CN113549496A - High-stability grease composition and preparation method thereof - Google Patents

High-stability grease composition and preparation method thereof Download PDF

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CN113549496A
CN113549496A CN202110807782.XA CN202110807782A CN113549496A CN 113549496 A CN113549496 A CN 113549496A CN 202110807782 A CN202110807782 A CN 202110807782A CN 113549496 A CN113549496 A CN 113549496A
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stability
stirring
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oil
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CN113549496B (en
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张健
梁军
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Anhui Laysen Food Co ltd
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    • 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
    • C11B5/00Preserving by using additives, e.g. anti-oxidants
    • 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
    • C11B5/00Preserving by using additives, e.g. anti-oxidants
    • C11B5/0092Mixtures
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/90Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation

Abstract

The invention relates to a high-stability grease composition and a preparation method thereof, belonging to the technical field of food processing, wherein the composition comprises the following raw materials: modified starch, deionized water, sodium caseinate, a grease component, monoglyceride, sucrose ester and an additive; the preparation method of the composition comprises the following steps: firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase; secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 10-20min to obtain an oil phase; and thirdly, mixing the water phase and the oil phase, shearing at a high speed by 5min, adding an additive, homogenizing, and feeding the homogenized emulsion into a spray drying tower for spray drying to obtain the high-stability oil composition. The high-stability grease component prepared by the invention has good shelf life stability, good embedding performance and long product shelf life.

Description

High-stability grease composition and preparation method thereof
Technical Field
The invention belongs to the technical field of food processing, and particularly relates to a high-stability grease composition and a preparation method thereof.
Background
In recent years, people have increasingly demanded more and more instant coffee and milk tea, and the production and sale of non-dairy creamer (liquid or solid) which is a main raw material matched with the instant coffee and milk tea are continuously increased, and the instant coffee and milk tea mainly appears in tea restaurants, coffee shops and terminal retail products, namely, consumers can consume the instant coffee and milk tea products at the first time, so that the instant coffee and milk tea products have no quality guarantee period problem in a liquid state. The instant coffee and milk tea exist in a liquid state, the packaging forms mainly comprise PET, tetra Pak and iron cans, the shelf life is 9-12 months, more fat floats upwards usually in the shelf life, the product quality is seriously influenced, the product mainly comprises tea, coffee, milk or whole milk powder, the fat floats upwards through the control of an emulsifier and a colloid, and a certain effect is achieved, but the milk fat is a very complex grease system, and the change of the emulsification state of the grease is large, so that great difficulty is brought to process control.
The emulsified oil takes hydrogenated vegetable oil with higher purity as an emulsifying object, and a fat product with higher emulsifying stability can be obtained through a proper emulsifying formula and an efficient emulsifying process, but the stability of the emulsified oil in the current market cannot meet the requirement of a ready-to-drink liquid product, the emulsified oil with high stability can completely replace milk fat, the process requirement of the ready-to-drink milk tea and coffee can be met, the shelf life stability of the product is improved, and more choices can be made in flavor to have excellent shelf life.
Disclosure of Invention
The invention aims to provide a high-stability grease composition and a preparation method thereof.
The purpose of the invention can be realized by the following technical scheme:
a high-stability grease composition comprises the following raw materials in parts by weight:
50-90 parts of modified starch, 50-80 parts of deionized water, 1-10 parts of sodium caseinate, 40-80 parts of grease component, 0.5-3 parts of monoglyceride, 0.6-2 parts of sucrose ester and 10-15 parts of additive;
further, the modified starch is prepared by the following steps:
step S11, mixing sodium hydroxide, ferulic acid and deionized water, then adding acetic anhydride, stirring and reacting for 1h at the temperature of 20 ℃ after the addition is finished, adjusting the pH value to 2 by using concentrated hydrochloric acid with the mass fraction of 37%, then standing for 30min, performing reduced pressure suction filtration, and washing a filter cake with the deionized water to obtain an intermediate 1; wherein the dosage ratio of the sodium hydroxide, the ferulic acid, the deionized water and the acetic anhydride is 2.5 g: 3.8 g: 20mL of: 2.4 mL;
the reaction process is as follows:
Figure BDA0003167214900000021
step S12, mixing the intermediate 1, thionyl chloride and chloroform, adding N, N-dimethylformamide, heating to 55 ℃, stirring for reacting for 8 hours, cooling to room temperature after the reaction is finished, and removing the solvent through reduced pressure concentration to obtain an intermediate 2; wherein the dosage ratio of the intermediate 1, thionyl chloride, chloroform and N, N-dimethylformamide is 2.9 g: 2mL of: 20mL of: 20 mg;
the reaction process is as follows:
Figure BDA0003167214900000022
step S13, drying corn starch to constant weight at 60 ℃, mixing the dried corn starch with pyridine, carrying out reflux stirring for 1-2h at 110 ℃, then cooling to 0 ℃, adding the intermediate 2, carrying out reflux stirring for 4-6h at 95 ℃ after the addition is finished, washing with absolute ethyl alcohol and distilled water in sequence after the reaction is finished, then putting the product into a Soxhlet extractor, extracting for 8h with acetone, and carrying out vacuum drying for 24h to obtain a solid a; wherein the dosage ratio of the corn starch, the pyridine and the intermediate 2 is 5 g: 60mL of: 6-10 g;
and step S14, treating the solid a to obtain modified starch.
Further, the specific steps of the processing in step S14 are as follows:
mixing the solid a with distilled water, adding sodium hydroxide to adjust the pH value to 9, heating to 30 ℃, stirring to react for 50-60min, then dropwise adding an auxiliary agent, adding a sodium hydroxide solution with the mass fraction of 3% in the dropwise adding process to maintain the pH value of the system to be about 8.5, reacting for 4h, after the reaction is finished, adjusting the pH value to 6 by using a hydrochloric acid solution with the mass fraction of 3%, then sequentially washing by using distilled water and absolute ethyl alcohol until chloride ions cannot be detected in a washing solution, and after the washing is finished, drying to constant weight at the temperature of 45 ℃.
Further, the using ratio of the solid a to the distilled water to the auxiliary agent is 10 g: 20mL of: 31-32 mL.
Further, the additive is a filler and an antioxidant, and the mass ratio of the filler to the antioxidant is 100: 2-3.
Further, the filler is one or two of glucose and sucrose mixed according to any proportion, and the antioxidant is one or more of vitamin E, ascorbyl palmitate and tea polyphenol mixed according to any proportion.
Further, the oil component is one of coconut oil and walnut oil.
Further, the auxiliary agent is octenyl succinic anhydride and isopropanol according to the dosage ratio of 1 g: 10mL of the above-mentioned components were mixed.
A preparation method of a high-stability grease composition comprises the following steps:
firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase;
secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 10-20min to obtain an oil phase;
and thirdly, mixing the water phase and the oil phase, shearing at a high speed for 5min under the condition that the rotating speed is 10000r/min, adding an additive, homogenizing, and feeding the homogenized emulsion into a spray drying tower for spray drying to obtain the high-stability grease composition.
Further, homogenizing at 70-80 deg.C under 15-20 MPa; the air inlet temperature is 190 ℃ and the feeding temperature is 60 ℃ during spray drying.
The invention has the beneficial effects that:
in the process of preparing the grease composition, modified starch is prepared, wherein corn starch is used as a matrix, ferulic acid is used as a raw material, acetic anhydride is used for protecting hydroxyl on a molecular structure of the ferulic acid, acyl chloride is introduced to prepare an intermediate 2, the intermediate 2 and the starch undergo a grafting reaction, the ferulic acid is introduced to the starch, the oxidation resistance of the starch is improved, lipid peroxy free radicals are eliminated, the lipid peroxidation process is stopped or delayed, a solid a is prepared, deacetylation protection is carried out under an alkaline condition, and meanwhile, the starch and octenyl succinic anhydride undergo an esterification reaction under the alkaline condition, so that the modified starch is prepared. The high-stability grease composition provided by the invention provides an emulsified grease with high stability, and avoids fat floating in the shelf life, so that the shelf life stability of the product is improved; in addition, the embedding performance is good, the shelf life of the product is long, and the stability is good.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the 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.
Example 1
Preparing modified starch:
step S11, mixing sodium hydroxide, ferulic acid and deionized water, then adding acetic anhydride, stirring and reacting for 1h at the temperature of 20 ℃ after the addition is finished, adjusting the pH value to 2 by using concentrated hydrochloric acid with the mass fraction of 37%, then standing for 30min, performing reduced pressure suction filtration, and washing a filter cake with the deionized water to obtain an intermediate 1; wherein the dosage ratio of the sodium hydroxide, the ferulic acid, the deionized water and the acetic anhydride is 2.5 g: 3.8 g: 20mL of: 2.4 mL;
step S12, mixing the intermediate 1, thionyl chloride and chloroform, adding N, N-dimethylformamide, heating to 55 ℃, stirring for reacting for 8 hours, cooling to room temperature after the reaction is finished, and removing the solvent through reduced pressure concentration to obtain an intermediate 2; wherein the dosage ratio of the intermediate 1, thionyl chloride, chloroform and N, N-dimethylformamide is 2.9 g: 2mL of: 20mL of: 20 mg;
step S13, drying corn starch to constant weight at 60 ℃, mixing the dried corn starch with pyridine, refluxing and stirring for 1h at 110 ℃, then cooling to 0 ℃, adding the intermediate 2, refluxing and stirring for 4h at 95 ℃ after the addition is finished, washing with absolute ethyl alcohol and distilled water in sequence after the reaction is finished, then putting the product into a Soxhlet extractor, extracting for 8h with acetone, and then drying in vacuum for 24h to obtain a solid a; wherein the dosage ratio of the corn starch, the pyridine and the intermediate 2 is 5 g: 60mL of: 6g of a mixture;
and step S14, mixing the solid a with distilled water, adding sodium hydroxide to adjust the pH value to 9, heating to 30 ℃, stirring to react for 50min, then dropwise adding an auxiliary agent, adding a sodium hydroxide solution with the mass fraction of 3% in the dropwise adding process to maintain the pH value of the system to be about 8.5, reacting for 4h, after the reaction is finished, adjusting the pH value to 6 by using a hydrochloric acid solution with the mass fraction of 3%, then washing by using distilled water and absolute ethyl alcohol in sequence, and after the washing is finished, drying to constant weight at the temperature of 45 ℃. Wherein the dosage ratio of the solid a to the distilled water to the auxiliary agent is 10 g: 20mL of: 31 mL. The auxiliary agent is octenyl succinic anhydride and isopropanol according to the dosage ratio of 1 g: 10mL of the above-mentioned components were mixed.
Example 2
Preparing modified starch:
step S11, mixing sodium hydroxide, ferulic acid and deionized water, then adding acetic anhydride, stirring and reacting for 1h at the temperature of 20 ℃ after the addition is finished, adjusting the pH value to 2 by using concentrated hydrochloric acid with the mass fraction of 37%, then standing for 30min, performing reduced pressure suction filtration, and washing a filter cake with the deionized water to obtain an intermediate 1; wherein the dosage ratio of the sodium hydroxide, the ferulic acid, the deionized water and the acetic anhydride is 2.5 g: 3.8 g: 20mL of: 2.4 mL;
step S12, mixing the intermediate 1, thionyl chloride and chloroform, adding N, N-dimethylformamide, heating to 55 ℃, stirring for reacting for 8 hours, cooling to room temperature after the reaction is finished, and removing the solvent through reduced pressure concentration to obtain an intermediate 2; wherein the dosage ratio of the intermediate 1, thionyl chloride, chloroform and N, N-dimethylformamide is 2.9 g: 2mL of: 20mL of: 20 mg;
step S13, drying corn starch to constant weight at 60 ℃, mixing the dried corn starch with pyridine, refluxing and stirring for 2 hours at 110 ℃, then cooling to 0 ℃, adding the intermediate 2, refluxing and stirring for 6 hours at 95 ℃ after the addition is finished, washing with absolute ethyl alcohol and distilled water in sequence after the reaction is finished, then putting the product into a Soxhlet extractor, extracting for 8 hours with acetone, and then drying for 24 hours in vacuum to obtain a solid a; wherein the dosage ratio of the corn starch, the pyridine and the intermediate 2 is 5 g: 60mL of: 10g of a mixture;
and step S14, mixing the solid a with distilled water, adding sodium hydroxide to adjust the pH value to 9, heating to 30 ℃, stirring to react for 60min, then dropwise adding an auxiliary agent, adding a sodium hydroxide solution with the mass fraction of 3% in the dropwise adding process to maintain the pH value of the system to be about 8.5, reacting for 4h, after the reaction is finished, adjusting the pH value to 6 by using a hydrochloric acid solution with the mass fraction of 3%, then washing by using distilled water and absolute ethyl alcohol in sequence, and after the washing is finished, drying to constant weight at the temperature of 45 ℃. Wherein the dosage ratio of the solid a to the distilled water to the auxiliary agent is 10 g: 20mL of: 32 mL. The auxiliary agent is octenyl succinic anhydride and isopropanol according to the dosage ratio of 1 g: 10mL of the above-mentioned components were mixed.
Example 3
Preparing a high-stability grease composition:
firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase;
secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 10min to obtain an oil phase;
thirdly, mixing the water phase and the oil phase, shearing at a high speed for 5min under the condition that the rotating speed is 10000r/min, adding an additive, and then homogenizing at the temperature of 70 ℃ and the pressure of 15 MPa; and (3) feeding the homogenized emulsion into a spray drying tower for spray drying, wherein the air inlet temperature is 190 ℃ and the feeding temperature is 60 ℃ during spray drying, so as to obtain the high-stability grease composition.
Wherein the weight parts of the substances are 50 parts of modified starch, 50 parts of deionized water, 1 part of sodium caseinate, 40 parts of grease component, 0.5 part of monoglyceride, 0.6 part of sucrose ester and 10 parts of additive;
wherein, the modified starch is prepared by the method of example 2; the additive is a filler and an antioxidant, and the dosage mass ratio of the filler to the antioxidant is 100: 2; the filler is glucose, and the antioxidant is vitamin E; the oil component is coconut oil.
Example 4
Preparing a high-stability grease composition:
firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase;
secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 15min to obtain an oil phase;
thirdly, mixing the water phase and the oil phase, shearing at a high speed for 5min under the condition that the rotating speed is 10000r/min, adding an additive, and then homogenizing at 75 ℃ under the pressure of 18 MPa; and (3) feeding the homogenized emulsion into a spray drying tower for spray drying, wherein the air inlet temperature is 190 ℃ and the feeding temperature is 60 ℃ during spray drying, so as to obtain the high-stability grease composition.
Wherein the weight parts of the substances are 70 parts of modified starch, 80 parts of deionized water, 5 parts of sodium caseinate, 60 parts of grease component, 2 parts of monoglyceride, 1 part of sucrose ester and 12 parts of additive;
wherein, the modified starch is prepared by the method of example 2; the additive is a filler and an antioxidant, and the dosage mass ratio of the filler to the antioxidant is 100: 2.5; the bulking agent is glucose, antioxidant ascorbyl palmitate; the oil component is coconut oil.
Example 5
Preparing a high-stability grease composition:
firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase;
secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 20min to obtain an oil phase;
thirdly, mixing the water phase and the oil phase, shearing at a high speed for 5min under the condition that the rotating speed is 10000r/min, adding an additive, and then homogenizing at the temperature of 80 ℃ and the pressure of 20 MPa; and (3) feeding the homogenized emulsion into a spray drying tower for spray drying, wherein the air inlet temperature is 190 ℃ and the feeding temperature is 60 ℃ during spray drying, so as to obtain the high-stability grease composition.
Wherein the weight parts of the substances are 90 parts of modified starch, 80 parts of deionized water, 10 parts of sodium caseinate, 80 parts of grease component, 3 parts of monoglyceride, 2 parts of sucrose ester and 15 parts of additive;
wherein, the modified starch is prepared by the method of example 2; the additive is a filler and an antioxidant, and the dosage mass ratio of the filler to the antioxidant is 100: 3; the filler is sucrose, and the antioxidant is tea polyphenol; the oil component is walnut oil.
Comparative example 1
The modified starch from example 4 was replaced by starch octenylsuccinate, and the remaining raw materials and preparation process were kept unchanged.
Comparative example 2
The modified starch of example 4 was replaced by corn starch, and the remaining raw materials and preparation process remained unchanged.
The samples prepared in examples 3-5 and comparative examples 1-2 were tested by mixing 40g of the sample with 200mL of hot water at 80 ℃, then adding citric acid with a mass fraction of 20% dropwise, adjusting the pH to 3 and observing the condition of the emulsion;
the results are shown in table 1 below:
TABLE 1
Emulsion character
Example 3 Uniform and fine liquid, no conjunctival layering and no particle wall hanging
Example 4 Uniform and fine liquid, no conjunctival layering and no particle wall hanging
Example 5 Uniform and fine liquid, no conjunctival layering and no particle wall hanging
Comparative example 1 Even and fine liquid, slight layering, no particle wall hanging
Comparative example 2 Serious layering phenomenon, serious particle wall hanging and oil precipitation phenomenon on the surface
The acid value and peroxide value of the samples prepared in example 4 and comparative example 1 were measured, and the results of the measurement test with reference to GB5009.229-2016 and GB5009.227-2016, respectively, are shown in Table 2 below:
the test results are shown in table 2 below:
TABLE 2
Example 4 Comparative example 1
Acid value (KOH)/(mg/g) 0.35 0.78
Peroxide number/(mmol/kg) 0.19 0.97
The high-stability grease composition prepared by the invention has better acid resistance and is more stable.
In the description herein, references to the description of "one embodiment," "an example," "a specific example" or the like are intended to mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The foregoing is illustrative and explanatory only and is not intended to be exhaustive or to limit the invention to the precise embodiments described, and various modifications, additions, and substitutions may be made by those skilled in the art without departing from the scope of the invention or exceeding the scope of the claims.

Claims (9)

1. A high-stability grease composition comprises the following raw materials in parts by weight:
50-90 parts of modified starch, 50-80 parts of deionized water, 1-10 parts of sodium caseinate, 40-80 parts of grease component, 0.5-3 parts of monoglyceride, 0.6-2 parts of sucrose ester and 10-15 parts of additive; the method is characterized in that the modified starch is prepared by the following steps:
step S11, mixing sodium hydroxide, ferulic acid and deionized water, then adding acetic anhydride, and after the addition is finished, stirring and reacting for 1h at the temperature of 20 ℃ to obtain an intermediate 1;
step S12, mixing the intermediate 1, thionyl chloride and chloroform, adding N, N-dimethylformamide, heating to 55 ℃, and stirring for reacting for 8 hours to obtain an intermediate 2;
step S13, drying corn starch to constant weight at 60 ℃, mixing the dried corn starch with pyridine, refluxing and stirring for 1-2h at 110 ℃, then cooling to 0 ℃, adding the intermediate 2, and refluxing and stirring for 4-6h at 95 ℃ after the addition is finished to obtain a solid a;
and step S14, treating the solid a to obtain modified starch.
2. The high-stability fat composition according to claim 1, wherein the specific steps of the treatment in step S14 are as follows:
mixing the solid a with distilled water, adding sodium hydroxide to adjust the pH value to 9, heating to 30 ℃, stirring to react for 50-60min, then dropwise adding an auxiliary agent to react for 4h, adjusting the pH value to 6 by using a hydrochloric acid solution with the mass fraction of 3% after the reaction is finished, then sequentially washing by using distilled water and absolute ethyl alcohol, and drying to constant weight at the temperature of 45 ℃ after the washing is finished.
3. The high-stability grease composition according to claim 2, wherein the ratio of the solid a to the distilled water to the auxiliary agent is 10 g: 20mL of: 31-32 mL.
4. The high-stability grease composition according to claim 2, wherein the auxiliary agent is octenyl succinic anhydride and isopropanol in a ratio of 1 g: 10mL of the above-mentioned components were mixed.
5. The high-stability grease composition according to claim 1, wherein the additives are a filler and an antioxidant, and the mass ratio of the filler to the antioxidant is 100: 2-3.
6. The high-stability fat composition according to claim 5, wherein the filler is one or two of glucose and sucrose mixed at any ratio, and the antioxidant is one or more of vitamin E, ascorbyl palmitate, and tea polyphenol mixed at any ratio.
7. The high stability fat composition according to claim 1, wherein the fat component is one of coconut oil and walnut oil.
8. The method for preparing the high-stability grease composition according to claim 1, characterized by comprising the following steps:
firstly, mixing modified starch and deionized water, heating to 60 ℃, adding sodium caseinate, and stirring for 3min to obtain a water phase;
secondly, heating the oil component to 70 ℃, adding monoglyceride and sucrose ester, and stirring for 10-20min to obtain an oil phase;
and thirdly, mixing the water phase and the oil phase, shearing at a high speed for 5min under the condition that the rotating speed is 10000r/min, adding an additive, homogenizing, and carrying out spray drying on the homogenized emulsion to obtain the high-stability oil composition.
9. The method for preparing a high-stability fat composition according to claim 8, wherein the homogenizing conditions are a temperature of 70-80 ℃ and a pressure of 15-20 MPa; the air inlet temperature is 190 ℃ and the feeding temperature is 60 ℃ during spray drying.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104054849A (en) * 2014-05-21 2014-09-24 上海英莱腾医药研究有限公司 High-content medium chain triglyceride powdered oil and preparation method thereof
CN104277127A (en) * 2013-07-10 2015-01-14 江苏宝宝宿迁国民生物科技有限公司 Preparation method for oxidized esterified rice starch

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104277127A (en) * 2013-07-10 2015-01-14 江苏宝宝宿迁国民生物科技有限公司 Preparation method for oxidized esterified rice starch
CN104054849A (en) * 2014-05-21 2014-09-24 上海英莱腾医药研究有限公司 High-content medium chain triglyceride powdered oil and preparation method thereof

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