CN113115840A - Low erucic acid and low fatty acid vegetable blend oil and preparation method thereof - Google Patents

Low erucic acid and low fatty acid vegetable blend oil and preparation method thereof Download PDF

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Publication number
CN113115840A
CN113115840A CN202110471942.8A CN202110471942A CN113115840A CN 113115840 A CN113115840 A CN 113115840A CN 202110471942 A CN202110471942 A CN 202110471942A CN 113115840 A CN113115840 A CN 113115840A
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oil
parts
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filter
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李达智
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Yunnan Jinfenghui Grease Co ltd
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Yunnan Jinfenghui Grease Co ltd
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/007Other edible oils or fats, e.g. shortenings, cooking oils characterised by ingredients other than fatty acid triglycerides
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/02Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
    • A23D9/04Working-up
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L27/00Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/10Natural spices, flavouring agents or condiments; Extracts thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/105Plant extracts, their artificial duplicates or their derivatives
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/115Fatty acids or derivatives thereof; Fats or oils
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/15Vitamins
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/001Refining fats or fatty oils by a combination of two or more of the means hereafter
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/008Refining fats or fatty oils by filtration, e.g. including ultra filtration, dialysis
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/02Refining fats or fatty oils by chemical reaction
    • C11B3/06Refining fats or fatty oils by chemical reaction with bases
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/16Refining fats or fatty oils by mechanical means
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

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Abstract

The invention discloses a low erucic acid and low fatty acid vegetable blend oil and a preparation method thereof, wherein the blend oil comprises the following components: 40-50 parts of tea seed oil, 45-60 parts of rice oil, 50-70 parts of peanut oil, 40-55 parts of sesame oil, 30-50 parts of low erucic acid rapeseed oil, 20-30 parts of sunflower oil, 35-45 parts of sunflower oil, 45-60 parts of walnut oil, 30-45 parts of soybean oil, 20-35 parts of castor oil and 30-45 parts of palm oil. The vegetable blend oil is helpful for digestion and reducing body and mental pressure, has a certain antibacterial capacity, can reduce nausea, has a certain seasoning effect, has the advantages of rich nutrient components, good health care and health preserving effects, good antibacterial property, and simple preparation, and is beneficial to human body digestion, and the problems that the conventional vegetable blend oil is single in type, less in nutrient components, incapable of supplementing various nutrient components to human bodies, free of health care and health preserving effects, free of antibacterial property, not beneficial to human body digestion, and complex in preparation process are solved.

Description

Low erucic acid and low fatty acid vegetable blend oil and preparation method thereof
Technical Field
The invention relates to the technical field of vegetable blend oil preparation, in particular to low erucic acid and low fatty acid vegetable blend oil and a preparation method thereof.
Background
The blend oil is edible oil prepared by blending more than two refined oils according to the use requirement, is transparent and can be used as oil for frying, stir-frying, deep-frying or cold mixing, is generally prepared from refined soybean oil, rapeseed oil, peanut oil, sunflower seed oil, cottonseed oil and the like serving as main raw materials, and can also be prepared from refined rice bran oil, corn germ oil, camellia seed oil, safflower seed oil, wheat germ oil and other special oil esters, and the processing process comprises the following steps: selecting above two refined oil esters as required, deacidifying, decolorizing, deodorizing, and blending to obtain blend oil. The quality guarantee period of the blend oil is generally 12 months, and the blend oil only has enterprise standards and no national standards at present. The development prospect of the blend oil is good, and the blend oil becomes one of oil products loved by consumers.
The existing vegetable blend oil has single type and few nutrient components, can not supplement various nutrient components for human bodies, so that the edible oil has no health care and health preserving effect, has no antibacterial property, is not beneficial to human body digestion, and has a complex preparation process, thereby providing the low erucic acid and low fatty acid vegetable blend oil and the preparation method thereof.
Disclosure of Invention
The invention aims to provide low erucic acid and low fatty acid vegetable blend oil and a preparation method thereof, which have the advantages of rich nutrient components, good health care and health preservation effects, good antibacterial property, benefit for human digestion and simple preparation, and solve the problems that the existing vegetable blend oil has single type and few nutrient components, can not supplement various nutrient components for human bodies, so that the edible oil has no health care and health preservation effects, has no antibacterial property, is not beneficial for human digestion and has a complex preparation process.
In order to achieve the purpose, the invention provides the following technical scheme: a low erucic acid, low fatty acid vegetable blend oil comprises the following components: 40-50 parts of tea seed oil, 45-60 parts of rice oil, 50-70 parts of peanut oil, 40-55 parts of sesame oil, 30-50 parts of low erucic acid rapeseed oil, 20-30 parts of sunflower oil, 35-45 parts of sunflower oil, 45-60 parts of walnut oil, 30-45 parts of soybean oil, 20-35 parts of castor oil and 30-45 parts of palm oil.
Preferably, the tea seed oil, rice oil, peanut oil, sesame oil, canola oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil are all prepared in a refining process.
Preferably, the natural vitamin E also comprises 1.5-3.5 parts of natural vitamin E, 0.5-1.5 parts of vitamin B group, 0.2-0.8 part of fennel essential oil and 0.2-0.7 part of clove essential oil.
A preparation method of low erucic acid and low fatty acid vegetable blend oil comprises the following steps:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 20-35 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 20-30min, and cooling to 15-25 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
Preferably, in the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali may be added for hydration degumming, so that the content of free fatty acids in the oil may be reduced, and a small amount of soap base formed may agglomerate the micelle, thereby accelerating the sedimentation rate of the micelle, and in addition, the presence of the soap base may also play a certain role in the adsorption of pigments, and the solubility of phospholipids in oil and fat may be reduced at low temperature.
Preferably, the water content of each raw material in the step C is controlled to be 0.2-0.6%.
Preferably, in the step B, the container is divided into an upper cavity and a lower cavity by the filter medium through the filter medium, the vegetable oil is added into the upper cavity, and enters the lower cavity through the filter medium under the pressure action to form filtrate, and the solid particles are intercepted on the surface of the filter medium to form filter residue.
Preferably, in the filtering process in the step B, the filter residue layer accumulated on the surface of the filter medium is gradually thickened, the resistance of the liquid passing through the filter residue layer is increased, the filtering speed is reduced, and when the filter chamber is filled with the filter residue or the filtering speed is too low, the filtering is stopped, the filter residue is removed, and the filter medium is regenerated to complete one filtering cycle.
Compared with the prior art, the invention has the following beneficial effects:
1. the vegetable blend oil has the advantages of rich nutrient components, good health-care and health-preserving effects, good antibacterial property, contribution to human body digestion and simple preparation, and solves the problems that the conventional vegetable blend oil has single type and few nutrient components, cannot supplement various nutrient components to human bodies, does not have the health-care and health-preserving effects, does not have the antibacterial property, is not beneficial to human body digestion and has a complex preparation process.
2. According to the invention, natural vitamin E and vitamin B are added, so that the plant blend oil has excellent health care and health preserving effects, and the fennel essential oil and the clove essential oil help digestion and reduce physical and mental pressure, and simultaneously have certain antibacterial capacity, can reduce nausea symptoms, and can play a certain seasoning role.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the following embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
A low erucic acid, low fatty acid vegetable blend oil comprises the following components: 40-50 parts of tea seed oil, 45-60 parts of rice oil, 50-70 parts of peanut oil, 40-55 parts of sesame oil, 30-50 parts of low erucic acid rapeseed oil, 20-30 parts of sunflower oil, 35-45 parts of sunflower oil, 45-60 parts of walnut oil, 30-45 parts of soybean oil, 20-35 parts of castor oil and 30-45 parts of palm oil.
Tea seed oil, rice oil, peanut oil, sesame oil, canola oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil are all prepared in a refining process.
Also comprises natural vitamin E1.5-3.5 parts, vitamin B group 0.5-1.5 parts, fennel essential oil 0.2-0.8 part and clove essential oil 0.2-0.7 part.
A preparation method of low erucic acid and low fatty acid vegetable blend oil comprises the following steps:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 20-35 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 20-30min, and cooling to 15-25 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
In the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali can be added for hydration degumming, so that the content of free fatty acid in the oil can be reduced, and a small amount of soap base formed can agglomerate colloid, thereby accelerating the sedimentation speed of the micelle, in addition, the existence of the soap base plays a certain role in the adsorption of pigments, and the solubility of phospholipid in oil can be reduced at low temperature.
In the step C, the water content of each raw material is controlled to be 0.2-0.6%.
And B, separating the container into an upper cavity and a lower cavity by using a filter medium in the filter in the step B, adding the vegetable oil into the upper cavity, allowing the vegetable oil to enter the lower cavity through the filter medium under the action of pressure to form filtrate, and intercepting solid particles on the surface of the filter medium to form filter residues.
And B, gradually thickening the filter residue layer accumulated on the surface of the filter medium in the filtering process, increasing the resistance of the liquid passing through the filter residue layer, reducing the filtering speed, stopping filtering when the filter chamber is full of filter residues or the filtering speed is too low, removing the filter residues, and regenerating the filter medium to finish one filtering cycle.
The first embodiment is as follows:
a low erucic acid, low fatty acid vegetable blend oil comprises the following components: 40 parts of tea seed oil, 45 parts of rice oil, 50 parts of peanut oil, 40 parts of sesame oil, 30 parts of low erucic acid rapeseed oil, 20 parts of sunflower oil, 35 parts of sunflower oil, 45 parts of walnut oil, 30 parts of soybean oil, 20 parts of castor oil and 30 parts of palm oil.
Tea seed oil, rice oil, peanut oil, sesame oil, canola oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil are all prepared in a refining process.
Also comprises 1.5 parts of natural vitamin E, 0.5 part of vitamin B group, 0.2 part of fennel essential oil and 0.2 part of clove essential oil.
A preparation method of low erucic acid and low fatty acid vegetable blend oil comprises the following steps:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 20 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 20min, and cooling to 15 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
In the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali can be added for hydration degumming, so that the content of free fatty acid in the oil can be reduced, and a small amount of soap base formed can agglomerate colloid, thereby accelerating the sedimentation speed of the micelle, in addition, the existence of the soap base plays a certain role in the adsorption of pigments, and the solubility of phospholipid in oil can be reduced at low temperature.
In step C, the water content of each raw material was controlled to 0.2%.
And B, separating the container into an upper cavity and a lower cavity by using a filter medium in the filter in the step B, adding the vegetable oil into the upper cavity, allowing the vegetable oil to enter the lower cavity through the filter medium under the action of pressure to form filtrate, and intercepting solid particles on the surface of the filter medium to form filter residues.
And B, gradually thickening the filter residue layer accumulated on the surface of the filter medium in the filtering process, increasing the resistance of the liquid passing through the filter residue layer, reducing the filtering speed, stopping filtering when the filter chamber is full of filter residues or the filtering speed is too low, removing the filter residues, and regenerating the filter medium to finish one filtering cycle.
Example two:
a low erucic acid, low fatty acid vegetable blend oil comprises the following components: 45 parts of tea seed oil, 50 parts of rice oil, 60 parts of peanut oil, 48 parts of sesame oil, 40 parts of low erucic acid rapeseed oil, 25 parts of sunflower oil, 40 parts of sunflower oil, 50 parts of walnut oil, 33 parts of soybean oil, 30 parts of castor oil and 40 parts of palm oil.
Tea seed oil, rice oil, peanut oil, sesame oil, canola oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil are all prepared in a refining process.
Also comprises 2 parts of natural vitamin E, 1 part of vitamin B group, 0.5 part of fennel essential oil and 0.5 part of clove essential oil.
A preparation method of low erucic acid and low fatty acid vegetable blend oil comprises the following steps:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 30 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 25min, and cooling to 20 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
In the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali can be added for hydration degumming, so that the content of free fatty acid in the oil can be reduced, and a small amount of soap base formed can agglomerate colloid, thereby accelerating the sedimentation speed of the micelle, in addition, the existence of the soap base plays a certain role in the adsorption of pigments, and the solubility of phospholipid in oil can be reduced at low temperature.
In step C, the water content of each raw material was controlled to 0.4%.
And B, separating the container into an upper cavity and a lower cavity by using a filter medium in the filter in the step B, adding the vegetable oil into the upper cavity, allowing the vegetable oil to enter the lower cavity through the filter medium under the action of pressure to form filtrate, and intercepting solid particles on the surface of the filter medium to form filter residues.
And B, gradually thickening the filter residue layer accumulated on the surface of the filter medium in the filtering process, increasing the resistance of the liquid passing through the filter residue layer, reducing the filtering speed, stopping filtering when the filter chamber is full of filter residues or the filtering speed is too low, removing the filter residues, and regenerating the filter medium to finish one filtering cycle.
Example three:
a low erucic acid, low fatty acid vegetable blend oil comprises the following components: 50 parts of tea seed oil, 60 parts of rice oil, 70 parts of peanut oil, 55 parts of sesame oil, 50 parts of low erucic acid rapeseed oil, 30 parts of sunflower oil, 45 parts of sunflower oil, 60 parts of walnut oil, 45 parts of soybean oil, 35 parts of castor oil and 45 parts of palm oil.
Tea seed oil, rice oil, peanut oil, sesame oil, canola oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil are all prepared in a refining process.
Also comprises 3.5 parts of natural vitamin E, 1.5 parts of vitamin B group, 0.8 part of fennel essential oil and 0.7 part of clove essential oil.
A preparation method of low erucic acid and low fatty acid vegetable blend oil comprises the following steps:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 35 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 30min, and cooling to 25 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
In the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali can be added for hydration degumming, so that the content of free fatty acid in the oil can be reduced, and a small amount of soap base formed can agglomerate colloid, thereby accelerating the sedimentation speed of the micelle, in addition, the existence of the soap base plays a certain role in the adsorption of pigments, and the solubility of phospholipid in oil can be reduced at low temperature.
In step C, the water content of each raw material was controlled to 0.6%.
And B, separating the container into an upper cavity and a lower cavity by using a filter medium in the filter in the step B, adding the vegetable oil into the upper cavity, allowing the vegetable oil to enter the lower cavity through the filter medium under the action of pressure to form filtrate, and intercepting solid particles on the surface of the filter medium to form filter residues.
And B, gradually thickening the filter residue layer accumulated on the surface of the filter medium in the filtering process, increasing the resistance of the liquid passing through the filter residue layer, reducing the filtering speed, stopping filtering when the filter chamber is full of filter residues or the filtering speed is too low, removing the filter residues, and regenerating the filter medium to finish one filtering cycle.
In summary, the following steps: the low erucic acid and low fatty acid plant blend oil and the preparation method thereof solve the problems that the existing plant blend oil has single type and few nutrient components, can not supplement various nutrient components for human bodies, causes no health care and health preservation effect, has no antibacterial property, is not beneficial to human body digestion and has complex preparation process.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (8)

1. A low erucic acid and low fatty acid vegetable blend oil is characterized by comprising the following components: 40-50 parts of tea seed oil, 45-60 parts of rice oil, 50-70 parts of peanut oil, 40-55 parts of sesame oil, 30-50 parts of low erucic acid rapeseed oil, 20-30 parts of sunflower oil, 35-45 parts of sunflower oil, 45-60 parts of walnut oil, 30-45 parts of soybean oil, 20-35 parts of castor oil and 30-45 parts of palm oil.
2. The canola, low fatty acid vegetable blend oil of claim 1, wherein: the tea seed oil, the rice oil, the peanut oil, the sesame oil, the low erucic acid rapeseed oil, the sunflower oil, the walnut oil, the soybean oil, the castor oil and the palm oil are all prepared in a refining process.
3. The canola, low fatty acid vegetable blend oil of claim 1, wherein: the composition also comprises 1.5-3.5 parts of natural vitamin E, 0.5-1.5 parts of vitamin B group, 0.2-0.8 part of fennel essential oil and 0.2-0.7 part of clove essential oil.
4. A process for preparing a low erucic acid, low fatty acid vegetable blend oil according to any one of claims 1 to 3, comprising the steps of:
a: introducing the refined tea seed oil, rice oil, peanut oil, sesame oil, low erucic acid rapeseed oil, sunflower oil, walnut oil, soybean oil, castor oil and palm oil into a precipitation tank for precipitation, so that impurities in the vegetable oil are precipitated at the bottom of an inner cavity of the precipitation tank;
b: taking vegetable oil on the upper part of the settling tank, introducing the vegetable oil into a filter for filtering, hermetically connecting an oil outlet of the filter with a food-grade transparent plastic connecting pipeline, connecting the other end of the connecting pipeline with a suspension separator to realize oil fume collection, introducing the oil separated from the bottom of the suspension separator into the oil tank, and purifying the air separated from the top and then returning the air to an air compressor for recycling;
c: b, introducing the vegetable oil prepared in the step B into a stirrer, adding hot water into the oil under the stirring of the stirrer, so that the phospholipid absorbs water, expands and coagulates, the expanded oil can adsorb other colloids in the oil, the solubility of the colloids in the oil is reduced, and the oil is separated from the oil through natural sedimentation;
d: mixing vegetable oil at 20-35 deg.C, adding natural vitamin E, vitamin B group, oleum Foeniculi and flos Caryophylli essential oil respectively, stirring under nitrogen for 20-30min, and cooling to 15-25 deg.C to obtain erucic acid and low fatty acid vegetable blend oil.
5. The method of claim 1, wherein the canola oil is prepared by a process comprising: in the step C, in order to accelerate the sedimentation of the micelle and increase the agglomeration of the micelle, a certain amount of dilute alkali can be added for hydration degumming, so that the content of free fatty acid in the oil can be reduced, a small amount of soap base formed can agglomerate colloid, the sedimentation speed of the micelle is accelerated, in addition, the existence of the soap base has a certain effect on the adsorption of pigment, and the solubility of phospholipid in oil can be reduced at low temperature.
6. The method of claim 1, wherein the canola oil is prepared by a process comprising: and C, controlling the water content of each raw material to be 0.2-0.6%.
7. The method of claim 1, wherein the canola oil is prepared by a process comprising: and B, separating the container into an upper cavity and a lower cavity by using a filter medium in the step B, adding the vegetable oil into the upper cavity, allowing the vegetable oil to enter the lower cavity through the filter medium under the action of pressure to form filtrate, and intercepting solid particles on the surface of the filter medium to form filter residues.
8. The method of claim 1, wherein the canola oil is prepared by a process comprising: and B, gradually thickening the filter residue layer accumulated on the surface of the filter medium in the filtering process in the step B, increasing the resistance of the liquid passing through the filter residue layer, reducing the filtering speed, stopping filtering when the filter chamber is full of filter residues or the filtering speed is too low, removing the filter residues, and regenerating the filter medium to finish one filtering cycle.
CN202110471942.8A 2021-04-29 2021-04-29 Low erucic acid and low fatty acid vegetable blend oil and preparation method thereof Pending CN113115840A (en)

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Application publication date: 20210716