFA from distillate obtained at 180°C during second distillation step at vacuum pressure of 0.1 Pa. Second scheme involved the removal of MAG and FFA in first step at 180°C prior to purification of DAG from residue at 250°C during second distillation step at vacuum achieved up to 0.1 Pa. The results suggested that the first scheme of 2-step distillation operation was able to achieve 89.9-wt% of DAG purity without exceeding the limit of 0.1-wt% of FFA. A final yield of 21.5-wt% and DAG recovery of 47.8% were obtained using the first scheme. A detailed DAG profile was identified and product characterizations such as fatty acid composition, slip melting point, and solid fat content profile were also investigated. It was observed that purified-DAG product showed lower iodine value and higher slip melting point than raw material palm olein. The final product had 1134 ± 10 ppm tocols content.
format Article
author Yeoh, Chiou Moi
Phuah, Eng Tong
Tang, Teck Kim
Siew, Wai Lin
Abdullah, Luqman Chuah
Choong, Thomas Shean Yaw
spellingShingle Yeoh, Chiou Moi
Phuah, Eng Tong
Tang, Teck Kim
Siew, Wai Lin
Abdullah, Luqman Chuah
Choong, Thomas Shean Yaw
Molecular distillation and characterization of diacylglycerol-enriched palm olein
author_facet Yeoh, Chiou Moi
Phuah, Eng Tong
Tang, Teck Kim
Siew, Wai Lin
Abdullah, Luqman Chuah
Choong, Thomas Shean Yaw
author_sort Yeoh, Chiou Moi
title Molecular distillation and characterization of diacylglycerol-enriched palm olein
title_short Molecular distillation and characterization of diacylglycerol-enriched palm olein
title_full Molecular distillation and characterization of diacylglycerol-enriched palm olein
title_fullStr Molecular distillation and characterization of diacylglycerol-enriched palm olein
title_full_unstemmed Molecular distillation and characterization of diacylglycerol-enriched palm olein
title_sort molecular distillation and characterization of diacylglycerol-enriched palm olein
publisher Wiley
publishDate 2014
url http://psasir.upm.edu.my/id/eprint/34579/
http://onlinelibrary.wiley.com/doi/10.1002/ejlt.201300502/abstract
_version_ 1643831196584509440
score 13.188404