首页> 外国专利> Fractionation of olibanum Resin using Supercritical Carbon Dioxide

Fractionation of olibanum Resin using Supercritical Carbon Dioxide

机译:使用超临界二氧化碳分馏olibanum树脂

摘要

A process for extracting essential oil from sequentially, incensole and boswellic acid from olibanum resin,Understanding the stages of the procedure: (a) Crush olibanum Resin; (b) Separating a First fraction of Essential Oil with liquid carbon dioxide to a First temperature QEU varies between 0 Deg and 30 deg C and a pressure of between 40 and 60 bar bar with soft or supercritical carbon dioxide.And with a First Flow that varies between 10 and 400 g of Crushed material g / kg / min until you can no longer Recover more essential oil or extract yield is lower than 0.1% of initial Mass per hour; (c) recover Essential Oil separator; (d) Separating a fraction of Second Derivatives of incensole with Supercritical Carbon Dioxide to a Second temperatureVaries between 31 and 100 deg C and a pressure of at least 72 Second,8 bar and a Second Flow that varies between 10 and 400 g of Crushed material g / kg / min until you can no longer Recover more incensole or their Derivatives or the extract yield is lower than 0.1% of initial Mass per hour; (e) recover from incensole optionally separator; (f)Continue the process of Separation with Supercritical Carbon Dioxide to other sets of temperature and / or pressure increasing until they separated fractions most desired; (g) to separate a fracciu00f3Additional boswellic acid in Supercritical Carbon Dioxide at a temperature of at least 31 deg C and a pressure of at least 728 bar and to a Flow that varies between G and 400 g / kg / min using a cosolvent Crushed material at a level that varies between 0.05 and 50% in volume.0% in volume of flow of CO2 until it achieves complete separation of boswellic acids or determines that it can extract more materials or the extract yield is lower than 0.1% of initial Mass per hour; (H) recover boswellic acid of the separator and remove the cosolvent by Evaporation or Distillation; Optionally,Continue the process of Separation with Supercritical Carbon Dioxide to another set of pressure and temperature and cosolvent until they separate all the desired fractions; (j) to recover the resCough not remaining separate.
机译:一种从油脂树脂中依次提取香豆油和香气酸的精油的方法,其步骤如下:(a)粉碎油脂树脂; (b)将第一馏分的精油与液态二氧化碳分离至第一温度QEU在0°C至30摄氏度之间变化,压力在40至60 bar bar之间(使用软或超临界二氧化碳)变化。在10到400克碎料g / kg / min之间变化,直到不再能回收更多精油或提取物产量低于每小时初始质量的0.1%为止; (c)回收精油分离器; (d)用超临界二氧化碳将香茅素的二阶衍生物的一部分分离到第二温度,温度在31至100摄氏度之间,压力至少为72 Seconds,8 bar,第二流量在10至400 g压碎物料之间变化克/千克/分钟,直到您无法再回收更多的琴竹烯或其衍生物,或者提取物收率低于每小时初始质量的0.1%为止; (e)从可选的分离剂中回收; (f)继续使用超临界二氧化碳进行分离,直至其他温度和压力升高,直到它们分离出最需要的馏分为止; (g)在至少31摄氏度的温度和至少728巴的压力下,在超临界二氧化碳中分离出fracci u00f3附加的香气酸,流量为G至400 g / kg kg / min助溶剂压碎的物料,其含量在0.05至50%的体积之间变化.CO2流量的0%的体积,直到实现完全分离乳香酸或确定它可以提取更多的材料或提取率低于0.1%每小时的初始质量; (H)回收分离器的乳香酸并通过蒸发或蒸馏除去助溶剂;可选地,将超临界二氧化碳的分离过程继续进行到另一组压力,温度和助溶剂的分离过程,直到它们分离出所有所需的馏分为止; (j)收回未分开的咳嗽。

著录项

  • 公开/公告号ES2673609T3

    专利类型

  • 公开/公告日2018-06-25

    原文格式PDF

  • 申请/专利权人 PHYTOVATION LTD;

    申请/专利号ES20150771578T

  • 发明设计人 MARRIOTT RAYMOND;

    申请日2015-09-28

  • 分类号C11B9/02;B01D11/02;B01D11/04;

  • 国家 ES

  • 入库时间 2022-08-21 12:48:30

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