Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid

Public interest in natural drugs has enormously increased in industrialized countries with expanding use of plants and herbal medicines. Recently, one of the plant herbs involves in curing cancer diseases has emerged and is recognized as Christia vespertilionis. Previously, Christia vespertilionis w...

詳細記述

保存先:
書誌詳細
第一著者: Abd Hamid, Izni Atikah
フォーマット: 学位論文
言語:English
出版事項: 2019
主題:
オンライン・アクセス:https://ir.uitm.edu.my/id/eprint/82813/1/82813.pdf
https://ir.uitm.edu.my/id/eprint/82813/
タグ: タグ追加
タグなし, このレコードへの初めてのタグを付けませんか!
id my.uitm.ir.82813
record_format eprints
spelling my.uitm.ir.828132024-02-02T07:41:29Z https://ir.uitm.edu.my/id/eprint/82813/ Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid Abd Hamid, Izni Atikah Biochemistry Public interest in natural drugs has enormously increased in industrialized countries with expanding use of plants and herbal medicines. Recently, one of the plant herbs involves in curing cancer diseases has emerged and is recognized as Christia vespertilionis. Previously, Christia vespertilionis was extracted using solvent extraction such as hexane, methanol and dichloromethane. Unfortunately, conventional solvent was toxic, unsafe and might contaminate the extract of the product especially product that were used for medicinal purposes. Therefore, extraction of Christia vespertilionis plant using pure supercritical carbon dioxide (SC-CO2) without any co-solvent was assessed for the first time. The aim of the research is to investigate kinetic behaviour of Christia vespertilionis oil in SC-CO2 fluid in terms of extraction yield, oil’s solubility, mass transfer and phytocompound’s characterization. The effect of extraction parameter such as temperatures (40 to 85°C) and pressures (276 to 414 bar) of SC-CO2 extraction on yield, solubility and mass transfer of Christia vespertilionis oil were evaluated. Extracted oil was then analysed under gas chromatography mass spectrometry according to their retention indices and mass spectra. Experimental data of solubility was correlated using four empirical of density-based models i.e. Chrastil (1982), del Valle and Aguilera (1988), Adachi and Lu (1983), and Sparks et al. (2008) models. Furthermore, behaviour of extraction yield and mass transfer of oil in solid and fluid phases was modeled using a Lack’s plug flow model by Sovova (1994). Results demonstrated that the oil yield and solubility were highly dependent on the extraction pressure. 2019 Thesis NonPeerReviewed text en https://ir.uitm.edu.my/id/eprint/82813/1/82813.pdf Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid. (2019) PhD thesis, thesis, Universiti Teknologi MARA (UiTM).
institution Universiti Teknologi Mara
building Tun Abdul Razak Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Mara
content_source UiTM Institutional Repository
url_provider http://ir.uitm.edu.my/
language English
topic Biochemistry
spellingShingle Biochemistry
Abd Hamid, Izni Atikah
Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
description Public interest in natural drugs has enormously increased in industrialized countries with expanding use of plants and herbal medicines. Recently, one of the plant herbs involves in curing cancer diseases has emerged and is recognized as Christia vespertilionis. Previously, Christia vespertilionis was extracted using solvent extraction such as hexane, methanol and dichloromethane. Unfortunately, conventional solvent was toxic, unsafe and might contaminate the extract of the product especially product that were used for medicinal purposes. Therefore, extraction of Christia vespertilionis plant using pure supercritical carbon dioxide (SC-CO2) without any co-solvent was assessed for the first time. The aim of the research is to investigate kinetic behaviour of Christia vespertilionis oil in SC-CO2 fluid in terms of extraction yield, oil’s solubility, mass transfer and phytocompound’s characterization. The effect of extraction parameter such as temperatures (40 to 85°C) and pressures (276 to 414 bar) of SC-CO2 extraction on yield, solubility and mass transfer of Christia vespertilionis oil were evaluated. Extracted oil was then analysed under gas chromatography mass spectrometry according to their retention indices and mass spectra. Experimental data of solubility was correlated using four empirical of density-based models i.e. Chrastil (1982), del Valle and Aguilera (1988), Adachi and Lu (1983), and Sparks et al. (2008) models. Furthermore, behaviour of extraction yield and mass transfer of oil in solid and fluid phases was modeled using a Lack’s plug flow model by Sovova (1994). Results demonstrated that the oil yield and solubility were highly dependent on the extraction pressure.
format Thesis
author Abd Hamid, Izni Atikah
author_facet Abd Hamid, Izni Atikah
author_sort Abd Hamid, Izni Atikah
title Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
title_short Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
title_full Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
title_fullStr Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
title_full_unstemmed Kinetic behaviour of Christia vespertilionis oil in supercritical carbon dioxide / Izni Atikah Abd Hamid
title_sort kinetic behaviour of christia vespertilionis oil in supercritical carbon dioxide / izni atikah abd hamid
publishDate 2019
url https://ir.uitm.edu.my/id/eprint/82813/1/82813.pdf
https://ir.uitm.edu.my/id/eprint/82813/
_version_ 1789944544483082240
score 13.251813