Process for purification of EPA (eicosapentanoic acid) ethyl ester from fish oil
Disclosed is a process for extracting and purifying EPA (Eicosapentanoic acid) ethyl ester from a crude fish oil feedstock using a combination of novel esterification and simulated moving bed (SMB) techniques. Crude fish oil diluted in non-polar solvent is esterified with an acid and then transester...
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| creator | NAGARAJAN GOPAL KRISHNA OROSKAR ANIL R |
| description | Disclosed is a process for extracting and purifying EPA (Eicosapentanoic acid) ethyl ester from a crude fish oil feedstock using a combination of novel esterification and simulated moving bed (SMB) techniques. Crude fish oil diluted in non-polar solvent is esterified with an acid and then transesterified with a base. Following washing, the non-polar phase is directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an enhanced omega-3 product, comprising EPA. In a further embodiment, the enhanced omega-3 product is passed to a second and third SMB zones operating in reverse phase using a hydrophobic stationary phase and a polar mobile phase desorbent. The process is useful for producing high purity EPA at purities in excess of 97 wt-% which are not economically recoverable by conventional distillation methods combined with conventional SMB configurations. |
| format | Patent |
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Crude fish oil diluted in non-polar solvent is esterified with an acid and then transesterified with a base. Following washing, the non-polar phase is directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an enhanced omega-3 product, comprising EPA. In a further embodiment, the enhanced omega-3 product is passed to a second and third SMB zones operating in reverse phase using a hydrophobic stationary phase and a polar mobile phase desorbent. The process is useful for producing high purity EPA at purities in excess of 97 wt-% which are not economically recoverable by conventional distillation methods combined with conventional SMB configurations.</description><language>eng</language><subject>ANIMAL AND VEGETABLE OILS, FATS, FATTY SUBSTANCES AND WAXES ; CANDLES ; CHEMISTRY ; DETERGENTS ; ESSENTIAL OILS ; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS,OILS, OR FATTY ACIDS OBTAINED THEREFROM ; FATTY ACIDS FROM FATS, OILS OR WAXES ; FATTY ACIDS THEREFROM ; METALLURGY ; PERFORMING OPERATIONS ; PERFUMES ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; PRODUCING (PRESSING, EXTRACTION), REFINING AND PRESERVINGFATS, FATTY SUBSTANCES (e.g. LANOLIN), FATTY OILS AND WAXES,INCLUDING EXTRACTION FROM WASTE MATERIALS ; SEPARATION ; TRANSPORTING</subject><creationdate>2015</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20151020&DB=EPODOC&CC=US&NR=9163198B2$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20151020&DB=EPODOC&CC=US&NR=9163198B2$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>NAGARAJAN GOPAL KRISHNA</creatorcontrib><creatorcontrib>OROSKAR ANIL R</creatorcontrib><title>Process for purification of EPA (eicosapentanoic acid) ethyl ester from fish oil</title><description>Disclosed is a process for extracting and purifying EPA (Eicosapentanoic acid) ethyl ester from a crude fish oil feedstock using a combination of novel esterification and simulated moving bed (SMB) techniques. Crude fish oil diluted in non-polar solvent is esterified with an acid and then transesterified with a base. Following washing, the non-polar phase is directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an enhanced omega-3 product, comprising EPA. In a further embodiment, the enhanced omega-3 product is passed to a second and third SMB zones operating in reverse phase using a hydrophobic stationary phase and a polar mobile phase desorbent. 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Crude fish oil diluted in non-polar solvent is esterified with an acid and then transesterified with a base. Following washing, the non-polar phase is directly passed to an SMB zone, comprising a normal phase separation with a hydrophilic stationary phase agent and a non-polar/organic polar mobile phase desorbent to provide an enhanced omega-3 product, comprising EPA. In a further embodiment, the enhanced omega-3 product is passed to a second and third SMB zones operating in reverse phase using a hydrophobic stationary phase and a polar mobile phase desorbent. The process is useful for producing high purity EPA at purities in excess of 97 wt-% which are not economically recoverable by conventional distillation methods combined with conventional SMB configurations.</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | ANIMAL AND VEGETABLE OILS, FATS, FATTY SUBSTANCES AND WAXES CANDLES CHEMISTRY DETERGENTS ESSENTIAL OILS FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS,OILS, OR FATTY ACIDS OBTAINED THEREFROM FATTY ACIDS FROM FATS, OILS OR WAXES FATTY ACIDS THEREFROM METALLURGY PERFORMING OPERATIONS PERFUMES PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL PRODUCING (PRESSING, EXTRACTION), REFINING AND PRESERVINGFATS, FATTY SUBSTANCES (e.g. LANOLIN), FATTY OILS AND WAXES,INCLUDING EXTRACTION FROM WASTE MATERIALS SEPARATION TRANSPORTING |
| title | Process for purification of EPA (eicosapentanoic acid) ethyl ester from fish oil |
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