Method for preparing aroma rapeseed oil by adopting micro-channel reactor

A micro-channel reactor, rapeseed oil technology, which is applied in the production of fat oil/fat, fat production, etc., can solve the problems of preparation technology and research of rapeseed oil that have not yet been seen, so as to reduce the production of bad flavor substances and improve the efficiency. , the effect of shortening the enzymatic hydrolysis reaction time

Inactive Publication Date: 2017-07-21
ENZYMECODE BIOTECHNOLOGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

So far, there has been no research on the preparation process of aromatic rapeseed oil in the form of continuous flow in microchannel reactors

Method used

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  • Method for preparing aroma rapeseed oil by adopting micro-channel reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0070] Example 1: Preparation of aromatic rapeseed oil using a microchannel reactor.

[0071] (1) Device: The microchannel device adopts a self-made high-pressure microchannel reactor. The length of the microchannel is determined according to the flow rate and the reaction residence time. The length of each module channel used here is 10m, the pipe diameter is 0.1mm, and the heat exchange medium is heat transfer oil. .

[0072] (2) Preparation of strong sesame rapeseed oil:

[0073] A- Preparation of the Microchannel Reactor:

[0074]The residence time of the reaction system in each module is controlled by adjusting the flow rate of the delivery pump and the channel length of the microchannel, wherein the residence time in the first mixing module 1 is 30 seconds, the residence time in the reaction module 2 is 30 seconds, and the first high temperature module The residence time in 3 is 30 seconds, the residence time in the second mixing module 4 is 30 seconds, the residence t...

Embodiment 2

[0082] Example 2: Preparation of aromatic rapeseed oil using a microchannel reactor.

[0083] (1) Device: The microchannel device adopts a self-made high-pressure microchannel reactor. The length of the microchannel is determined according to the flow rate and the reaction residence time. The length of each module channel used here is 10m, the pipe diameter is 0.15mm, and the heat exchange medium is heat transfer oil. .

[0084] (2) Preparation of strong sesame rapeseed oil:

[0085] A- Preparation of the Microchannel Reactor:

[0086] The residence time of the reaction system in each module is controlled by adjusting the flow rate of the delivery pump and the channel length of the microchannel. The residence time in the first mixing module 1 is 300 seconds, the residence time in the reaction module 2 is 1200 seconds, and the first high temperature module The residence time in 3 is 300 seconds, the residence time in the second mixing module 4 is 1200 seconds, the residence t...

Embodiment 3

[0094] Example 3: Preparation of aromatic rapeseed oil using a microchannel reactor.

[0095] (1) Device: The microchannel device adopts a self-made high-pressure microchannel reactor. The length of the microchannel is determined according to the flow rate and the reaction residence time. The length of each module channel used here is 10m, the pipe diameter is 0.1mm, and the heat exchange medium is heat transfer oil. .

[0096] (2) Preparation of strong sesame rapeseed oil:

[0097] A- Preparation of the Microchannel Reactor:

[0098] The residence time of the reaction system in each module is controlled by adjusting the flow rate of the delivery pump and the channel length of the microchannel, wherein the residence time in the first mixing module 1 is 100 seconds, the residence time in the reaction module 2 is 300 seconds, and the first high temperature module The residence time in 3 is 200 seconds, the residence time in the second mixing module 4 is 500 seconds, the reside...

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Abstract

The invention relates to a method for preparing aroma rapeseed oil by adopting a micro-channel reactor. The method comprises the following steps: step one, pumping a rapeseed enzymatic hydrolysis solution and an enzyme solution into the micro-channel reactor, mixing in a first mixing module and then entering into a reaction module to carry out enzymatic hydrolysis; step two, carrying out high-temperature enzymatic activity passivation, and ending the enzymatic hydrolysis; step three, sufficiently mixing a reaction system with reducing sugar and rapeseed oil so as to obtain a mixed reaction system; step four, the mixed reaction system entering into a second high temperature module, quickly raising the temperature to a technological requirement temperature, and carrying out a Maillard heat reaction; and step five, the reaction system flowing to a low temperature module, and flowing out of the micro-channel reactor to obtain a rapeseed oil crude product. According to the method, the enzymatic hydrolysis process can be accurately controlled, the heat reaction temperature and aftertreatment temperature can be quickly and accurately controlled; and by using an unamplifying effect of the micro-channel reactor, the method is easy for upgrading amplification, and can realize seamless amplification from research and development to production.

Description

technical field [0001] The invention belongs to the technical field of food, and in particular relates to a method for preparing fragrant rapeseed oil in a microchannel reactor. Background technique [0002] Rapeseed oil is one of the main edible oils in my country. It is rich in unsaturated fatty acids and has high nutritional value. Rapeseed is the most important oil crop in China, mainly produced in the Yangtze River Basin, southwest, northwest and other regions. China's rapeseed planting area and total output ranks first in the world, accounting for about 30% of the world's rapeseed planting area and total output [Dong Jiabao, Zhang Changgui, Wang Zhenxu. Research and Application of Edible Rapeseed Protein [J]. Grain and Oil, 2005, (12 ): 11-13]. [0003] The aroma substances of strong-flavor rapeseed oil are mainly produced by the Maillard reaction of amino acids and reducing sugars in rapeseed during the heating process, mainly including some aldo-ketoacids, sulfur-c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C11B1/00C11B1/04
CPCC11B1/00C11B1/04
Inventor 袁永红郭旭杨贺
Owner ENZYMECODE BIOTECHNOLOGY CO LTD
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