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.

Inactive Publication Date: 2017-10-03
HENAN UNIVERSITY OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chloride ions are not easy to enter the hydrophobic environment of oil by nature, but in the presence of amino acid salts, phosphorus-containing compounds and surface active substances such as monoglycerides and diglycerides, the ability of chloride ions to chlorinate glycerin is greatly enhanced
Since there is a hydroxyl group in the molecular structure of diglycerides, if there are chloride ions in the system during the preparation and processing, the products of diglycerides are more likely to have the risk of producing 3-chloropropanol esters

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention relates to a method for preparing diglyceride through industrial molecular distillation and reducing 3-chloropropanol ester in diglyceride. The method comprises the following main steps: subjecting palm oil, cottonseed oil or vegetable fat to enzymatic glycerolysis so as to obtain diglyceride-rich mixed lipid which is used as a raw material, continuously conveying the raw material to a deaerator via a feed pump and removing air carried by the raw material; heating the degassed raw material to 135 to 160 DEG C, allowing the heated raw material to enter a film evaporator, adjusting the rotating speed of the film evaporator to 150 to 180 r/min and absolute pressure to be 1 mbar or so, and separating out lower-boiling-point components in the raw material; and adjusting the temperature of a heating medium to 230 to 280 DEG C, heating the raw material to 180 to 215 DEG C, uniformly pumping the raw material into a scraped-film type short-path distiller, adjusting the rotating speed of the scraped-film type short-path distiller to 220 to 300 r/min and absolute pressure to be 0.001 to 0.1 mbar or so, and collecting separated light-phase and heavy phase components. In industrial molecular distillation for preparation of a diglyceride product, the flow of the raw material is controlled to be 15 to 25 L/h; and the obtained diglyceride product with purity of 80% or more has to undergo molecular distillation twice.

Description

technical field [0001] The invention belongs to the preparation of diglyceride and the safety of the product in the technical field of functional edible oil production, and specifically relates to the preparation of diglyceride products by industrial molecular distillation and the reduction of 3- methods for potential risk factors such as chloropropanol or glycidyl esters. This method is suitable for the continuous industrial production of high-quality diglyceride products, and removes potential risk factors such as 3-chloropropanol ester or glycidyl ester that may exist in the diglyceride to the limit required by food safety to ensure that the diglyceride All physical and chemical indicators meet the relevant standards, the production method is green and pollution-free, and the process technology is continuous and automatic. Background technique [0002] Due to the continuous improvement of people's quality of life and unhealthy living habits, some rich and noble diseases ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C12P7/64
CPCC12P7/6454
Inventor 马传国司天雷杜蘅李利君马靖轩刘君孙亚辉李婕妤
Owner HENAN UNIVERSITY OF TECHNOLOGY
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