US2008138450A1PendingUtilityA1

Process for the recovery of a phytolipid composition

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Assignee: EASTMAN CHEM COPriority: Sep 10, 2003Filed: Feb 22, 2008Published: Jun 12, 2008
Est. expirySep 10, 2023(expired)· nominal 20-yr term from priority
A23D 7/0053A21D 2/14B01D 3/10A23L 33/11A61K 8/922C11B 11/00C07J 9/00A61Q 19/00Y02W30/74A21D 2/10C11B 13/00A23L 2/52B01D 3/146B01D 1/222A23D 7/011B01D 3/12B01D 3/143B01D 1/22A23D 7/013A23D 9/013B01D 1/065A23D 7/015C07C 7/04A23L 27/60B01D 1/26A23D 7/0056A23L 33/105B01D 3/14A61Q 19/001
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Claims

Abstract

Disclosed is a process for the recovery of a phytolipid composition from a vegetable oil by-product. The phytolipid composition produced comprises squalene, phytosterols, mixed tocopherols and tocotrieneols, and vegetable wax and is useful as an emollient. The phytochemical composition may be applied directly to the skin to provide emolliency. Alternatively, the phytolipid composition may be formulated in various aqueous or anhydrous cosmetic compositions such as creams, lotions, gels, ointments, lip balms, sticks, or pencils for treatment of the skin and lips. The phytolipid composition also may be incorporated into foods, beverages, and nutraceuticals to provide health benefits.

Claims

exact text as granted — not AI-modified
1 . Process for preparing a phytolipid composition comprising squalene, phytosterols, tocopherols and vegetable wax which comprises the steps of, in order:
 (1) distilling a vegetable oil by-product comprised of mixed tocols, fatty acids, hydrocarbons, vegetable waxes, sterol esters of fatty acids, sterols, triterpenoid alcohols, squalene, methyl-sterols, and mono-, di-, and triglycerides at a temperature of about 170 to 320° C. and a pressure of about 0.1 to 35 torr to produce (i) a vapor product comprising fatty acids and low boiling hydrocarbons and (ii) a liquid product;   (2) distilling the liquid product of step (1) at a temperature of about 230 to 300° C. and a pressure of about 0.0005 to 1 torr to produce (i) a second vapor product comprising a mixed tocols concentrate, squalene, phytosterols, and vegetable wax and (ii) a second liquid product;   (3) intimately contacting the condensed vapor product from step (2) with an extractant selected from alkanols and mixtures of acetone and water followed by separation of the resulting mixture into two phases comprising (i) a first phase comprising a majority of the extractant and (ii) a second phase comprising a majority of the condensed vapor effluent from step (2);   (4) collecting the second phase formed in step (3);   (5) cooling the first phase formed in step (3) to effect formation of a precipitate followed by collection of the precipitate; and   (6) combining the second phase collected in step (4) with the precipitate collected in step (5) and removing extractant employed in step (3) from the materials collected in steps (4) and (5);   whereby a phytolipid composition comprising about 15 to 40 weight percent squalene, about 10 to 40 weight percent phytosterols, about 1 to 10 weight percent of mixed tocols and about 25 to 60 weight percent vegetable wax is obtained.   
     
     
         2 . Process according to  claim 1  wherein the vegetable oil by-product is derived from palm oil or rice bran oil and the phytolipid composition obtained comprises about 20 to 35 weight percent squalene, about 15 to 35 weight percent phytosterols, about 2 to 8 weight percent of mixed tocols, about 30 to 55 weight percent vegetable wax and less than 0.1 weight percent extractant/solvent. 
     
     
         3 . Process for preparing a phytolipid composition comprising squalene, phytosterols, tocopherols and vegetable wax which comprises the steps of, in order:
 (1) distilling a vegetable oil by-product comprised of mixed tocols, fatty acids, hydrocarbons, vegetable waxes, sterol esters of fatty acids, sterols, triterpenoid alcohols, squalene, methyl-sterols, and mono-, di-, and triglycerides at a temperature of about 170 to 320° C. and a pressure of about 0.1 to 35 torr to produce (i) a vapor product comprising fatty acids and low boiling hydrocarbons and (ii) a liquid product;   (2) distilling the liquid product of step (1) at a temperature of about 230 to 300° C. and a pressure of about 0.0005 to 1 torr to produce (i) a second vapor product comprising a mixed tocols concentrate, squalene, phytosterols, and vegetable wax and (ii) a second liquid product;   (3) intimately contacting the condensed vapor effluent from step (2) with an extractant selected from alkanols and mixtures of acetone and water followed by separation of the resulting mixture into two phases comprising (i) a first phase comprising a majority of the extractant and (ii) a second phase comprising a majority of the condensed vapor effluent from step (2);   (4) collecting the second phase formed in step (3) and removing extractant employed in step (3);   (5) cooling the first phase formed in step (3) to effect formation of a precipitate followed by collection of the precipitate and removal of extractant employed in step (3); and   (6) combining the second phase collected in step (4) with the precipitate collected in step (5);   whereby a phytochemical composition comprising about 15 to 40 weight percent squalene, about 10 to 40 weight percent phytosterols, about 1 to 10 weight percent of mixed tocols and about 25 to 60 weight percent vegetable wax is obtained.   
     
     
         4 . Process according to  claim 3  wherein the vegetable oil by-product is derived from palm oil or rice bran oil and the phytochemical composition obtained comprises about 20 to 35 weight percent squalene, about 15 to 35 weight percent phytosterols, about 2 to 8 weight percent of mixed tocols, about 30 to 55 weight percent vegetable wax and less than 0.1 weight percent extractant/solvent. 
     
     
         5 . Process for preparing a phytochemical composition comprising squalene, phytosterols, tocopherols and vegetable wax which comprises the steps of, in order:
 (1) distilling a rice bran oil by-product comprised of mixed tocols, fatty acids, hydrocarbons, vegetable waxes, sterol esters of fatty acids, sterols, triterpenoid alcohols, squalene, methyl-sterols, and mono-, di-, and triglycerides at a temperature of about 240 to 290° C. and a pressure of about 0.2 to 20 torr to produce (i) a vapor product comprising fatty acids and low boiling hydrocarbons and (ii) a liquid product;   (2) distilling the liquid product of step (1) at a temperature of about 230 to 260° C. and a pressure of about 0.005 to 0.5 torr to produce (i) a second vapor product comprising a mixed tocols concentrate, squalene, phytosterols, and vegetable wax and (ii) a second liquid product;   (3) intimately contacting the condensed vapor effluent from step (2) with an extractant selected from methanol, ethanol, propanol and 2-propanol wherein the volume:volume ratio of extractant:condensed vapor effluent from step (2) is about 6:1 to 12:1 followed by separation of the resulting mixture into two phases comprising (i) a first phase comprising a majority of the extractant and (ii) a second phase comprising a majority of the condensed vapor effluent from step (2);   (4) collecting the second phase formed in step (3);   (5) cooling the first phase formed in step (3) to effect formation of a precipitate followed by collection of the precipitate; and   (6) combining the second phase collected in step (4) with the precipitate collected in step (5) and heating the materials collected in steps (4) and (5) at a temperature of about 50 to 100° C. and a pressure of about 200 to 1 Torr to remove extractant employed in step (3);   whereby a phytolipid composition comprising about 20 to 35 weight percent squalene, about 15 to 35 weight percent phytosterols, about 2 to 8 weight percent of mixed tocols, about 30 to 55 weight percent vegetable wax and less than 0.1 weight percent extractant/solvent is obtained.   
     
     
         6 . Process according to  claim 5  wherein the extractant employed in step (3) is methanol and the phytolipid composition obtained contains less than 100 ppm methanol. 
     
     
         7 - 9 . (canceled) 
     
     
         10 . A skin care preparation intended for application to human skin comprising the phytolipid composition obtained from the process of  claim 1 . 
     
     
         11 . A skin care preparation intended for application to human skin comprising a phytolipid composition consisting essentially of about 15 to 40 weight percent squalene, about 10 to 40 weight percent phytosterols, about 1 to 10 weight percent of mixed tocols and about 25 to 60 weight percent vegetable wax and contains less than 0.1 weight percent solvent. 
     
     
         12 . The skin care preparation according to  claim 11 , wherein the phytolipid composition is derived from rice bran oil and consisting essentially of about 20 to 35 weight percent squalene, about 15 to 35 weight percent phytosterols, about 4 to 8 weight percent of mixed tocols, about 30 to 55 weight percent vegetable wax and less than 0.1 weight percent solvent. 
     
     
         13 . A lip balm comprising the phytolipid composition obtained from the process of  claim 1 . 
     
     
         14 - 18 . (canceled) 
     
     
         19 . A skin care preparation intended for application to human skin comprising an emulsion of water and the phytolipid composition obtained from the process of  claim 2 . 
     
     
         20 . A skin care preparation intended for application to human skin comprising an emulsion of water and the phytolipid composition according to  claim 11  further characterized by the following properties: an iodine number of about 50 to 70; a saponification number of about 15 to 35 mg KOH per g lipid composition; a melting range of about 30 to 55° C.; an acid number of less than about 2 mg KOH per g lipid composition; and a peroxide value of less than about 10 millieguivalents per kg lipid composition wherein phytolipid composition:water weight ratio is about 1:50 to 2:1. 
     
     
         21 - 32 . (canceled)

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