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Low-erucic acid rapeseed oil and production process thereof

A technology of canola oil and production process, which is applied in the field of canola oil and its production process, can solve the problems of loss of nutrients, waste of energy and time, strong polarity of phenolic substances, etc., and achieve retention More, high oil yield, mild condition effect

Inactive Publication Date: 2021-12-17
易恒
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Requires further technical treatment of demulsification, which causes waste of energy and time
At the same time, due to the high content of water in the traditional water enzymatic method, the phenolic substances have strong polarity and are easily soluble in water, resulting in the loss of trace nutrients.

Method used

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  • Low-erucic acid rapeseed oil and production process thereof

Examples

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Effect test

Embodiment 1

[0030] A production process of canola oil, comprising the following steps:

[0031] (1) Clean the rapeseed, remove debris, deflated seeds, and impurities;

[0032] (2) Moisture conditioning is carried out on the rapeseed from which impurities have been removed, so that the moisture content thereof is 0.8wt%;

[0033] (3) Crushing and sieving the rapeseed obtained in the previous step, the mesh number is 50 mesh, and the pressing pressure is 15MPa to obtain primary crude oil;

[0034] (4) Take 0.8% water of primary crude oil weight, 0.15% weight compound enzyme of primary crude oil weight, mix, stir evenly, add to primary crude oil, carry out enzymatic hydrolysis, enzymatic hydrolysis time 11h, temperature 36 ℃ ; Wherein the compound enzyme comprises 0.05% lipase of primary crude oil weight, 0.05% cellulase of primary crude oil weight, 0.05 papain of primary crude oil weight;

[0035] (5) After enzymatic hydrolysis, add petroleum ether for extraction, the amount of petroleum ...

Embodiment 2

[0038] A production process of canola oil, comprising the following steps:

[0039] (1) Clean the rapeseed, remove debris, deflated seeds, and impurities;

[0040] (2) Moisture conditioning is carried out on the rapeseed from which impurities have been removed, so that the moisture content thereof is 1wt%;

[0041] (3) Crushing and sieving the rapeseed obtained in the previous step, the mesh number is 60 mesh, and the pressing pressure is 20MPa to obtain primary crude oil;

[0042] (4) Take 0.1% water of primary crude oil weight and 00.3% weight compound enzyme of primary crude oil weight, mix, stir evenly, add to primary crude oil, carry out enzymatic hydrolysis, enzymatic hydrolysis time 12h, temperature 40℃ ; Wherein the compound enzyme comprises 0.1% lipase of primary crude oil weight, 0.1% cellulase of primary crude oil weight, 0.1% papain of primary crude oil weight;

[0043](5) After enzymatic hydrolysis, add petroleum ether for extraction, the amount of petroleum eth...

Embodiment 3

[0046] A production process of canola oil, comprising the following steps:

[0047] (1) Clean the rapeseed, remove debris, deflated seeds, and impurities;

[0048] (2) Moisture conditioning is carried out on the rapeseed from which impurities have been removed, so that the moisture content thereof is 0.5wt%;

[0049] (3) Crushing and sieving the rapeseed obtained in the previous step, the mesh number is 40 mesh, and the pressing pressure is 10MPa to obtain primary crude oil;

[0050] (4) Take 0.05% water of the primary crude oil weight and 0.09% weight compound enzyme of the primary crude oil weight, mix, stir evenly, add to the primary crude oil, and carry out enzymatic hydrolysis, the enzymatic hydrolysis time is 10h, and the temperature is 35°C ; Wherein composite enzyme comprises 0.03% lipase of primary crude oil weight, 0.03% cellulase of primary crude oil weight, 0.03% papain of primary crude oil weight;

[0051] (5) After enzymatic hydrolysis, add petroleum ether for ...

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PUM

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Abstract

The invention discloses a production process of low-erucic acid rapeseed oil, wherein the production process comprises the following steps: (1) cleaning rapeseeds cleanly, and removing chippings, shriveled seeds and impurities; (2) carrying out moisture regulation on the rapeseeds subjected to impurity removal to enable the moisture content to be 0.5-1 wt%; (3) crushing, sieving and pressing the rapeseeds obtained in the step (2) to obtain primary crude oil; (4) taking water accounting for 0.05-0.1% of the weight of the primary crude oil and compound enzyme accounting for 0.09-0.3% of the weight of the primary crude oil, mixing, uniformly stirring, adding into the primary crude oil, and carrying out enzymolysis; (5) after the enzymolysis is finished, adding petroleum ether for extraction, and separating out a water layer to obtain an oil layer; and (6) after petroleum ether in the oil layer is completely recovered, obtaining rapeseed oil. The rapeseed oil prepared by the method retains more micronutrient active ingredients, and is high in tocopherol, sterol and beta-carotene content and low in erucic acid content.

Description

technical field [0001] The invention belongs to the technical field of rapeseed oil, and in particular relates to a low erucic acid rapeseed oil and a production process thereof. Background technique [0002] Rapeseed is one of the world's important grain and oil crops, accounting for about 25% of the world's total grain and oil production. Since the 1950s, with the development of the oil industry in the world, the production and output of rapeseed have increased significantly. Rapeseed oil is a kind of nutrient-rich oil. The content of unsaturated fatty acids accounts for more than 80%, of which oleic acid is more than 40%. It is easily absorbed by the human body and has good frying and anti-oxidation properties. The content of serum cholesterol in the body can prevent and treat arteriosclerosis, promote microvascular circulation, prevent colon cancer, reduce blood pressure and lose weight, especially beneficial to obesity, high blood pressure, heart disease, arteriosclero...

Claims

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Application Information

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IPC IPC(8): C11B1/04C11B1/06C11B3/00
CPCC11B1/04C11B1/06C11B3/003C11B3/006
Inventor 易恒
Owner 易恒
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