CN105580859A - Demoulding agent composition as well as preparation method and application thereof - Google Patents
Demoulding agent composition as well as preparation method and application thereof Download PDFInfo
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- CN105580859A CN105580859A CN201410562312.1A CN201410562312A CN105580859A CN 105580859 A CN105580859 A CN 105580859A CN 201410562312 A CN201410562312 A CN 201410562312A CN 105580859 A CN105580859 A CN 105580859A
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Abstract
The present invention relates to a demoulding agent composition as well as a preparation method and an application thereof. The demoulding agent composition provided by the invention comprises the following components in percentage by weight: 85-98.9wt% of triacylglycerols, 1-10wt% of deeply-hydrogenated oil and fat, and 0.1-5wt% of an emulsifying agent. When the demoulding agent composition disclosed by the invention is used for baking foods, smoke is not generated, wax does not need to be added as a raw material, so that the cost is greatly reduced, and the problem that the demoulding agent is unevenly settled and layered is solved.
Description
Technical field
The present invention relates to mold release compositions and its production and use.
Background technology
Food service industry, especially adds and tends to occur that sticking to mould is existing man-hour curing processing or candyResemble. In order to address this problem, food service industry is used releasing agent to process conventionally at present, conventionallyThe releasing agent using, includes each vegetable oil and animal fat, shortening and butter solid, liquidParaffin body (white oil) and special food releasing agent etc.
Existing existing releasing agent patent or patent application, for example WO94/23313,WO2005094599、ZA200306582、US4108678、JP7170910、CN200810113280.1, CN201310589151.0 etc., be all with grease, wax, emulsifying agent,Water, antioxidant etc. are raw material, mix.
Therefore, at least bring 2 deficiencies, first, in these schemes, one most important formerMaterial is wax, generally selects Brazil wax, beeswax, rice bran wax, certain herbaceous plants with big flowers seed wax, soya wax etc., becomesThis is higher; Secondly, wax and grease tend to occur layering after mixing placement a period of time, cause de-Moulding oil is inhomogeneous, has brought inconvenience to use, makes its holding time shorter.
Therefore, need to be improved releasing agent, to overcome the defect of existing releasing agent.
Summary of the invention
The invention provides a kind of mold release compositions, to overcome the defect of existing releasing agent. ThisThe bright mold release compositions providing comprises following component or composed of the following components:
(1) triacylglycerol, its consumption accounts for mold release compositions gross weight 85-98.9wt%;
(2) deep hydrogenation grease, its consumption accounts for mold release compositions gross weight 1-10wt%;
(3) emulsifying agent, its consumption accounts for mold release compositions gross weight 0.1-5wt%.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. Preferably, in the molecule of described triacylglycerol, also have 1Individual or 2 LCFA residues. In a specific embodiments of the present invention, described trigalloylBase glycerol is middle long-chain fat acid glyceride (MLCT).
In a specific embodiments of the present invention, the average grain diameter of described mold release compositions is littleIn 3 μ m. In a specific embodiments of the present invention, the average particle of described mold release compositionsFootpath is 1.2-2.5 μ m.
In a specific embodiments of the present invention, described emulsifying agent is lecithin, sucrose fatIn acid esters, polyglyceryl fatty acid ester, monoglyceride, mono succinate glyceride, propylene glycol alginateOne or more.
In a specific embodiments of the present invention, in described mold release compositions, do not contain vegetable wax.In the present invention, described vegetable wax is vegetable wax conventional in releasing agent, for example can comprise butBe not limited to: Brazil wax, beeswax, rice bran wax, certain herbaceous plants with big flowers seed wax, soya wax.
The present invention also provides a kind of method of preparing releasing agent.
The method of preparing releasing agent provided by the invention comprises triacylglycerol, deep hydrogenation greaseMix with emulsifying agent, homogenising processing, so that the particle diameter of mixture is less than 3 μ m.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. In a preferred embodiment of the invention, described trigalloylIn the molecule of base glycerol, also there are 1 or 2 LCFA residues. At a tool of the present inventionIn body embodiment, described triacylglycerol is middle long-chain fat acid glyceride (MLCT).
In a specific embodiments of the present invention, described homogenising be treated to high speed shear and/orHigh-pressure homogeneous.
The purposes of the mold release compositions described in the present invention also provides. Releasing agent provided by the inventionPurposes comprise the purposes for the preparation of food.
In a specific embodiments of the present invention, described food is bakery.
In a more particular embodiment of the present invention, described food include but not limited to cake,Yolk pie, bread, moon cake etc.
The present invention also provides the purposes of triacylglycerol as releasing agent.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. Preferably, in the molecule of described triacylglycerol, also have 1Individual or 2 LCFA residues. In a specific embodiments of the present invention, described trigalloylBase glycerol is middle long-chain fat acid glyceride (MLCT).
Releasing agent provided by the invention, has the following advantages:
1, releasing agent of the present invention, compared with traditional food releasing agent, can add wax as raw material,Greatly reduce costs, and avoid releasing agent sedimentation layering problem of non-uniform.
2, improve smoke point, when bakery, produce without oil smoke.
3, do not need chilling kneading, maturing process, can simplify work flow, the shortening time.
Detailed description of the invention
The percentage by weight sum that should be understood that the contained component of the present composition equals 100%.
Below in conjunction with specific embodiment, the invention will be further described. Should be understood that following realityExecute example only for the present invention is described but not for limiting scope of the present invention.
In the present invention, if not special explanation, percentage (%) or part all refer to phaseFor percetage by weight or the weight portion of composition.
In the present invention, if not special explanation, related each component or its preferred groupDivide and can mutually be combined to form new technical scheme.
In the present invention, if not special explanation, all embodiment mentioned in this articleAnd preferred embodiment can be combined to form new technical scheme mutually.
In the present invention, if not special explanation, all technical characterictic mentioned in this articleAnd preferred feature can be combined to form new technical scheme mutually.
In the present invention, if there is no contrary explanation, the content sum of each component in compositionBe 100%.
In the present invention, if there is no contrary explanation, the umber sum of each component in compositionCan be 100 weight portions.
In the present invention, unless there are other explanations, number range " a-b " represents that a is between bThe breviary that closes of arbitrary real array represent, wherein a and b are real numbers. For example number range " 0-5 "Represent all to have listed the whole real numbers between " 0-5 " herein, " 0-5 " is theseThe breviary of combinations of values represents.
In the present invention, unless there are other explanations, integer number range " a-b " represents that a is to bBetween the breviary of arbitrary integer combination represent, wherein a and b are integers. For example integer numberValue scope " 1-N " represents 1,2 ... N, wherein N is integer.
In the present invention, unless there are other explanations, " its combination " represents many groups of described each elementDivide mixture, for example two kinds, three kinds, four kinds and until the multicomponent mixture of maximum possible.
If do not particularly not pointed out, this description term " one " used refers to " at least one ".
If do not particularly not pointed out, percentage of the present invention (comprising percetage by weight)Benchmark is all the gross weight of described composition.
" scope " disclosed herein is with the form of lower limit and the upper limit. Can be respectively one orMultiple lower limits, and one or more upper limit. Given range is by a selected lower limit and oneThe upper limit limits. Selected lower limit and the upper limit define the border of special scope. All canThe scope limiting by this way comprises with capable of being combined, any lower limit can with appointWhat upper limit is combined to form a scope. For example, 60-120 and 80 have been listed for special parameter-110 scope, is interpreted as that the scope of 60-110 and 80-120 also expects. ThisOutward, if the minimum zone value of listing 1 and 2, and if would list maximum magnitude value 3,4 Hes5, scope below can all expect: 1-3,1-4,1-5,2-3,2-4 and2－5。
In this article, except as otherwise noted, the ratio of each component or weight all refer to dry weight.
In this article, except as otherwise noted, each reaction is all carried out at normal temperatures and pressures.
In this article, except as otherwise noted, each reactions steps can sequentially be carried out, and also canDo not carry out in order. For example, between each reactions steps, can comprise other steps, and anti-Answering also can exchange order between step. Preferably, reaction method is herein that order is carried out.
Mold release compositions
Mold release compositions provided by the invention comprises following component or composed of the following components:
(1) triacylglycerol, its consumption accounts for mold release compositions gross weight 85-98.9wt%;
(2) deep hydrogenation grease, its consumption accounts for mold release compositions gross weight 1-10wt%;
(3) emulsifying agent, its consumption accounts for mold release compositions gross weight 0.1-5wt%.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. Preferably, in the molecule of described triacylglycerol, also have 1Individual or 2 LCFA residues. In a specific embodiments of the present invention, described trigalloylBase glycerol is middle long-chain fat acid glyceride (MLCT).
In the present invention, " middle long-chain fat acid glyceride " refers to the interior tool of molecule of triacylglycerolHave 1 or 2 medium chain fatty acid residues, other fatty acid residues are three of LCFA residueAcylglycerol.
In the present invention, " medium chain fatty acid " to refer to carbon number be 6～12 aliphatic acid. " longChain fatty acid " to refer to carbon number be 16～24 aliphatic acid.
In a specific embodiments of the present invention, in the middle long-chain fat acid glyceride of useChain fatty acid is sad and/or capric acid, LCFA be myristic acid, palmitoleic acid, stearic acid,Oleic acid, linoleic acid, leukotrienes, arachidic acid, arachic acid, mountain Yu's acid, erucic acid, wooden pyro acid,One or more in nervonic acid, for example include but not limited to into sad (capric acid) myristic acid sweetOil three esters, sad (capric acid) palmitoleic acid triglycerides, sad (capric acid) palmitic acid glycerine threeEster, sad (capric acid) stearic acid triglycerides, sad (capric acid) oleic acid triglycerides, sad(capric acid) linoleic acid triglyceride, sad (capric acid) leukotrienes triglycerides, sad (capric acid)Arachidic acid triglycerides, sad (capric acid) arachic acid triglycerides, sad (capric acid) mountain YuAcid glycerol three esters, sad (capric acid) erucic acid triglycerides, sad (capric acid) wooden pyro acid glycerine threeOne or more in ester, sad (capric acid) nervonic acid triglycerides; Wherein, " sad (capric acid)Myristic acid triglycerides " can comprise medium chain fatty acid be sad and/or capric acid (be for example 1 or2 sad or, 1 or 2 capric acid or, 1 sad and 1 capric acid), LCFA is meatThe triglycerides of myristic acid, " sad (capric acid) palmitoleic acid triglycerides ", " sad (capric acid)Palmitic acid triglycerides " etc. there is similar implication. In a specific embodiments of the present invention,The middle long-chain fat acid glyceride using includes but not limited to as sad oleic acid triglycerides, capric acid AsiaOleic acid triglycerides, sad palmitic acid triglycerides, sad linoleic acid triglyceride etc.
Those skilled in the art understands, and the middle long-chain fat acid glyceride using in the present invention also canTaking be medium chain fatty acid as 1 sad or 1 capric acid, LCFA is myristic acid, palmOleic acid, stearic acid, oleic acid, linoleic acid, leukotrienes, arachidic acid, arachic acid, mountain Yu's acid,2 in erucic acid, wooden pyro acid, nervonic acid (for example, can be one in above-mentioned LCFAKind or two kinds) middle long-chain fat acid glyceride. Those skilled in the art can pass through above-mentioned lengthChain fatty acid combines and obtains corresponding middle long-chain fat acid glyceride.
In the present invention, " deep hydrogenation " refers to liquid fat under certain condition, sends out with hydrogenRaw addition reaction, makes the two keys saturated technical process completely in grease molecule, and its technique is abilityThe technical staff in territory knows, for example can be with reference to " food grade soybean oil deep hydrogenation Process Exploration "The method of (grain and grease, 01 phase in 1999). In a specific embodiments of the present invention," deep hydrogenation grease " refers to the grease through the processing of deep hydrogenation treatment process, in the present inventionIn, preferably using deep hydrogenation vegetable oil, for example can include but not limited to: deep hydrogenation soya-bean oil,Deep hydrogenation rape oil, deep hydrogenation palm-kernel oil, deep hydrogenation palm oil, deep hydrogenation certain herbaceous plants with big flowers wet goods.
In a specific embodiments of the present invention, the average grain diameter of described mold release compositions is littleIn 3 μ m. In a specific embodiments of the present invention, the average particle of described mold release compositionsFootpath is 1.2-2.5 μ m. In a specific embodiments of the present invention, described mold release compositionsAverage grain diameter is 1.2 μ m, 1.3 μ m, and 1.4 μ m, 1.5 μ m, 1.6 μ m, 1.7 μ m, 1.8 μ m,1.9 μ m, 2.0 μ m, 2.1 μ m, 2.2 μ m, 2.3 μ m, 2.4 μ m, or 2.5 μ m.
In a specific embodiments of the present invention, the routine breast that the emulsifying agent making is this areaAgent, for example can be, but not limited to into lecithin, sucrose fatty ester, polyglyceryl fatty acid ester,One or more in monoglyceride, mono succinate glyceride, propylene glycol alginate.
In a specific embodiments of the present invention, polyglyceryl fatty acid ester comprises that dimerization to ten is poly-Polyglyceryl fatty acid ester, particularly, comprise two polyglyceryl fatty acid esters, trimerization glycerin fattyAcid esters, four polyglyceryl fatty acid esters, five polyglyceryl fatty acid esters, six polyglyceryl fatty acid esters, sevenPolyglyceryl fatty acid ester, eight polyglyceryl fatty acid esters, nine polyglyceryl fatty acid esters and ten polyglycerol estersFat acid esters.
In a specific embodiments of the present invention, in described mold release compositions, do not contain vegetable wax.In the present invention, described vegetable wax is vegetable wax conventional in releasing agent, and concrete kind is abilityThe technical staff in territory knows, for example, can include but not limited to: Brazil wax, beeswax, riceChaff wax, certain herbaceous plants with big flowers seed wax, soya wax.
Method
The present invention also provides a kind of method of preparing releasing agent.
The method of preparing releasing agent provided by the invention comprises triacylglycerol, deep hydrogenation greaseMix with emulsifying agent, homogenising processing, so that the particle diameter of mixture is less than 3 μ m.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. In a preferred embodiment of the invention, described trigalloylIn the molecule of base glycerol, also there are 1 or 2 LCFA residues. At a tool of the present inventionIn body embodiment, described triacylglycerol is middle long-chain fat acid glyceride (MLCT).
In a specific embodiments of the present invention, described homogenising processing comprises but is not limited toHigh speed shear and/or high-pressure homogeneous.
Purposes
The purposes of releasing agent provided by the invention comprises the purposes for the preparation of food.
In a specific embodiments of the present invention, described food is bakery.
In a more particular embodiment of the present invention, described food include but not limited to cake,Yolk pie, bread, moon cake etc.
The present invention also provides the purposes of triacylglycerol as releasing agent.
In a specific embodiments of the present invention, in the molecule of described triacylglycerol, have 1Individual or 2 medium chain fatty acid residues. Preferably, in the molecule of described triacylglycerol, also have 1Individual or 2 LCFA residues. In a specific embodiments of the present invention, described trigalloylBase glycerol is middle long-chain fat acid glyceride (MLCT).
Embodiment
In following embodiment of the present invention and comparative example, use
Deep hydrogenation rape oil, deep hydrogenation soya-bean oil are purchased from the limited public affairs of special oil (Shanghai) in goodDepartment;
Lecithin, sucrose fatty ester, polyglyceryl fatty acid ester (818JC), monoglyceride, amberAmber acid monoglyceride, propylene glycol alginate are purchased from Danisco;
Brazil wax is purchased from the new promise chemical industry in Shanghai;
MLCT is with reference to the method preparation in CN103380827A;
MCT is purchased from BASF.
In following embodiment of the present invention,
The detection method of the average grain diameter of mould oil composition is as follows: the method providing by manufacturer,Test (model: American-European gram LS-C-III) by laser particle size analyzer.
Embodiment 1
Get 100g deep hydrogenation rape oil after 65 DEG C of fusings, add 850g rape oil base MLCTIn oil, then add 50g lecithin, after mix and blend in 10000rpm high speed shear 3min,Obtain mould oil composition 1.
Detect the average grain diameter of the mould oil composition 1 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 1 is 2.3 μ m.
Embodiment 2
Get 10g deep hydrogenation soya-bean oil after 65 DEG C of fusings, add 989g certain herbaceous plants with big flowers oil base MLCT oilIn, then add 1g sucrose fatty ester, high-pressure homogeneous after mix and blend, pressure 150Mpa,Homogenizing time 5min, obtains mould oil composition 2.
Detect the average grain diameter of the mould oil composition 2 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 2 is 1.2 μ m.
Embodiment 3
Get 50g deep hydrogenation rape oil after 65 DEG C of fusings, add 900g soya-bean oil base MLCT oilIn, then add 50g polyglyceryl fatty acid ester, high speed shear after mix and blend, rotating speed20000rpm, time 2min, obtains mould oil composition 3.
Detect the average grain diameter of the mould oil composition 3 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 3 is 1.6 μ m.
Embodiment 4
Get 40g deep hydrogenation rape oil after 65 DEG C of fusings, add 950g tea oil base MLCT oilIn, then add 10g monoglyceride, high speed shear after mix and blend, rotating speed 10000rpm, timeBetween 3min, obtain mould oil composition 4.
Detect the average grain diameter of the mould oil composition 4 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 4 is 2.1 μ m.
Embodiment 5
Get 90g deep hydrogenation rape oil after 65 DEG C of fusings, add 870g rice oil base MLCT oilIn, then add 40g propylene glycol alginate, high speed shear after mix and blend, rotating speed10000rpm, time 3min, obtains mould oil composition 5.
Detect the average grain diameter of the mould oil composition 5 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 5 is 2.5 μ m.
Embodiment 6
Get 75g deep hydrogenation soya-bean oil after 65 DEG C of fusings, add 920g soya-bean oil base MLCT oilIn, then add 5g mono succinate glyceride, high-pressure homogeneous after mix and blend, pressure 150Mpa,Homogenizing time 5min, obtains mould oil composition 6.
Detect the average grain diameter of the mould oil composition 6 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 6 is 1.8 μ m.
Comparative example 1
Get 100g deep hydrogenation rape oil after 65 DEG C of fusings, add 850g rape oil base MLCTIn oil, then add 50g lecithin, mixing and stirring, obtains mould oil composition 7.
Detect the average grain diameter of the mould oil composition 7 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 7 is 12 μ m.
Comparative example 2
Get 100g deep hydrogenation rape oil, 200g Brazil wax after 65 DEG C of fusings, add 650gIn certain herbaceous plants with big flowers oil base MLCT oil, then add 50g lecithin, after mix and blend, pass through high speed shear,Rotating speed 10000rpm, time 3min, obtains mould oil composition 8.
Detect the average grain diameter of the mould oil composition 8 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 8 is 1.8 μ m.
Comparative example 3
Get 300g deep hydrogenation rape oil after 65 DEG C of fusings, add 650g soya-bean oil base MLCT oilIn, then add 50g polyglyceryl fatty acid ester, high speed shear after mix and blend, rotating speed20000rpm, time 2min, obtains mould oil composition 9.
Detect the average grain diameter of the mould oil composition 9 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 9 is 1.5 μ m.
Comparative example 4
Get 300g deep hydrogenation rape oil after 65 DEG C of fusings, add in 650gMCT oil, soAfter add 50g polyglyceryl fatty acid ester, high speed shear after mix and blend, rotating speed 20000rpm,Time 2min, obtains mould oil composition 10.
Detect the average grain diameter of the mould oil composition 10 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 10 is 1.6 μ m.
Comparative example 5
Get 50g deep hydrogenation rape oil after 65 DEG C of fusings, add 900g soya-bean oil base MLCT oilIn, then add 50g polyglyceryl fatty acid ester, high speed shear after mix and blend, rotating speed10000rpm, time 1min, obtains mould oil composition 11.
Detect the average grain diameter of the mould oil composition 11 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 11 is 3.5 μ m.
Comparative example 6
Get 100g deep hydrogenation rape oil after 65 DEG C of fusings, add 850g rape oil base MLCTIn oil, then add 50g lecithin, after mix and blend, pass through high speed shear, rotating speed 5000rpm,Time 2min, obtains mould oil composition 12.
Detect the average grain diameter of the mould oil composition 12 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 12 is 7.2 μ m.
Comparative example 7
Get 50g palm oil after 65 DEG C of fusings, add in 900g soya-bean oil base MLCT oil, soAfter add 50g polyglyceryl fatty acid ester, high speed shear after mix and blend, rotating speed 20000rpm,Time 2min, obtains mould oil composition 13.
Detect the average grain diameter of the mould oil composition 13 obtaining, result shows, the demoulding of acquisitionThe average grain diameter of fluid composition 13 is 1.8 μ m.
Evaluation experimental 1
This experiment is used cake to evaluate the demoulding performance of mould oil composition 1-13.
Cake formula: weak strength flour 200g, yellow leaf fermenting butter 200g, Icing Sugar 160g, egg200g。
Cake preparation technology:
1, yellow leaf fermenting butter mixes with Icing Sugar and beats at a high speed in vain;
2, then slowly add egg high speed to beat, it is mixed completely with fermenting butter;
3, finally add weak strength flour (purchased from Xin Liang grain and oil company), low speed mixes, and obtains batter.
Gained batter is clamp-oned to atomized spray respectively and have 2g embodiment 1-6, the comparative example 1-7 demouldingIn the mould of oil, each 20g batter of clamp-oning. Send into baking oven and bake 20min and come out of the stove, baking box topPortion's temperature and bottom temp are 200 DEG C/180 DEG C, and the situation of being fuming of observing while baking (the results are shown inTable 1).
Baked cake is poured out simultaneously, then scraped cake bits residual in bed die, andWeigh, to determine that cake considers residual weight (the results are shown in Table 1) to be worth doing.
Evaluation experimental 2
Investigate different mould oil composition 1-13 and placing after a period of time, whether sedimentation layering.
300ml mold release compositions 1-13 is contained in respectively in PET bottle, is placed on room temperature(25 DEG C) are lower to be preserved after 6 months, observed releasing agent sedimentation layering situation (the results are shown in Table 1).
Table 1
The above results shows, releasing agent of the present invention in storing process without sedimentation phenomenon, evenlyStable, and compared with the control, there is better stripping result, and also do not have while bakingSmog produces.
Although be appreciated that the present invention is illustrated with certain form, the present invention is not limited toThe shown content with describing in this description. It should be apparent to those skilled in the art thatUnder the prerequisite that does not depart from scope of the present invention, also can make a variety of changes. These change all at thisInvent in claimed scope.
Claims (10)
1. a mold release compositions, is characterized in that, described mold release compositions comprises:
(1) triacylglycerol, its consumption accounts for mold release compositions gross weight 85-98.9wt%;
(2) deep hydrogenation grease, its consumption accounts for mold release compositions gross weight 1-10wt%;
(3) emulsifying agent, its consumption accounts for mold release compositions gross weight 0.1-5wt%.
2. mold release compositions as claimed in claim 1, is characterized in that, described three acyl groupsIn the molecule of glycerine, there are 1 or 2 medium chain fatty acid residues, preferred, described three acyl groupsIn the molecule of glycerine, also there are 1 or 2 LCFA residues.
3. mold release compositions as claimed in claim 1 or 2, is characterized in that, described de-The average grain diameter of mould agent composition is less than 3 μ m.
4. mold release compositions as claimed in claim 3, is characterized in that, described releasing agent groupThe average grain diameter of compound is 1.2-2.5 μ m.
5. the mold release compositions as described in any one in claim 1-4, is characterized in that,Described emulsifying agent is lecithin, sucrose fatty ester, polyglyceryl fatty acid ester, monoglyceride, amberAmber acid monoglyceride, propylene glycol alginate.
6. the mold release compositions as described in any one in claim 1-5, is characterized in that,In described mold release compositions, do not contain vegetable wax.
7. a method of preparing releasing agent, is characterized in that, by triacylglycerol, extreme hydrogenCarburetion fat and emulsifying agent mix, and homogenising processing is so that the particle diameter of mixture is less than 3 μ m, excellentChoosing, in the molecule of described triacylglycerol, there are 1 or 2 medium chain fatty acid residues, morePreferably, in the molecule of described triacylglycerol, also there are 1 or 2 LCFA residues.
8. method as claimed in claim 7, is characterized in that, described homogenising is treated to heightSpeed is sheared and/or is high-pressure homogeneous.
9. the mold release compositions as described in any one in claim 1-6 is for the preparation of the use of foodOn the way, preferred, described food is bakery, more preferably cake, yolk pie, bread, the moonCake etc.
10. triacylglycerol is as the purposes of releasing agent, preferred, described triacylglycerolIn molecule, there are 1 or 2 medium chain fatty acid residues, preferred, described triacylglycerolMolecule in also there are 1 or 2 LCFA residues.
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| CN201410562312.1A CN105580859A (en) | 2014-10-21 | 2014-10-21 | Demoulding agent composition as well as preparation method and application thereof |
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| CN201410562312.1A CN105580859A (en) | 2014-10-21 | 2014-10-21 | Demoulding agent composition as well as preparation method and application thereof |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4108678A (en) * | 1977-01-12 | 1978-08-22 | Central Soya Company, Inc. | Release agent and method |
| US20040115332A1 (en) * | 2002-03-18 | 2004-06-17 | Teran Pamela Lynn | Low-residue, easy-cleaning and low-viscosity structured lipid pan release compositions and methods |
| CN101433224A (en) * | 2008-11-28 | 2009-05-20 | 杨东升 | Bakeware mold oil and method for producing the same |
| CN102792986A (en) * | 2012-08-17 | 2012-11-28 | 芝兰雅烘焙原料（无锡）有限公司 | Demoulding oil for bread |
-
2014
- 2014-10-21 CN CN201410562312.1A patent/CN105580859A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4108678A (en) * | 1977-01-12 | 1978-08-22 | Central Soya Company, Inc. | Release agent and method |
| US20040115332A1 (en) * | 2002-03-18 | 2004-06-17 | Teran Pamela Lynn | Low-residue, easy-cleaning and low-viscosity structured lipid pan release compositions and methods |
| CN101433224A (en) * | 2008-11-28 | 2009-05-20 | 杨东升 | Bakeware mold oil and method for producing the same |
| CN102792986A (en) * | 2012-08-17 | 2012-11-28 | 芝兰雅烘焙原料（无锡）有限公司 | Demoulding oil for bread |
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Application publication date: 20160518 |