Extraction of particulate materials
There is disclosed a method of extracting components from particulate materials, for example, from ground seed particles fed from a mill 2. The method includes the steps of mixing the particles with a polar solvent from a feed line 14 in a mixing zone 16 to provide a slurry. The slurry is then passe...
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creator | DIOSADY, LEVENTE L TAR, CSABA G RUBIN, LEON J |
description | There is disclosed a method of extracting components from particulate materials, for example, from ground seed particles fed from a mill 2. The method includes the steps of mixing the particles with a polar solvent from a feed line 14 in a mixing zone 16 to provide a slurry. The slurry is then passed through an extraction zone 22. A non-polar solvent from a feed line 24 is passed countercurrently to the slurry through the extraction zone 22. The non-polar solvent has a different density from the polar solvent and is substantially immiscible with the polar solvent. The non-polar solvent with non-polar components dissolved therein is separated into a non-polar solvent fraction 32 and an oil fraction 34 in a solvent recovery unit 28. The polar solvent with dissolved components therein and the entrained particles leave the extraction zone 22 and the solid particles are separated in a separation zone 35. This process is particularly beneficial for use in the extraction of ground oil-seed particles. |
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The method includes the steps of mixing the particles with a polar solvent from a feed line 14 in a mixing zone 16 to provide a slurry. The slurry is then passed through an extraction zone 22. A non-polar solvent from a feed line 24 is passed countercurrently to the slurry through the extraction zone 22. The non-polar solvent has a different density from the polar solvent and is substantially immiscible with the polar solvent. The non-polar solvent with non-polar components dissolved therein is separated into a non-polar solvent fraction 32 and an oil fraction 34 in a solvent recovery unit 28. The polar solvent with dissolved components therein and the entrained particles leave the extraction zone 22 and the solid particles are separated in a separation zone 35. This process is particularly beneficial for use in the extraction of ground oil-seed particles.</description><language>eng ; fre ; ger</language><subject>ANIMAL AND VEGETABLE OILS, FATS, FATTY SUBSTANCES AND WAXES ; CANDLES ; CHEMISTRY ; DETERGENTS ; ESSENTIAL OILS ; 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>1988</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=19881109&DB=EPODOC&CC=EP&NR=0290156A2$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19881109&DB=EPODOC&CC=EP&NR=0290156A2$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>DIOSADY, LEVENTE L</creatorcontrib><creatorcontrib>TAR, CSABA G</creatorcontrib><creatorcontrib>RUBIN, LEON J</creatorcontrib><title>Extraction of particulate materials</title><description>There is disclosed a method of extracting components from particulate materials, for example, from ground seed particles fed from a mill 2. The method includes the steps of mixing the particles with a polar solvent from a feed line 14 in a mixing zone 16 to provide a slurry. The slurry is then passed through an extraction zone 22. A non-polar solvent from a feed line 24 is passed countercurrently to the slurry through the extraction zone 22. The non-polar solvent has a different density from the polar solvent and is substantially immiscible with the polar solvent. The non-polar solvent with non-polar components dissolved therein is separated into a non-polar solvent fraction 32 and an oil fraction 34 in a solvent recovery unit 28. The polar solvent with dissolved components therein and the entrained particles leave the extraction zone 22 and the solid particles are separated in a separation zone 35. 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The method includes the steps of mixing the particles with a polar solvent from a feed line 14 in a mixing zone 16 to provide a slurry. The slurry is then passed through an extraction zone 22. A non-polar solvent from a feed line 24 is passed countercurrently to the slurry through the extraction zone 22. The non-polar solvent has a different density from the polar solvent and is substantially immiscible with the polar solvent. The non-polar solvent with non-polar components dissolved therein is separated into a non-polar solvent fraction 32 and an oil fraction 34 in a solvent recovery unit 28. The polar solvent with dissolved components therein and the entrained particles leave the extraction zone 22 and the solid particles are separated in a separation zone 35. This process is particularly beneficial for use in the extraction of ground oil-seed particles.</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 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 | Extraction of particulate materials |
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