食品科学

• 工艺技术 • 上一篇    下一篇

胡萝卜中类胡萝卜素的提取动力学

刘晓庚1,陈梅梅2,陈优生3,张雅坤1,袁 磊1,胡唐明2,王立峰1,彭冬梅1   

  1. 1.南京财经大学食品科学与工程学院,江苏省现代粮食流通与安全协同创新中心,江苏省粮油品质控制及深加工技术重点实验室,
    江苏 南京 210023;2.南京财经大学图书馆,江苏 南京 210023;3.广东食品药品职业学院,广东 广州 510520
  • 出版日期:2015-08-25 发布日期:2015-08-17
  • 基金资助:

    江苏高校优势学科建设工程资助项目;“十二五”国家科技支撑计划项目(2012BAD37B08);
    江苏省粮油品质控制及深加工技术重点实验室项目(LYPK201301)

Kinetic Studies on Extraction of Carotenoids from Carrot Powder

LIU Xiaogeng1, CHEN Meimei2, CHEN Yousheng3, ZHANG Yakun1, YUAN Lei1, HU Tangming2, WANG Lifeng1, PENG Dongmei1   

  1. 1. Key Laboratory of Grains and Oils Quality Control and Processing, Collaborative Innovation Center for Modern Grain Circulation and Safety,
    College of Food Science and Engineering, Nanjing University of Finance and Economics, Nanjing 210023, China;
    2. The Library of Nanjing University of Finance and Economics, Nanjing 210023, China;
    3. Guangdong Food and Drug Vocational College, Guangzhou 510520, China
  • Online:2015-08-25 Published:2015-08-17

摘要:

使用抗坏血酸和2,6-二叔丁基-4-甲基苯酚保护剂,以石油醚-丙酮(体积比4∶1)混合液为提取剂,分别用水浴直接提取法、超声辅助提取法和微波辅助提取法从胡萝卜粉中提取类胡萝卜素。采用不同温度和原料粒度进行从胡萝卜粉中提取类胡萝卜素的提取动力学实验。结果表明,水浴法和超声辅助法是符合反应-内扩散控制的动力学模型,所得提取动力学方程分别为:1)水浴法:y=0.009 9t+0.110 7(R2=0.920 9,30 ℃)、y= 0.018 6t+0.096 1(R2=0.893 7,40 ℃)、y=0.018 2t+0.088 6(R2=0.965 7,45 ℃);2)超声辅助法:y=0.001 1t+0.080 9(R2= 0.917 9,30 ℃)、y=0.001 6t+0.043 9(R2=0.978 8,40 ℃)、y=0.001 8t+0.039(R2=0.964 2,45 ℃)。表观活化能分别为Ea(水浴)=-26.825 1 kJ/mol和Ea(超声)=-35.196 5 kJ/mol。而微波辅助法则是符合混合控制的动力学模型,其方程为y=0.027 5t+0.344 6(R2=0.972 3,30 ℃)、y=0.031 9t+0.426 5(R2=0.868 9,40 ℃)、y=0.058 7t+0.275 1(R2=0.973 4,45 ℃),表观活化能为E a(微波)=-36.105 2 kJ/mol。通过水浴法考察原料粒度对提取动力学的影响,结果表明原料粒度对提取速率和提取率的影响程度是60~80 目>40~60 目>20~40 目,即粒度越细越有利于类胡萝卜素的提取。

关键词: 胡萝卜粉, 类胡萝卜素, 提取方法, 提取动力学, 动力学方程, 表观活化能

Abstract:

In this paper, kinetic studies were carried out to investigate the extraction of carotenoids from carrot powders of
different particle sizes by three different methods, namely water bath, ultrasonic-assisted and microwave-assisted extraction,
at different temperatures respectively, using vitamin C and BHT as antioxidants and petroleum:acetone (4:1, V/V) as
extractant. The results showed that the kinetic models for water bath and ultrasonic-assisted extraction conformed to the
internal diffusion-controlled chemical kinetic models, which were as follows: y = 0.009 9t + 0.110 7 (R2 = 0.920 9, 30 ℃), y =
0.018 6t + 0.096 1 (R2 = 0.893 7, 40 ℃), y = 0.018 2t + 0.088 6 (R2 = 0.965 7, 45 ℃) for water bath extraction; y = 0.001 1t +
0.080 9 (R2 = 0.917 9, 30 ℃ ), y = 0.001 6t + 0.043 9 (R2 = 0.978 8, 40 ℃ ), y = 0.001 8t + 0.039 (R2 = 0.964 2, 45 ℃ ) for
ultrasonic-assisted extraction. In addition, the values of activation energy were Ea (water bath extraction) = -26.825 1 kJ/mol
and Ea (ultrasonic-assisted extraction) = -35.196 5 kJ/mol. However, the kinetic model for microwave-assisted extraction
conformed to the hybrid-controlled kinetic model and the fitted equations were as follows: y = 0.027 5t + 0.344 6 (R2 = 0.972 3,
30 ℃), y = 0.031 9t + 0.426 5 (R2 = 0.868 9, 40 ℃), y = 0.058 7t + 0.275 1 (R2 = 0.973 4, 45 ℃); the value of activation
energy, Ea(microwave-assisted extraction), was -36.105 2 kJ/mol. The extraction efficiency and rate with water bath was
affected by raw material particle size in the decreasing order of 60–80 mesh > 40–60 mesh > 20–40 mesh. Therefore, small
particle size is beneficial for the extraction of caroteinoids.

Key words: carrot powder, carotenoids, extraction methods, extraction kinetics, kinetic equation, activation energy

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