Method for preparing diglyceride through industrial molecular distillation and reducing 3-chloropropanol ester in diglyceride
A technology of diglyceride and molecular distillation, applied in the direction of fermentation, etc., can solve the problems of greatly increasing the ability of producing 3-chloropropanol ester and chloride ion chlorinated glycerol, etc.
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Embodiment 1
[0025] Industrial molecular distillation prepares diglyceride and reduces 3-chloropropanol fat in diglyceride, and it comprises the following steps:
[0026] (1) Bio-enzymatic glycerol hydrolysis of soybean oil to obtain a lipid mixed system rich in diglycerides of 45%-48% (mass percentage), with a continuous and stable flow rate of about 15 liters / hour by the feed pump and metering controller, raw materials After the oil is heated to about 70°C, it enters the gas separator; the absolute pressure of the gas separator is controlled at about 1mbar to completely remove the air that may be carried in the raw oil. The raw material oil after degassing continues to be heated to an operating temperature of about 150°C, and then enters the falling film thin film evaporator. boiling point components. Adjust the temperature of the heat medium to about 245°C, continue to heat the raw material oil to an operating temperature of about 190°C, and the raw material oil enters the wiped-film mol...
Embodiment 2
[0030] Industrial molecular distillation prepares diglyceride and reduces 3-chloropropanol fat in diglyceride, and it comprises the following steps:
[0031] (1) Bio-enzyme glycerolizes palm oil to obtain a lipid mixed system rich in diglycerides of 41%-45% (mass percentage), with a continuous and stable flow rate of about 18 liters / hour by a feeding pump and a metering controller. After the oil is heated to about 75°C, it enters the gas separator; the absolute pressure of the gas separator is controlled at about 1mbar to completely remove the air that may be carried in the raw oil. The raw material oil after degassing continues to be heated to an operating temperature of about 160°C, and enters the falling film thin film evaporator. boiling point components. Adjust the temperature of the heat medium to about 240°C, continue to heat the raw material oil to an operating temperature of about 185°C, and the raw material oil enters the wiped-film molecular still (short-path still...
Embodiment 3
[0035] Industrial molecular distillation prepares diglyceride and reduces 3-chloropropanol fat in diglyceride, and it comprises the following steps:
[0036] (1) Using natural palm oil as raw material, the diglyceride content is 5.8% (mass percentage), the continuous and stable flow rate is about 15 liters / hour by the feeding pump and metering controller, and the raw material oil is heated to about 85°C Then enter the gas separator; control the absolute pressure of the gas separator to operate at about 0.1mbar to completely remove the air that may be carried in the raw material oil. The raw material oil after degassing continues to be heated to an operating temperature of about 150°C, and then enters the falling film thin film evaporator. boiling point components. Adjust the temperature of the heat medium to about 240°C, continue to heat the raw material oil to an operating temperature of about 190°C, and the raw material oil enters the wiped-film molecular still (short-path ...
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