食品科学 ›› 2009, Vol. 30 ›› Issue (14): 41-46.doi: 10.7506/spkx1002-6630-200914003

• 工艺技术 • 上一篇    下一篇

超临界CO2 反相微乳萃取人参皂甙的研究

李 超1,2,王卫东1,郑 义1,丘泰球2,*   

  1. 1.徐州工程学院食品工程学院 2.华南理工大学轻工与食品学院
  • 收稿日期:2008-10-24 修回日期:2009-01-22 出版日期:2009-07-15 发布日期:2010-12-29
  • 通讯作者: 丘泰球2,* E-mail:chaoge002@163.com
  • 基金资助:

    广东省科技计划项目(2006B35605002); 广州市科技计划项目(2007Z3-E5131)

Supercritical CO2 Reverse Microemulsion Extraction of Ginsenosides from Panax ginseng

LI Chao1,2,WANG Wei-dong1,ZHENG Yi1,QIU Tai-qiu2,*   

  1. 1. College of Food Engineering, Xuzhou Institute of Technology, Xuzhou 210008, China ;
    2. College of Light Industry and Food Sciences, South China University of Technology, Guangzhou 510640, China
  • Received:2008-10-24 Revised:2009-01-22 Online:2009-07-15 Published:2010-12-29
  • Contact: QIU Tai-qiu2,* E-mail:chaoge002@163.com

摘要:

利用萃取罐体积为1 L 的超临界CO2 萃取设备,采用琥珀酸二(2- 乙基己基)酯磺酸钠(AOT)/ 乙醇/ 水/ 超临界CO2 反相微乳对人参皂甙的萃取进行了研究。结果表明:最优萃取参数为萃取温度55℃,萃取时间3h,加水量 36ml/100g 人参,萃取压力 30MPa 和 AOT 添加量0.06mol/100g 人参,此时人参皂甙的得率为0.757%;E=0.870 ×(1 - e-0.618t)为超临界CO2 反相微乳萃取人参皂甙的具体动力学模型方程;超临界CO2 反相微乳萃取与超临界CO2 萃取人参皂甙相比是一种相对有效的萃取技术。

关键词: 超临界CO2反相微乳萃取, 超临界CO2萃取, 人参皂甙

Abstract:

The extraction of ginsenosides from Panax ginseng root using supercritical CO2 reverse microemulsion formed by bis(2-ethylhexyl) sodium sulfosuccinate (AOT), ethanol and water was studied, which was carried out in a 1 L supercritical CO2 extraction device. Single-factor and orthogonal array design methods were applied to optimize the extraction. The effects of 7 parameters on ginsenosides extraction were investigated by the single-factor method. A higher extraction yield of ginsenosides was achieved using ethanol as the cosufactant in comparison with butanol and n-pentanol, with the optimal added amount of 120 ml/ 100 g ginseng. Other 5 parameters such as amount of added water, amount of added AOT, extraction time, temperature and pressure were optimized using the orthogonal array design method. The optimal levels of the 5 parameters for improved ginsenosides extraction were determined as follows: amount of added water 36 ml/ 100 g ginseng, amount of added AOT 0.06 mol/100 g ginseng, extraction time 3 h, extraction temperature 55 ℃ and extraction pressure 30 MPa. An extraction yield of 0.757% was achieved under the optimized conditions. Moreover a dynamic model for ginsenosides yield as a function of extraction time was developed, which was E = 0.870 × (1- e-0.618t). Compared to supercritical CO2 extraction (SCE), this extraction method yielded more ginsenosides.

Key words: supercritical CO2 reverse microemulsion extraction, supercritical CO2 extraction, ginsenosides

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