CN109913312A - A kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed - Google Patents

A kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed Download PDF

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CN109913312A
CN109913312A CN201910282663.XA CN201910282663A CN109913312A CN 109913312 A CN109913312 A CN 109913312A CN 201910282663 A CN201910282663 A CN 201910282663A CN 109913312 A CN109913312 A CN 109913312A
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emulsion
rice bran
oil
rice
aqueous enzymatic
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张敏
许朵霞
王振华
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Beijing Technology and Business University
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Abstract

The invention discloses a kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed, emulsion layer, hydrolysis liquid layer, residual layer is can be obtained in the rice bran zymolyte obtained after cellulase treatment after centrifugation.Emulsion layer is taken, pH is adjusted, after centrifugation, free oil and obstinate emulsion is obtained, adds a certain amount of calcium chloride solution to obstinate emulsion, after centrifugation, obtain upper layer grease, the sum of the resulting free oil that is demulsified twice is total Rice bran crude oil.Adjusting pH method is to achieve the purpose that the structure and charging property that change interfacial film, to effectively be demulsified by changing emulsion system pH environment.Still the double electrical layers of protein are destroyed, generation aggregation between oil droplet is promoted to cause to be demulsified by the way that calcium chloride solution is added with the presence of part stubbornness emulsion after first demulsification centrifugation.Demulsification efficiency can be effectively improved by carrying out demulsification processing to the emulsion that aqueous enzymatic extraction Rice oil generates using breaking method provided by the invention, oryzanol content also significantly improves in gained Rice bran crude oil simultaneously, has low energy consumption, pollution-free, green and healthy, simple operation and other advantages.

Description

A kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed
Technical field
The present invention relates to a kind of processing methods of aqueous enzymatic extraction Rice oil, and especially one kind is in aqueous enzymatic extraction Rice oil In the process, emulsion breakdown is carried out by combining using adjusting pH method with electrostatic screen method, so that the method for improving demulsification efficiency, belongs to In field of food industry.
Background technique
China is maximum eating rice production state in the world, and rice bran is as the important by-products during Rice producing, mainly It is made of exocarp, middle pericarp, cross-linked layer, kind skin and aleurone.Rice bran is as rice oil extract raw material, and wherein oil quality divides Number is up to 12-22%.Rice oil is a kind of novel edible vegetable oil important, with high nutritive value, wherein the oleic acid contained, Linoleic acid plus linolenic acid mass fraction is up to 80% or more, and oleic acid and linoleic ratio meet international organization and pushed away close to 1: 1 The oleic acid and linoleic acid optimal proportion recommended.Also contain more oryzanol, tocotrienols, squalene and plant in Rice oil simultaneously The important biomolecules active material such as object sterol, nutritive value is far more than traditional edible vegetable oil such as peanut oil, soybean oil.At present Have the effects that the cholesterol in removing blood there are many research confirmation Rice oil, reduces blood lipid, promotes growth in humans's development, because This is described as nutrition oil by nutritionist.
Currently, common Rice oil extracting method includes organic solvent extraction, physical squeezing method and aqueous enzymatic method.Aqueous enzymatic method It is by oil-containing raw material by broken in various degree, is medium by adding specific biological enzyme, enzyme under conditions of most suitable using water Oil and non-oil component are divided the difference of oil and water affinity and the different of grease density using non-oil component by solution certain time From.More other two methods, aqueous enzymatic extraction is with oil quality is good, low energy consumption, equipment is simple, excellent without chemical contamination etc. Point is a kind of to propose oily new technology with broad prospect of application.
During aqueous enzymatic extraction Rice oil, oil and albumen are digested simultaneously, since albumen has good emulsibility, It can be adsorbed between grease rapidly, form interfacial film and be wrapped in outside oil droplet, to form stable oil-in-water emulsified system.Cause This first isolated free oil is very limited, and most oil is all present in emulsion layer, although mild enzymatic hydrolysis item Part is conducive to save the active skull cap components in grease, but generates a large amount of emulsion while mentioning oil and can significantly reduce grease Oil yield, thus limit aqueous enzymatic method mention oil development.
Summary of the invention
The purpose of the present invention is to above-mentioned defect in the prior art, a kind of aqueous enzymatic extraction Rice oil is provided Breaking method is demulsified to the emulsion of generation by being combined using adjusting pH method with electrostatic screen method, further increases brokenly Newborn rate, lower production costs meet the environmental requirement of " safety, green ".
To achieve the above object, the present invention adopts the following technical scheme:
A kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed, operating procedure are as follows:
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) it is enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, be tuned by certain solid-liquid ratio mixed Liquid is closed, mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Rice bran mixing is adjusted with the HCL solution of 2mol/L Liquid pH to 5.0 adds a certain amount of 1,4 beta-glucanase and plant extract enzyme, is digested to obtain first rice bran zymolyte.With The NaOH solution of 2mol/L adjusts first rice bran zymolyte pH to 9.0, the alkali carries certain time at 60 DEG C.2mol/L is used later NaOH solution continue adjust pH to 9.0, add a certain amount of Acalase2.4L alkali protease, carry out under certain condition Enzymatic hydrolysis, obtains final rice bran zymolyte.Obtained rice bran zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, later one It is centrifuged under fixed condition, obtains emulsion layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and stands 12h at 4 DEG C, carries out at demulsification to it Reason, is centrifuged under certain condition, upper layer grease is taken out, and lower layer's stubbornness emulsion takes out spare.The stubbornness that will be obtained after centrifugation Emulsion carries out demulsification processing again, is centrifuged under certain condition, take out upper layer free oil, be demulsified twice resulting free oil it As total Rice bran crude oil.
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (2) Middle solid-liquid ratio, that is, rice bran weight: deionized water weight 1: (5~8).
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (2) The amount of middle 1,4 beta-glucanase and plant extract enzyme is 1%~5%, and the two ratio is 1: (1~3), enzymatic hydrolysis condition are 50 DEG C, 1h~ 3h。
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (2) The middle alkali carries time is 5min~60min.
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (2) The amount of middle Acalase2.4L alkali protease is 1%~5%, and enzymatic hydrolysis condition is 60 DEG C, 2h~3h.
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (2) Centrifugal condition with step (3) is 6000r/min~10000r/min, 10min~30min.
Further, the method for the emulsion breakdown that a kind of above-mentioned aqueous enzymatic extraction Rice oil is formed, the step (3) In twice demulsification processing be respectively adjust emulsion pH to 3.5~5.5, at 40 DEG C~80 DEG C, water bath processing 1h~3h;Addition 0.03mol/L~0.1mol/L calcium chloride solution, at 60 DEG C~80 DEG C, water bath processing 10min~90min.
The beneficial effects are mainly reflected as follows carry out brokenly to the emulsion generated during aqueous enzymatic extraction Rice oil Cream processing, adjusting pH method is to achieve the purpose that the structure and charging property that change interfacial film by changing emulsion system pH environment, To effectively be demulsified.Calcium chloride solution is added in obstinate emulsion, stable protein double electrical layers will be destroyed, promote oil Aggregation occurs between drop to be caused to be demulsified.Two kinds of breaking methods joint can effectively improve demulsification efficiency, have low energy consumption, pollution-free, green Color health, simple operation and other advantages.
Detailed description of the invention
Fig. 1 is the process flow for the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil of the present invention is formed Figure.
Specific embodiment
The present invention is further explained and described combined with specific embodiments below, but protection scope of the present invention is simultaneously It is not limited only to this.
Comparative example 1
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 6 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/L HCL solution adjust rice bran pH of mixed to 5.0, add the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 3%, the two ratio Example is 1: 2, at 50 DEG C, digests 2h, obtains first rice bran zymolyte.First rice bran enzymatic hydrolysis is adjusted with the NaOH solution of 2mol/L Object pH to 9.0, the alkali carries 10min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran weight The Acalase2.4L alkali protease of amount 3% digests 2h, obtains final rice bran zymolyte at 60 DEG C.The rice bran that will be obtained Zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 20min under the revolving speed of 8500r/min later, obtains emulsion Layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and 12h is stood at 4 DEG C, adjust emulsion pH to 4.5, at 50 DEG C, water bath processing 3h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken out, calculates demulsification Rate and gained edible vegetable oil oryzanol content.
Comparative example 2
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 6 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/ The HCL solution of L adjusts rice bran pH of mixed to 5.0, adds the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 3%, the two Ratio is 1: 2, at 50 DEG C, digests 2h, obtains first rice bran zymolyte.First rice bran enzyme is adjusted with the NaOH solution of 2mol/L Solve object pH to 9.0, the alkali carries 10min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran The Acalase2.4L alkali protease of weight 3% digests 2h, obtains final rice bran zymolyte at 60 DEG C.The rice that will be obtained Chaff zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 20min under the revolving speed of 8500r/min later, obtains emulsion Layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and stands 12h at 4 DEG C, adds in emulsion 0.04mol/L calcium chloride solution, at 70 DEG C, water bath processing 1h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken Out, demulsification efficiency and gained edible vegetable oil oryzanol content are calculated.
Comparative example 3
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 6 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/ The HCL solution of L adjusts rice bran pH of mixed to 5.0, adds the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 3%, the two Ratio is 1: 2, at 50 DEG C, digests 2h, obtains first rice bran zymolyte.First rice bran enzyme is adjusted with the NaOH solution of 2mol/L Solve object pH to 9.0, the alkali carries 10min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran The Acalase2.4L alkali protease of weight 3% digests 2h, obtains final rice bran zymolyte at 60 DEG C.The rice that will be obtained Chaff zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 20min under the revolving speed of 8500r/min later, obtains emulsion Layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and stands 12h at 4 DEG C, adds in emulsion 0.04mol/L calcium chloride solution, at 70 DEG C, water bath processing 1h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken Out, lower layer's stubbornness emulsion takes out spare.The obstinate emulsion obtained after centrifugation is subjected to demulsification processing again, adjusts emulsion PH to 4.5, at 50 DEG C, water bath processing 3h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken out, twice The sum of the resulting free oil that is demulsified is total Rice bran crude oil, calculates demulsification efficiency and gained edible vegetable oil oryzanol content.
Embodiment 1
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 6 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/ The HCL solution of L adjusts rice bran pH of mixed to 5.0, adds the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 3%, the two Ratio is 1: 2, at 50 DEG C, digests 2h, obtains first rice bran zymolyte.First rice bran enzyme is adjusted with the NaOH solution of 2mol/L Solve object pH to 9.0, the alkali carries 10min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran The Acalase2.4L alkali protease of weight 3% digests 2h, obtains final rice bran zymolyte at 60 DEG C.The rice that will be obtained Chaff zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 20min under the revolving speed of 8500r/min later, obtains emulsion Layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and 12h is stood at 4 DEG C, adjust emulsion pH to 4.5, at 50 DEG C, water bath processing 3h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken out, lower layer is obstinate Emulsion takes out spare.The obstinate emulsion obtained after centrifugation is subjected to demulsification processing again, addition 0.04mol/L calcium chloride is molten Liquid, at 70 DEG C, water bath processing 1h.It is centrifuged 20min under the revolving speed of 8500r/min, upper layer grease is taken out, twice demulsification gained The sum of free oil be total Rice bran crude oil, calculate demulsification efficiency and gained edible vegetable oil oryzanol content.
Embodiment 2
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 8 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/ The HCL solution of L adjusts rice bran pH of mixed to 5.0, adds the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 4%, the two Ratio is 1: 3, at 50 DEG C, digests 3h, obtains first rice bran zymolyte.First rice bran enzyme is adjusted with the NaOH solution of 2mol/L Solve object pH to 9.0, the alkali carries 30min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran The Acalase2.4L alkali protease of weight 5% digests 3h, obtains final rice bran zymolyte at 60 DEG C.The rice that will be obtained Chaff zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 30min under the revolving speed of 6000r/min later, obtains emulsion Layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and 12h is stood at 4 DEG C, adjust emulsion pH to 3.5, at 60 DEG C, water bath processing 2h.It is centrifuged 30min under the revolving speed of 6000r/min, upper layer grease is taken out, lower layer is obstinate Emulsion takes out spare.The obstinate emulsion obtained after centrifugation is subjected to demulsification processing again, addition 0.1mol/L calcium chloride is molten Liquid, at 80 DEG C, water bath processing 30min.It is centrifuged 30min under the revolving speed of 6000r/min, upper layer grease is taken out, is demulsified twice The sum of resulting free oil is total Rice bran crude oil, calculates demulsification efficiency and gained edible vegetable oil oryzanol content.
Embodiment 3
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) be enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, by 1: 5 (rice bran weight: go from Sub- water weight) solid-liquid ratio is tuned into mixed liquor, and mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Use 2mol/ The HCL solution of L adjusts rice bran pH of mixed to 5.0, adds the 1,4 beta-glucanase and plant extract enzyme of rice bran weight 2%, the two Ratio is 1: 1, at 50 DEG C, digests 1h, obtains first rice bran zymolyte.First rice bran enzyme is adjusted with the NaOH solution of 2mol/L Solve object pH to 9.0, the alkali carries 60min at 60 DEG C.Continued to adjust pH to 9.0 with the NaOH solution of 2mol/L later, adds rice bran The Acalase2.4L alkali protease of weight 2% digests 2.5h, obtains final rice bran zymolyte at 60 DEG C.By what is obtained Rice bran zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, is centrifuged 10min under the revolving speed of 10000r/min later, obtains cream Shape liquid layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and 12h is stood at 4 DEG C, adjust emulsion pH to 5.5, at 80 DEG C, water bath processing 1h.It is centrifuged 10min under the revolving speed of 10000r/min, upper layer grease is taken out, lower layer is obstinate Emulsion takes out spare.The obstinate emulsion obtained after centrifugation is subjected to demulsification processing again, addition 0.08mol/L calcium chloride is molten Liquid, at 60 DEG C, water bath processing 90min.It is centrifuged 10min under the revolving speed of 10000r/min, upper layer grease is taken out, is demulsified twice The sum of resulting free oil is total Rice bran crude oil, calculates demulsification efficiency and gained edible vegetable oil oryzanol content.
The demulsification efficiency and oryzanol content for the emulsion difference breaking method that 1 aqueous enzymatic extraction Rice oil of table is formed
Adjusting pH method is to reach the mesh of the structure and charging property that change interfacial film by changing emulsion system pH environment , to effectively be demulsified.There is still the obstinate emulsion in part to exist after first demulsification centrifugation, by the way that calcium chloride solution is added, breaks The double electrical layers of bad egg's white matter promote to occur to assemble between oil droplet to cause to be demulsified.It can be seen that from the data of table 1 using this The breaking method for inventing offer, which carries out demulsification processing to the emulsion that aqueous enzymatic extraction Rice oil generates, can effectively improve demulsification efficiency, Oryzanol content also significantly improves in gained Rice bran crude oil simultaneously, has low energy consumption, pollution-free, green and healthy, easy to operate etc. Advantage.
The above is only a preferred embodiment of the present invention, it is noted that those skilled in the art are come It says, without departing from the principle of the present invention, several improvement can also be made, these improvement also should be regarded as protection of the invention Range.

Claims (7)

1. a kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed, which comprises the following steps:
(1) rice bran sample treatment: carry out the rice bran Jing Guo expanding treatment to crushed 40 meshes obtaining rice bran powder;
(2) it is enzymatically treated: deionized water will be added in rice bran powder that step (1) obtains, be tuned into mixed liquor by certain solid-liquid ratio, Mixed liquor is warming up to 90 DEG C of enzyme deactivation 15min, is cooled to room temperature later.Rice bran pH of mixed is adjusted with the HCL solution of 2mol/L To 5.0, a certain amount of 1,4 beta-glucanase and plant extract enzyme are added, is digested to obtain first rice bran zymolyte.Use 2mol/L NaOH solution adjust first rice bran zymolyte pH to 9.0, the alkali carries certain time at 60 DEG C.It is molten with the NaOH of 2mol/L later Liquid continues to adjust pH to 9.0, adds a certain amount of Acalase2.4L alkali protease, is digested, obtained under certain condition Final rice bran zymolyte.Obtained rice bran zymolyte is placed in enzyme deactivation 10min in 90 DEG C of water-baths, later under certain condition from The heart obtains emulsion layer, hydrolysis liquid layer, residual layer;
(3) emulsion breakdown: the emulsion that step (2) is obtained takes out, and stands 12h at 4 DEG C, carries out demulsification processing to it, It is centrifuged under certain condition, upper layer grease is taken out, lower layer's stubbornness emulsion takes out spare.The obstinate emulsion that will be obtained after centrifugation Demulsification processing is carried out again, is centrifuged under certain condition, upper layer free oil is taken out, and the sum of the resulting free oil that is demulsified twice is Total Rice bran crude oil.
2. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that Solid-liquid ratio, that is, rice bran weight in the step (2): deionized water weight 1: (5~8).
3. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that The amount of 1,4 beta-glucanase and plant extract enzyme is 1%~5% in the step (2), and the two ratio is 1: (1~3), enzymatic hydrolysis condition It is 50 DEG C, 1h~3h.
4. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that The alkali carries time is 5min~60min in the step (2).
5. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that The amount of Acalase2.4L alkali protease is 1%~5% in the step (2), and enzymatic hydrolysis condition is 60 DEG C, 2h~3h.
6. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that The centrifugal condition of the step (2) and step (3) is 6000r/min~10000r/min, 10min~30min.
7. the emulsion breakdown method that a kind of aqueous enzymatic extraction Rice oil according to claim 1 is formed, which is characterized in that Demulsification processing twice is respectively to adjust emulsion pH to 3.5~5.5, at 40 DEG C~80 DEG C, water bath processing in the step (3) 1h~3h;Add 0.03mol/L~0.1mol/L calcium chloride solution, at 60 DEG C~80 DEG C, water bath processing 10min~90min.
CN201910282663.XA 2019-04-10 2019-04-10 A kind of emulsion breakdown method that aqueous enzymatic extraction Rice oil is formed Pending CN109913312A (en)

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Application publication date: 20190621