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1. 发明申请

US20110124728A1 DHA ENRICHMENT PROCESS 审中-公开
标题翻译： DHA充实过程
公开(公告)号：US20110124728A1
公开(公告)日：2011-05-26
申请号：US12950723
申请日：2010-11-19
申请人： Florence MARCIACQ , Mathieu Soulayres , Bernard Freiss
发明人： Florence MARCIACQ , Mathieu Soulayres , Bernard Freiss
IPC分类号： A61K31/225 , A61P43/00
CPC分类号： C11B1/104 , A23D9/007 , C11B7/005 , C11C1/005 , C11C1/08 , C11C3/003 , Y02P20/544
摘要： The present invention relates to a continuous process of DHA enrichment of a solution of fatty acids or derivatives thereof comprising less than 50% of DHA relative to the total fatty acids of the solution or to derivatives thereof, wherein the process comprises the steps of (a) simultaneous countercurrent injection, into a fractionation column, of the flow of the solution of fatty acids or of derivatives thereof and of a flow of supercritical CO2 at a temperature of less than or equal to 70° C. and at a pressure of between 100×105 Pa and 160×105 Pa, wherein the level of supercritical CO2 is between 30 and 70, and (b) recovery of the residue comprising at least 50% of DHA relative to the total fatty acids of the residue or to derivatives thereof, wherein the DHA yield is greater than or equal to 60%.
摘要翻译：本发明涉及DHA富集脂肪酸或其衍生物的方法的连续方法，其包含相对于溶液的总脂肪酸或其衍生物的小于50％的DHA，其中该方法包括以下步骤：（a ）在小于或等于70℃的温度和在100℃之间的压力下同时逆流注入脂肪酸或其衍生物和超临界CO 2流的流动的分馏塔中 ×105Pa和160×105Pa，其中超临界CO 2的水平在30和70之间，和（b）相对于残基或其衍生物的总脂肪酸，回收包含至少50％的DHA的残余物，其中DHA产率大于或等于60％。

2. 发明授权

US07906666B2 DHA enrichment process 有权
标题翻译： DHA浓缩过程
公开(公告)号：US07906666B2
公开(公告)日：2011-03-15
申请号：US12086771
申请日：2006-12-19
申请人： Florence Marciacq , Mathieu Soulayres , Bernard Freiss
发明人： Florence Marciacq , Mathieu Soulayres , Bernard Freiss
IPC分类号： C11B3/00
CPC分类号： C11B1/104 , A23D9/007 , C11B7/005 , C11C1/005 , C11C1/08 , C11C3/003 , Y02P20/544
摘要： The present invention relates to a continuous process of DHA enrichment of a solution of fatty acids or derivatives thereof comprising less than 50% of DHA relative to the total fatty acids of the solution or to derivatives thereof, wherein the process comprises the steps of (a) simultaneous countercurrent injection, into a fractionation column, of the flow of the solution of fatty acids or of derivatives thereof and of a flow of supercritical CO2 at a temperature of less than or equal to 70° C. and at a pressure of between 100×105 Pa and 160×105 Pa, wherein the level of supercritical CO2 is between 30 and 70, and (b) recovery of the residue comprising at least 50% of DHA relative to the total fatty acids of the residue or to derivatives thereof, wherein the DHA yield is greater than or equal to 60%.
摘要翻译：本发明涉及DHA富集脂肪酸或其衍生物的方法的连续方法，其包含相对于溶液的总脂肪酸或其衍生物的小于50％的DHA，其中该方法包括以下步骤：（a ）在小于或等于70℃的温度和在100℃之间的压力下同时逆流注入脂肪酸或其衍生物和超临界CO 2流的流动的分馏塔中 ×105Pa和160×105Pa，其中超临界CO 2的水平在30和70之间，和（b）相对于残基或其衍生物的总脂肪酸，回收包含至少50％的DHA的残余物，其中DHA产率大于或等于60％。

3. 发明申请

US20090036532A1 DHA Enrichment Process 有权
标题翻译： DHA浓缩过程
公开(公告)号：US20090036532A1
公开(公告)日：2009-02-05
申请号：US12086771
申请日：2006-12-19
申请人： Florence Marciacq , Mathieu Soulayres , Bernard Freiss
发明人： Florence Marciacq , Mathieu Soulayres , Bernard Freiss
IPC分类号： A61K31/202 , A61P25/00 , A61P25/28
CPC分类号： C11B1/104 , A23D9/007 , C11B7/005 , C11C1/005 , C11C1/08 , C11C3/003 , Y02P20/544
摘要： The present invention relates to a continuous process of DHA enrichment of a solution of fatty acids or derivatives thereof comprising less than 50% of DHA relative to the total fatty acids of the solution or to derivatives thereof, wherein the process comprises the steps of (a) simultaneous countercurrent injection, into a fractionation column, of the flow of the solution of fatty acids or of derivatives thereof and of a flow of supercritical CO2 at a temperature of less than or equal to 70° C. and at a pressure of between 100×105 Pa and 160×105 Pa, wherein the level of supercritical CO2 is between 30 and 70, and (b) recovery of the residue comprising at least 50% of DHA relative to the total fatty acids of the residue or to derivatives thereof, wherein the DHA yield is greater than or equal to 60%.
摘要翻译：本发明涉及DHA富集脂肪酸或其衍生物的方法的连续方法，其包含相对于溶液的总脂肪酸或其衍生物的小于50％的DHA，其中该方法包括以下步骤：（a ）在小于或等于70℃的温度和在100×10 5的压力下同时逆流注入脂肪酸或其衍生物和超临界CO 2流的流动的分馏塔中 Pa和160×10 5 Pa，其中超临界CO 2的水平在30和70之间，和（b）相对于残基或其衍生物的总脂肪酸，包含至少50％的DHA的残余物的回收，其中DHA产率大于或等于60％。

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