Process for extracting prolycopene oil resin with supercritical fluid
A technology of lycopene oil and supercritical fluid, which is applied in the production of fat oil/fat and fat production, can solve the problems of large loss of lycopene, solvent residue, low extraction rate, etc., and achieves short extraction cycle, low solvent consumption, The effect of low solvent cost
Inactive Publication Date: 2002-02-06
XINJIANG UNIVERSITY +1
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Problems solved by technology
The disadvantages of solvent extraction are the consumption of a large amount of valuable organic solvents, high energy con
Method used
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Embodiment 1
[0020] Extraction conditions: Pressure: 35MPa Temperature: 70°C CO 2 Flow rate: 25kg / hr Raw material particle size: 60-80 mesh Extraction time: 2 hours The equipment uses an extraction kettle (model HA121-50-02, Jiangsu Haian Petroleum Research Instrument Factory)
[0021]
[0022]
[0023]
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A process for extracting lycopene oil resin from tomato or water melon by supercritical fluid (CO2, propane, ethane, or ethene) includes pre-treating for removing sugar, gum and water from raw material, extracting with said supercritical fluid to obtain lycopene oil resin, packing it under protection of inertial gas in dark position or vacuum packing, and low-temp storage. Its advantages are simple process, high efficiency, low energy consumption, no pollution and low cost.
Description
technical field [0001] The invention relates to a method for extracting lycopene oleoresin by using tomato, watermelon and the like as raw materials, especially a method for extracting lycopene oleoresin by using supercritical carbon dioxide, propane, ethane and ethylene fluid. Background technique [0002] The countries that produce lycopene oleoresin on a large scale in the world today mainly include Israel, the United States, Germany, Japan and other countries, and the method used is solvent extraction [WO97 / 48287, WO96 / 13178 (CN1176577A)]. The disadvantages of the solvent extraction method are the consumption of a large amount of valuable organic solvents, high energy consumption, large loss of lycopene during the extraction process, solvent residues, and low extraction rate (only about 80%). Contents of the invention [0003] In order to solve the shortcomings of the above-mentioned existing solvent extraction method for extracting lycopene, the present invention prov...
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Inventor 刘奎钫赵锁奇刘玉梅胡云翔刘罡王仁安李刚齐国鹏陈德军刘玉英
Owner XINJIANG UNIVERSITY
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