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Continuous reactor for oleic acid ester exchange reaction and purifying method of fatty acid diglyceride

A technology of transesterification reaction and purification method, which is applied in the continuous reactor of oil transesterification reaction and the field of fatty acid diglyceride purification, can solve the problems of small output, low reaction yield, low efficiency and the like, and achieves a high production efficiency. Effect

Pending Publication Date: 2018-12-21
金溪遥遥领先高科有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The current oil transesterification reaction is generally a batch reactor, which has a small output and low efficiency. The inventor once invented a continuous diacylglycerol reactor CN201210191389.3, and a catalyst glycerol solution is added to the upper part of the reactor body. A glycerin heater and a catalyst mixing tank are arranged on the catalyst glycerin solution feeding pipe, and a grease feeding pipe is arranged at the lower part of the reactor body, and the grease feeding pipe is arranged in the reactor body with the nozzle facing down; A grease heater is arranged on the top of the reactor body, and a mixed solution heater is arranged in the inner cavity of the reactor body. Several baffles arranged in a horizontal staggered manner are arranged in the reactor body above the mixed solution heater. There is a reaction product outlet on the top, and an emptying pipe is provided at the bottom of the reactor body; fatty acid diglycerides are separated from the reaction product by multi-stage molecular distillation equipment. When separating, the distillation temperature is 180-260 degrees. Vacuum degree is 0-1000Pa
During the small test of this invention, it was found that its reaction effect was not ideal, the reaction yield was not high, and the multi-stage molecular distillation purification technology was vague, because at that time we had not invented advanced energy-saving molecular distillation equipment without stirring, Therefore, it is necessary to continue to innovate, and now the present invention further improves and innovates on the basis of the original patent (CN201210191389.3)

Method used

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  • Continuous reactor for oleic acid ester exchange reaction and purifying method of fatty acid diglyceride
  • Continuous reactor for oleic acid ester exchange reaction and purifying method of fatty acid diglyceride
  • Continuous reactor for oleic acid ester exchange reaction and purifying method of fatty acid diglyceride

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Embodiment 1

[0035] Such as figure 1 , figure 2 , image 3 , Figure 4 Shown, a kind of continuous reactor of fat transesterification reaction, comprises reactor body 1, is provided with catalyst solution feeding pipe 2 at the top of reactor body 1, and the top of reactor body 1 is provided with reaction product outlet 3, reacts The product outlet 3 extends to the top of the reactor; the bottom of the reactor body 1 is provided with a grease feeding pipe 4, and the grease feeding pipe 4 extends to the bottom of the reactor, and the bottom of the reactor body 1 is provided with an emptying pipe 5. The inner cavity of the reactor body 1 is provided with a mixed solution heater 6 and several reaction discs a and b, the reaction discs a and reaction discs b are alternately placed in the inner cavity of the reactor body, and the adjacent reaction discs A multi-stage reaction chamber 7 is formed between the plate a and the reaction circular plate b.

[0036] In the present invention, the di...

Embodiment 2

[0043] Taking the transesterification reaction of oil and soybean oil and glycerin as an example, the entire continuous reactor equipment is evacuated through the emptying pipe 5 to prevent the oxidation of the materials entered in the previous stage; The solution enters from the catalyst solution feeding pipe 2 at the top of the continuous reactor, passes through multiple reaction discs a and b to reach the heating zone, and at the same time, the oil and soybean oil entering from the oil feeding pipe 4 reacts while heating up, when the temperature rises to 210 degrees , and then add materials from the top catalyst solution feeding pipe 2 and grease feeding pipe 4 at the same time, so that the two materials fill the entire reactor body 1, and the continuous reaction officially starts from then on;

[0044] Add the glycerol solution of the catalyst sodium hydroxide above 160 degrees continuously from the top of the continuous reactor to the catalyst solution into the pipe 2, and...

Embodiment 3

[0046] Carrying out the transesterification reaction to generate diglyceride with embodiment 2 oleander soybean oil and glycerin is example, as Figure 4 As shown, a mixture of free fatty acids of monoglycerides, diesters, and triesters is obtained, which is stored in the raw material storage tank 11 to wait for purification and refining, and is pumped into the first-stage molecular distillation equipment 12 with a material pump, under the conditions of a vacuum degree of 1500-1600pa and a temperature of 100-105 degrees. Under the conditions of vacuum degree 300-400pa, temperature 170-175 degrees, diglyceride oil is removed Residual glycerol in the oil; then enter the third stage molecular distillation equipment 14, under the conditions of vacuum degree 80-130pa and temperature 190-195 degrees, remove the free fatty acid in the diglyceride oil; then enter the fourth stage molecular distillation equipment 15 , at a vacuum of 5-30pa and a temperature of 210-220 degrees, the mono...

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Abstract

The invention relates to a continuous reactor for oleic acid ester exchange reaction. The continuous reactor comprises a reactor body, wherein a catalyst solution adding pipe is arranged at the top part of the reactor body; the upper part of the reactor body is provided with a reaction generation matter outlet; the reaction generation matter outlet extends to the top part of the reactor; a greaseadding pipe is arranged at the lower part of the reactor body, and extends to the bottom part of the reactor; an air exhaust pipe is arranged at the bottom part of the reactor body, and is connected with a vacuum pump; a mixed solution heater and a plurality of reaction circular plates a and reaction circulate plates b are arranged in an inner cavity of the reactor body; the reaction circular plates a and the reaction circular plates b are alternatively arranged in the inner cavity of the reactor body; a multi-stage reaction cavity is formed between the adjacent reaction circular plates a andreaction circular plates b. The purifying method of the fatty acid diglyceride using the continuous reactor for oleic acid ester exchange reaction is characterized in that a molecule distillation purifying technology of distillation equipment comprises five stages of molecule distillation purifying production technology, so as to improve the production efficiency, save energy and decrease energy consumption.

Description

technical field [0001] The invention relates to the fields of oil industry and oil chemical industry, in particular to a continuous reactor for oil transesterification and a method for purifying fatty acid diglyceride. Background technique [0002] Diacylglycerol (DG) is a structural lipid in which one fatty acid in triacylglycerol (TG) is replaced by a hydroxyl group. DG is a trace component of natural vegetable oil and an endogenous intermediate product of fat metabolism in the body. It is a food ingredient generally recognized as safe (GRAS). In recent years, it has been found that dietary DG has the functions of reducing visceral fat, inhibiting weight gain, and lowering blood lipids, so it has received extensive attention. [0003] DG has many advantages such as safety, nutrition, good processing suitability, and high human compatibility. Diacylglycerol is a product obtained by esterifying glycerol (glycerol) with two fatty acids, referred to as diacylglycerol and digl...

Claims

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Application Information

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IPC IPC(8): C11C3/10C11B3/12B01J19/24C07C67/02C07C69/003
CPCB01J19/24B01J19/245C07C67/02C11B3/12C11C3/10C07C69/003Y02P20/10
Inventor 饶雨农饶攀饶燕李贤李抗宋冠雄
Owner 金溪遥遥领先高科有限公司
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