CN106189271A - A kind of preparation method of edible eco-friendly emulsion film material - Google Patents

A kind of preparation method of edible eco-friendly emulsion film material Download PDF

Info

Publication number
CN106189271A
CN106189271A CN201610641096.9A CN201610641096A CN106189271A CN 106189271 A CN106189271 A CN 106189271A CN 201610641096 A CN201610641096 A CN 201610641096A CN 106189271 A CN106189271 A CN 106189271A
Authority
CN
China
Prior art keywords
edible
eco
sodium caseinate
film material
emulsion film
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201610641096.9A
Other languages
Chinese (zh)
Other versions
CN106189271B (en
Inventor
尹艳
尹寿伟
彭永宏
王国莉
吕镇城
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
South China University of Technology SCUT
Huizhou University
Original Assignee
South China University of Technology SCUT
Huizhou University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by South China University of Technology SCUT, Huizhou University filed Critical South China University of Technology SCUT
Priority to CN201610641096.9A priority Critical patent/CN106189271B/en
Publication of CN106189271A publication Critical patent/CN106189271A/en
Application granted granted Critical
Publication of CN106189271B publication Critical patent/CN106189271B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L89/00Compositions of proteins; Compositions of derivatives thereof
    • C08L89/005Casein
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2389/00Characterised by the use of proteins; Derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2491/00Characterised by the use of oils, fats or waxes; Derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/06Biodegradable
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/14Gas barrier composition
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/16Applications used for films

Abstract

The present invention relates to packaging material for food field, particularly to the preparation method of a kind of eco-friendly packaging material for food.The method by step is: S1. sodium caseinate is prepared as aqueous solution, fully after aquation, adding and be equivalent to the glycerol of sodium caseinate quality 10 40% and be equivalent to the oil phase of sodium caseinate quality 5 30%, described oil phase is mixed with ethyl acetate by edible fats;S2. the pre-homogenizing of material high speed dispersor S1 obtained;Then high pressure microjet nanometer homogenizer is used to carry out second homogenate;S3. the material rotary evaporation obtained by S2, removes ethyl acetate, is dried to obtain edible eco-friendly emulsion film material.Membrane material safety edible use prepared by the present invention, and there is stronger water vapor rejection performance and mechanical performance, it is with a wide range of applications in packaging material for food.

Description

A kind of preparation method of edible eco-friendly emulsion film material
Technical field
The present invention relates to packaging material for food field, particularly to the preparation side of a kind of eco-friendly packaging material for food Method.
Background technology
In today that white pollution is the most serious, while plastic package material offers convenience to our life, also carry Carry out environmental problem seriously, built biodegradable packaging material for food and be increasingly becoming hot issue.Edible film refers to With natural biological macromole such as protein, lipid and polysaccharide as film forming matrix, formed by intermolecular interaction have many The thin film of pore network structure, is the favorable substitutes of plastic sheeting, is with a wide range of applications in packaging material for food.
Compared with commercial plastic packaging, the water preventing ability of albuminous membranae material is poor.Add in albuminous membranae material and dredge The lipid of water can significantly improve the hydrophobicity of membrane material, improves micro structure and the surface wettability of membrane material, improves block-water performance And mechanical performance.
High pressure microjet is a kind of eco-friendly Physical Processing means.The inside of high pressure microjet is by narrow zigzag Cavity is constituted, and under high-pressure situations, swiftly flowing biological macromolecule solns constantly collides cavity, simultaneously by high speed shear, The mechanical force such as high frequency oscillation, void effect and convection current shock.Compared with high pressure homogenizer, high pressure microjet has higher Energy, it is possible to reach more preferable homogenizing effect.
Summary of the invention
Present invention aims to the albuminous membranae mechanical property of materials and barrier property is poor, conventional high rate homogeneous dispersion The emulsion film material structure of preparation is unstable, the shortcoming of bad mechanical property, it is provided that a kind of novel edible biodegradable The preparation method of emulsion film material.The method selects the sodium caseinate with good effects and mouthfeel as the base of membrane material Matter, adding Semen Maydis oil is the water vapor rejection factor, uses high pressure microjet nanometer homogenizing and solvent evaporated method to obtain nanoscale Emulsion, prepares and has stronger water vapor rejection performance and the membrane material of mechanical performance.Compared with prior art, high pressure microjet and molten Emulsion film material prepared by agent evaporation has obvious advantage and broader practice prospect.
The purpose of the present invention is achieved by the following technical programs:
A kind of preparation method of edible eco-friendly emulsion film material, step is:
S1. sodium caseinate is prepared as aqueous solution, after abundant aquation, adds the glycerol being equivalent to sodium caseinate quality 10-40% Be equivalent to the oil phase of sodium caseinate quality 5-30%, described oil phase is mixed with ethyl acetate by edible fats;Its In, glycerol is for improving the ductility of film, if without glycerol, the film of formation is the most crisp, fragile;
S2. the material high speed dispersor pre-homogenizing 2-5min, rotating speed 2000-6000rpm S1 obtained;Then high pressure is used Microjet nanometer homogenizer carries out second homogenate, and condition is 5000-12000psi, circulates 1-3 time;
S3. the material rotary evaporation obtained by S2, removes ethyl acetate, is dried to obtain edible eco-friendly emulsion film Material.
Further, in described caseinic acid sodium water solution, the mass percent concentration of sodium caseinate is 3 ~ 7%.
Further, in described oil phase, the mass ratio of edible fats and ethyl acetate is (1 ~ 5): (1 ~ 5).
Further, described edible fats is preferably Semen Maydis oil.The oil droplet of Semen Maydis oil has the effect of a toe-in Power, can make droplet size less, be more evenly distributed, and last membrane structure is the finest and close.
Further, rotary evaporation described in S3 is rotary evaporation 20min under the conditions of 50 DEG C.
Further, being dried described in S3 is to be placed in climatic chamber by material, and the temperature of climatic chamber is 20-40 DEG C, relative humidity is 50 ± 5%.
Preferably, the preparation method of a kind of edible eco-friendly emulsion film material, step is:
S1. sodium caseinate is prepared as the aqueous solution that mass percent concentration is 5%, after abundant aquation, adds and is equivalent to casein The glycerol of acid sodium quality 30% and be equivalent to the oil phase of sodium caseinate quality 30%, described oil phase by Semen Maydis oil and ethyl acetate with The mass ratio of 2:1 mixes;
S2. the material high speed dispersor pre-homogenizing 2-5min, rotating speed 2000-6000rpm S1 obtained;Then high pressure is used Microjet nanometer homogenizer carries out second homogenate, and condition is 5000-12000psi, circulates 1-3 time;
S3. the material rotary evaporation obtained by S2, removes ethyl acetate, is dried to obtain edible eco-friendly emulsion film Material.
There is advantages that
The present invention selects the sodium caseinate with good effects and mouthfeel as the substrate of membrane material, and interpolation Semen Maydis oil is steam Intercept the factor, use high pressure microjet nanometer homogenizing and solvent evaporated method to obtain the emulsion of nanoscale, prepare and there is stronger water Vapour locking separating performance and the membrane material of mechanical performance.
The present invention uses high pressure microjet nanometer homogeneous technology to prepare the film forming liquid of nanoscale, with tradition sonde-type Micro-meter scale emulsion prepared by high speed homogenization is compared, and has less particle diameter, finer and close structure, oil phase and aqueous phase active force more By force, mechanical performance and the water vapor rejection performance of emulsion film has clear improvement.
Edible eco-friendly emulsion film material prepared by the present invention, has edibility, can be as food Inner packaging material, has biocompatibility, can have environment friendly as the controlled release carrier of bioactive substance, it is possible to Effectively degraded, alleviates the pressure to environment.The present invention solves the hydrophilic of albuminous coat material and mechanical strength is weak etc. that application is weak Point, also can add active substance, improves using value.
Detailed description of the invention
Below in conjunction with embodiment, the present invention will be described in detail, and embodiment is only the preferred embodiment of the present invention, It it not limitation of the invention.
Embodiment 1
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 5:1(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
3rd step utilizes rotary evaporation devices (50 DEG C, 20min) by clean for ethyl acetate volatilization, pours 18 cm × 20 cm into Poly (methyl methacrylate) plate in, be placed in 25 DEG C, film forming 48h in the climatic chamber of relative humidity 40%, make emulsion film material.
The present embodiment has carried out granulometry to this emulsion, and this membrane material has carried out mechanical performance and steam breathability energy Test.The granule size of film forming solution uses nano particle size and Zata potentiometric analyzer (MasterSizer 2000, Malvern Instruments, UK) measure, the mechanical performance of membrane material passes through INSTRON tensilometer (Instron 5565, Instron Corp., USA) measure, water vapor rejection performance uses poisture-penetrability tester (TYS-T1H, the Jinan limited public affairs of blue streak mechanical & electrical technology Department, China) measure.Test result such as table 1.
Embodiment 2
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 2:1(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
3rd step utilizes rotary evaporation devices (50 DEG C, 20min) by clean for ethyl acetate volatilization, pours 18 cm × 20 cm into Poly (methyl methacrylate) plate in, be placed in 25 DEG C, film forming 48h in the climatic chamber of relative humidity 40%, make emulsion film material.
Method as the present embodiment uses with embodiment 1 has carried out granulometry to this emulsion, carries out this membrane material Mechanical performance and steam breathability can be tested.Test result such as table 2.
Embodiment 3
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 1:1(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
3rd step utilizes rotary evaporation devices (50 DEG C, 20min) by clean for ethyl acetate volatilization, pours 18 cm × 20 cm into Poly (methyl methacrylate) plate in, be placed in 25 DEG C, film forming 48h in the climatic chamber of relative humidity 40%, make emulsion film material.
Method as the present embodiment uses with embodiment 1 has carried out granulometry to this emulsion, carries out this membrane material Mechanical performance and steam breathability can be tested.Test result such as table 3.
Embodiment 4
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 1:2(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
3rd step utilizes rotary evaporation devices (50 DEG C, 20min) by clean for ethyl acetate volatilization, pours 18 cm × 20 cm into Poly (methyl methacrylate) plate in, be placed in 25 DEG C, film forming 48h in the climatic chamber of relative humidity 40%, make emulsion film material.
Method as the present embodiment uses with embodiment 1 has carried out granulometry to this emulsion, carries out this membrane material Mechanical performance and steam breathability can be tested.Test result such as table 4.
Embodiment 5
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 1:5(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
3rd step utilizes rotary evaporation devices (50 DEG C, 20min) by clean for ethyl acetate volatilization, pours 18 cm × 20 cm into Poly (methyl methacrylate) plate in, be placed in 25 DEG C, film forming 48h in the climatic chamber of relative humidity 40%, make emulsion film material.
Method as the present embodiment uses with embodiment 1 has carried out granulometry to this emulsion, carries out this membrane material Mechanical performance and steam breathability can be tested.Test result such as table 5.
Comparative example 1
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, in the aqueous solution of sodium caseinate add 30%(w/w sodium caseinate) Semen Maydis oil and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
The material that step 2 is obtained by the 3rd step is poured in the poly (methyl methacrylate) plate of 18 cm × 20 cm, is placed in 25 DEG C, the wettest Film forming 48h in the climatic chamber of degree 40%, makes emulsion film material.
Method as this comparative example uses with embodiment 1 has carried out granulometry to this emulsion, carries out this membrane material Mechanical performance and steam breathability can be tested.Test result such as table 6.
Comparative example 2
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, in the aqueous solution of sodium caseinate add 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min), then uses high pressure Microjet (10000psi, 2 times) homogenizing is complete;
The material that step 2 is obtained by the 3rd step is poured in the poly (methyl methacrylate) plate of 18 cm × 20 cm, is placed in 25 DEG C, the wettest Film forming 48h in the climatic chamber of degree 40%, makes emulsion film material.
Method as this comparative example uses with embodiment 1 has carried out granulometry to this emulsion, to this membrane material Carry out mechanical performance and steam breathability can have been tested.Test result such as table 7.
Comparative example 3
First step sodium caseinate is dissolved in the water, and is made into 5%(w/w) solution, Semen Maydis oil is dissolved in ethyl acetate preparation Becoming oil phase, wherein, Semen Maydis oil is 5:1(w/w with the ratio of ethyl acetate), in the aqueous solution of sodium caseinate, add 30%(w/ W sodium caseinate) oil phase and 30%(w/w sodium caseinate) glycerol;
The material that step one is obtained by second step passes through the pre-homogenizing of high pressure dispersing machine (4000rpm, 2min);
The material that step 2 is obtained by the 3rd step is poured in the poly (methyl methacrylate) plate of 18 cm × 20 cm, is placed in 25 DEG C, the wettest Film forming 48h in the climatic chamber of degree 40%, makes emulsion film material.
The present embodiment has carried out granulometry to this emulsion, and this membrane material has carried out mechanical performance and steam breathability energy Test.The granule size of film forming solution uses nano particle size and Zata potentiometric analyzer (MasterSizer 2000, Malvern Instruments, UK) measure, the mechanical performance of membrane material passes through INSTRON tensilometer (Instron 5565, Instron Corp., USA) measure, water vapor rejection performance uses poisture-penetrability tester (TYS-T1H, the Jinan limited public affairs of blue streak mechanical & electrical technology Department, China) measure.Test result such as table 8.
In each embodiment, the granularity of filming emulsion and the steam transmission coefficient of membrane material are added up such as table 9 below.Such as table 9 institute Show, high pressure microjet and the intervention of solvent evaporation technique so that the size of filming emulsion has had significant reduction, especially Along with the increase of the addition of solvent ethyl acetate, the granule size of filming emulsion is gradually reduced, the effect of solvent evaporation technique The most notable.High pressure microjet and solvent evaporation technique make the steam transmission coefficient of membrane material also be varied from.From contrast The Data Comparison of example 1 and comparative example 2 is found out, the application of the interpolation of oils and fats and high pressure micro jetting technology makes the steam of membrane material Transmission coefficient has had and has significantly reduced.The Data Comparison of each embodiment and comparative example 1 is found out, solvent evaporation technique can enter one Step reduces the steam transmission coefficient of membrane material, say, that the block-water performance of membrane material is increased by solvent evaporation technique, This may be relevant on the impact of the size of filming emulsion with solvent evaporation technique, and the particle diameter of filming emulsion is the least, and structure is more Densification, the ability intercepting steam of membrane material is the strongest.The Data Comparison of each embodiment is found out, along with adding of solvent ethyl acetate The increase of dosage, the size of filming emulsion is gradually reduced, and the steam transmission coefficient of membrane material first reduces and raises afterwards, a side Face, along with the reduction of the particle diameter of filming emulsion, the structure of membrane material is finer and close, and its ability intercepting steam is gradually increasing, another Aspect, along with the increase of the amount adding ethyl acetate, the content of the Semen Maydis oil being deposited in membrane material constantly reduces, hydrophobic material The reduction of ratio cause the raising of membrane material hydrophilicity, the ability intercepting steam of membrane material the most constantly declines, and implements Example 2 can be issued to the best state intercepting steam in the effect of these two aspects with embodiment 3.
The vapor transfer rate deviation of membrane material prepared by the present invention is respectively less than 20%, has reached GB10457-2009 food plastic self-adhesion and has protected The standard level of fresh film.
In each embodiment, the elastic modelling quantity of membrane material, hot strength and elongation at break are added up such as table 10 below.By table 10 It can be seen that elastic modelling quantity, hot strength and the elongation at break of membrane material are all had by high pressure microjet with solvent evaporation technique Impact.From the Data Comparison of comparative example 1 and comparative example 2 it can be seen that the interpolation of oils and fats can significantly reduce the elasticity of membrane material Modulus and hot strength, improve the elongation at break of membrane material, and this good ductility with oils and fats is inseparable.From comparative example 1 and the Data Comparison of each embodiment it can be seen that in the case of oil phase content is equal, solvent evaporation technique can significantly improve The elastic modelling quantity of membrane material and hot strength, this granularity structure less, membrane material with filming emulsion before is more compacted There is certain cause effect relation in situation.From the Data Comparison of each embodiment it can be seen that along with the addition of solvent ethyl acetate Be continuously increased, solvent evaporation effect constantly strengthens, and the elastic modelling quantity of membrane material, hot strength and elongation at break all present elder generation Downward trend after rising, embodiment 2 then can reach hot strength and be more than or equal to 10MPa, and elongation at break is more than or equal to 120%, be equivalent to reach the standard level of PE in GB10457-2009 food plastic self-adhering plastic wrap.

Claims (7)

1. the preparation method of an edible eco-friendly emulsion film material, it is characterised in that step is:
S1. sodium caseinate is prepared as aqueous solution, after abundant aquation, adds the glycerol being equivalent to sodium caseinate quality 10-40% Be equivalent to the oil phase of sodium caseinate quality 5-30%, described oil phase is mixed with ethyl acetate by edible fats;
S2. the material high speed dispersor pre-homogenizing 2-5min, rotating speed 2000-6000rpm S1 obtained;Then high pressure is used Microjet nanometer homogenizer carries out second homogenate, and condition is 5000-12000psi, circulates 1-3 time;
S3. the material rotary evaporation obtained by S2, removes ethyl acetate, is dried to obtain edible eco-friendly emulsion film Material.
The preparation method of edible eco-friendly emulsion film material the most according to claim 1, it is characterised in that: institute Stating the mass percent concentration of sodium caseinate in caseinic acid sodium water solution is 3 ~ 7%.
The preparation method of edible eco-friendly emulsion film material the most according to claim 4, it is characterised in that: institute Stating the mass ratio of edible fats and ethyl acetate in oil phase is (1 ~ 5): (1 ~ 5).
The preparation method of edible eco-friendly emulsion film material the most according to claim 1, it is characterised in that: institute Stating edible fats is Semen Maydis oil.
The preparation method of edible eco-friendly emulsion film material the most according to claim 1, it is characterised in that: S3 Described rotary evaporation is rotary evaporation 20min under the conditions of 50 DEG C.
The preparation method of edible eco-friendly emulsion film material the most according to claim 1, it is characterised in that: S3 Described being dried is to be placed in climatic chamber by material, and the temperature of climatic chamber is 20-40 DEG C, and relative humidity is 50 ± 5%.
The preparation method of edible eco-friendly emulsion film material the most according to claim 1, it is characterised in that step Suddenly it is preferably:
S1. sodium caseinate is prepared as the aqueous solution that mass percent concentration is 5%, after abundant aquation, adds and is equivalent to casein The glycerol of acid sodium quality 30% and be equivalent to the oil phase of sodium caseinate quality 30%, described oil phase by Semen Maydis oil and ethyl acetate with The mass ratio of 2:1 mixes;
S2. the material high speed dispersor pre-homogenizing 2-5min, rotating speed 2000-6000rpm S1 obtained;Then high pressure is used Microjet nanometer homogenizer carries out second homogenate, and condition is 5000-12000psi, circulates 1-3 time;
S3. the material rotary evaporation obtained by S2, removes ethyl acetate, is dried to obtain edible eco-friendly emulsion film Material.
CN201610641096.9A 2016-08-08 2016-08-08 A kind of preparation method of edible environmental-friendly lotion membrane material Active CN106189271B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610641096.9A CN106189271B (en) 2016-08-08 2016-08-08 A kind of preparation method of edible environmental-friendly lotion membrane material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610641096.9A CN106189271B (en) 2016-08-08 2016-08-08 A kind of preparation method of edible environmental-friendly lotion membrane material

Publications (2)

Publication Number Publication Date
CN106189271A true CN106189271A (en) 2016-12-07
CN106189271B CN106189271B (en) 2019-04-26

Family

ID=57513687

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610641096.9A Active CN106189271B (en) 2016-08-08 2016-08-08 A kind of preparation method of edible environmental-friendly lotion membrane material

Country Status (1)

Country Link
CN (1) CN106189271B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101878904A (en) * 2010-06-23 2010-11-10 华南理工大学 Method for producing whey protein gel-like emulsion
CN102604394A (en) * 2012-03-19 2012-07-25 华南理工大学 Preparation method of biodegradable emulsion film material
EP2716697A1 (en) * 2012-10-08 2014-04-09 Codem Picardie Construction Durable et Eco Materiaux Picardie Composition including an oil and a protein
CN105410934A (en) * 2015-11-16 2016-03-23 华南理工大学 Water-soluble protein-phytosterin nanometer particles as well as preparation and application

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101878904A (en) * 2010-06-23 2010-11-10 华南理工大学 Method for producing whey protein gel-like emulsion
CN102604394A (en) * 2012-03-19 2012-07-25 华南理工大学 Preparation method of biodegradable emulsion film material
EP2716697A1 (en) * 2012-10-08 2014-04-09 Codem Picardie Construction Durable et Eco Materiaux Picardie Composition including an oil and a protein
CN105410934A (en) * 2015-11-16 2016-03-23 华南理工大学 Water-soluble protein-phytosterin nanometer particles as well as preparation and application

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
徐人平主编: "《包装新材料与新技术(第1版)》", 30 June 2006, 化学工业出版社 *

Also Published As

Publication number Publication date
CN106189271B (en) 2019-04-26

Similar Documents

Publication Publication Date Title
Zhang et al. Effects of hydrophobic agents on the physicochemical properties of edible agar/maltodextrin films
Yuan et al. Development of stable Pickering emulsions/oil powders and Pickering HIPEs stabilized by gliadin/chitosan complex particles
Bonilla et al. Effect of essential oils and homogenization conditions on properties of chitosan-based films
Zhang et al. Formation and stability of core–shell nanofibers by electrospinning of gel-like corn oil-in-water emulsions stabilized by gelatin
Tatar et al. Evaluation of hemicellulose as a coating material with gum arabic for food microencapsulation
Erdem et al. Development and structural assessment of whey protein isolate/sunflower seed oil biocomposite film
Aguilar et al. Protein adsorption onto alginate-pectin microparticles and films produced by ionic gelation
CN113614037A (en) Plant-based functional materials
CN112961409A (en) Chitosan-based edible film containing cinnamon oil/cellulose nanocrystals and preparation method and application thereof
Tam et al. Influence of solution properties and pH on the fabrication of electrospun lentil flour/HPMC blend nanofibers
Chalco‐Sandoval et al. Development of an encapsulated phase change material via emulsion and coaxial electrospinning
Li et al. Preparation of powdered oil by spray drying the Pickering emulsion stabilized by ovalbumin–gum Arabic polyelectrolyte complex
Bar et al. The unique nanostructure of shellac films
Jiang et al. Double scaffold networks regulate edible Pickering emulsion gel for designing thermally actuated 4D printing
Yu et al. Pickering emulsions co-stabilised by cellulose nanofibres and nicotinamide mononucleotide
CN107286546B (en) A kind of preparation method of Biodegradable high-molecular film
Xu et al. Robust and highly adaptable high internal phase gel emulsions stabilized solely by a natural saponin hydrogelator glycyrrhizic acid
WO2013151694A1 (en) Formation of conjugated protein by electrospinning
Liaotrakoon et al. Modifying the properties of whey protein isolate edible film by incorporating palm oil and glycerol
Sun et al. Biomass-based edible film with enhanced mass barrier capacity and gas permeable selectivity
Cartaxo da Costa Urtiga et al. Preparation and characterization of safe microparticles based on xylan
CN106189271A (en) A kind of preparation method of edible eco-friendly emulsion film material
EP3013325B1 (en) Nanoparticle and gelation stabilized functional composites of an ionic salt in a hydrophobic polymer matrix
CN102604394B (en) Preparation method of biodegradable emulsion film material
Kuznetsov et al. Specific features of the porous polymeric particle composites application as fillers for electrorheological fluids

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant