Method for removing various hazardous substances in capsorubin
A technology for capsanthin and hazardous substances, which is applied in the field of extraction of natural products, can solve the problems of different adsorption effects, loss of pigment and high temperature, and achieves the effects of simple operation, less loss and improved safety.
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Embodiment 1
[0038] The present embodiment relates to the removal of harmful components in capsanthin, comprising the following steps:
[0039] Dissolve capsanthin 1000g (color value 145.2, benzopyrene 26ppb, total Sudan red (Sudan Ⅰ-Ⅳ) 200ppb, rhodamine B 65ppb, ethion 36ppm, chlorpyrifos 12ppm, triazophos 21ppm) into vegetable oil pumping Mixed solution of extraction solvent and acetone (vegetable oil extraction solvent: acetone = 3:2) 10000ml, filter to remove solid insolubles, put the feed liquid into the feed liquid tank of the organic solvent-resistant nanofiltration membrane equipment, turn on the power, the device is running, and the separation process Keep the temperature of the feed liquid at 30-35°C, and the operating pressure is 1.6-2.0MP. The feed liquid circulates on the upstream side of the membrane, and the primary permeate is collected downstream. When the collection volume of the primary permeate is 7L, the equipment is closed; Add 7.5L of a mixed solution of vegetable oi...
Embodiment 2
[0042] This embodiment relates to the removal of harmful components in capsanthin. Compared with Example 1, the difference is that the amount of organic solvent is different, including the following steps:
[0043] Dissolve capsanthin 1000g (color value 145.2, benzopyrene 26ppb, total Sudan red (Sudan Ⅰ-Ⅳ) 200ppb, rhodamine B 65ppb, ethion 36ppm, chlorpyrifos 12ppm, triazophos 21ppm) into vegetable oil for extraction Mixed solution of solvent and acetone (vegetable oil extraction solvent: acetone = 3:2) 20000ml, filter to remove solid insoluble matter, put the feed liquid into the feed liquid tank of the organic solvent-resistant nanofiltration membrane equipment, turn on the power, the device is running, and the separation process Keep the temperature of the feed liquid at 30-35°C, and the operating pressure at 1.6-2.0MPa. The feed liquid circulates on the upstream side of the membrane, and the primary permeate is collected downstream. When the collection volume of the primary...
Embodiment 3
[0046] Compared with Example 1, the difference is that the organic solvent is ethyl acetate.
[0047] The present embodiment relates to the removal of harmful components in capsanthin, comprising the following steps:
[0048] 1) Dissolve capsanthin 1000g (color value 145.2, benzopyrene 26ppb, total Sudan red (Sudan Ⅰ-Ⅳ) 200ppb, rhodamine B 65ppb, ethion 36ppm, chlorpyrifos 12ppm, triazophos 21ppm) into acetic acid Ethyl ester 10000ml, filter to remove solid insoluble matter, put the feed liquid into the feed liquid tank of the organic solvent-resistant nanofiltration membrane equipment, turn on the power, the device runs, keep the feed liquid temperature at 30-35 °C during the separation process, and the operating pressure is 1.6-2.0 MPa. The feed liquid is circulated on the upstream side of the membrane, and the primary permeate is collected downstream. When the collection volume of the primary permeate is 7L, the equipment is turned off; 7.5L of ethyl acetate is added to th...
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