CN102191128A - Method for preparing edible idesia oil - Google Patents
Method for preparing edible idesia oil Download PDFInfo
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- CN102191128A CN102191128A CN2011101147654A CN201110114765A CN102191128A CN 102191128 A CN102191128 A CN 102191128A CN 2011101147654 A CN2011101147654 A CN 2011101147654A CN 201110114765 A CN201110114765 A CN 201110114765A CN 102191128 A CN102191128 A CN 102191128A
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- idesia oil
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Abstract
The invention discloses a method for preparing idesia oil, which is characterized by comprising the following steps of: filtering crude idesia oil by a filtering cloth to remove mechanical impurities; adding 100 parts of the filtered crude idesia oil into 0.5 to 2.0 parts of degumming agents at 75 to 80 DEG C; stirring for 20 to 35 minutes; cooling and centrifuging to separate the colloid in the lower layer; washing the idesia oil in the upper layer by using deionized water to a neutral state to obtain degummed idesia oil; dehydrating the degummed idesia oil at a vacuum degree of 4000 to 5000 Pa and the temperature of 60 to 80 DEC C for 20 to 30 minutes; continuously deacidifying the dehydrated idesia oil at the temperature of 105 to 130 DEG C, the pressure of 10 to 20 Pa, the feed rate of 80 to 120 mL/h and the film scraper rotation speed of 150 to 200 r/min, wherein the light component is removed free fatty acid, and the heavy component is product oil. The method has the advantages that the colloid and the fatty acid are removed completely, the production period is short, the effective ingredients, such as vitamin E and the like in the grease are effectively remained; the prepared edible idesia oil has the advantages of high yield, high smoke point, stable property in a storage process, no precipitate, and invariant color; and a special deodorization technology is not needed.
Description
Technical field
The present invention relates to a kind of preparation method of edible idesia oil, belong to the processing technique field of edible oil.
Background technology
Root or bark of Nepal Mallotus (Idesia polycarpaMaxim.var.vestita Diels) is a strong wind section root or bark of Nepal Mallotus platymiscium, and deciduous tree is distributed in China Yangtze valley, and especially there is a large amount of wild resources on ground such as Sichuan, Shaanxi.The root or bark of Nepal Mallotus oleaginousness is up to 36-38%, and the individual plant oil offtake is up to 25-30kg, and becomes to reach term 40-50.Idesia oil contains abundant unsaturated fatty acids, is rich in nutritive value, and early stage research and the producing region edible process of local peasant reality has for many years also proved its security.China has a large population to plough and lacks in addition, and the plantation of root or bark of Nepal Mallotus does not occupy cultivated land, and makes full use of the root or bark of Nepal Mallotus resource and helps satisfying the demand of China people to edible oil, alleviates arable land pressure, meets the national strategy requirement.
The general crude oil of producing from oil crops is called crude oil, contain impurity, do not satisfy the daily life needs, some in addition contain harmful material, as the gossypol in the Oleum Gossypii semen, therefore erucic acid in the rapeseed oil etc. need make with extra care the plant standard that reaches to crude oil.Vegetables oil is refining to be needed through coming unstuck depickling, decolouring, operations such as deodorization.
So come unstuck and be also referred to as dephosphorization because the grease colloid is mainly phosphatide, technology has the aquation method to come unstuck at present, acid system comes unstuck, embrane method is come unstuck and enzymatic degumming.The aquation method is to remove a kind of traditional method of gelationus in the grease, hydration degum is to utilize gelationus wetting abilities such as hydrated phospholipid, under agitation hot water is added in the oil, make phosphatide water-swelling cohesion, other colloid in the grease energy absorb oil after the expansion, the solubleness of colloid in oil is reduced, through natural subsidence and separating of oil.Phosphoric acid degumming is not come unstuck or the pH value of regulation system such as hydration degum oil heated phosphoric or citric acid, nonhydratable phosphatide is dissociated, afterwards the phosphatide cooling is added water and make phosphatide form stable liquid crystal under the state at a slow speed, these crystal can fetter sugar and metal ion effectively, precipitate.At present the treating process of idesia oil has often been ignored the importance of coming unstuck, and does not often come unstuck or only carries out hydration degum.
High-acid value grease is if adopt chemical alkali refining or physics distillatory acid stripping method in the present industrial production that certain limitation is arranged.Because the acid value of oil and fat height, the excess alkali consumption that adds in the chemical bases sweetening process is big, alkali with the N-process of free fatty acids in, also saponification a large amount of neutral oils, make refining yield on the low side; The depickling of physical refining water vapor stripping, grease need be handled under the high temperature of long period, influences oil quality, in the grease some effective constituents as: meetings such as VE and sterol are overflowed with the water vapor stripping, have reduced health nutrient value.Molecular distillation technique is that the residence time is short because the material heating temperature is low, and advantages such as Heat stability is good provide approach to the processing of high molecular, high viscosity, heat-sensitive material.Preserve the effective constituent in the grease when adopting the molecular distillation technique separation of free fatty acids, removed the peculiar smell in the grease.
Summary of the invention
The present invention seeks to provide a kind of preparation method of idesia oil at the deficiencies in the prior art, be characterized in idesia oil come unstuck, depickling handles, and obtains colory edible idesia oil.It has the hygienic standard that loss of effective components in yield height, the grease meets national edible oil for a short time.
Purpose of the present invention is realized that by following technology wherein said raw material umber is parts by weight except that specified otherwise.
The preparation method of idesia oil may further comprise the steps:
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is removed by filter mechanical impurity with filter cloth;
(2), come unstuck
With 100 parts of the root or bark of Nepal Mallotus crude oils after the above-mentioned filtration, in temperature 75-80 ℃, add the degumming agent of 0.5-2.0 part, stir 20-35min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, obtains the root or bark of Nepal Mallotus degummed oil;
(3), dehydration:
With above-mentioned degummed oil in vacuum tightness 4000-5000Pa, temperature 60-80 ℃ the dehydration 20-30min;
(4), depickling
With 100 parts of above-mentioned dehydrated oils, at temperature 105-130 ℃, pressure 10-20Pa, feeding rate 80-120mL/h, the continuous depickling of blade applicator rotating speed 150-200r/min, light constituent is for removing free fatty acids, reorganization is divided into processed oil, and the yield that obtains idesia oil is 75-80%.
Degumming agent is phosphoric acid or citric acid.
The idesia oil that method for preparing obtains.
Above-mentioned idesia oil is used in food oil.
Performance test:
Adopt standard GB 5537-2008, GB/T17756-2003, GB/T5530.37-1996 and GB/T5530-2005 to detect, idesia oil is the light red transparent liquid, and no solvent residue, phospholipids content are less than 50ppm, and acid number is lower than 0.46, and smoke point is higher than 200 ℃.
The present invention has following advantage
1, the preparation method of idesia oil provided by the invention removes colloid and lipid acid is thorough, grease yield height, and processed oil smoke point height, deposited phenomenon does not appear in stable in properties in the storage process, and nondiscoloration does not need special deodorizing technology.
2, the preparation method of idesia oil provided by the invention is with short production cycle, effectively keeps the effective constituents such as vitamin-E in the grease.
Embodiment:
Below by embodiment the present invention is specifically described; it is important to point out that present embodiment only is used for the present invention is further specified; can not be interpreted as limiting the scope of the invention, the person skilled in the art in this field can content according to the present invention make some nonessential improvement and adjustment.
Embodiment 1
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is filtered with filter cloth, remove mechanical impurity;
(2), come unstuck
With 100 parts of above-mentioned pretreated idesia oils, add in the three-necked flask, in 75 ℃ of temperature, add 0.5 part of heavy phosphoric acid of oil, stir 20min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, acquires the root or bark of Nepal Mallotus degummed oil;
(3), dehydration
With above-mentioned degummed oil in vacuum tightness 4000Pa, 60 ℃ of temperature dehydration 30min;
(4), depickling
With 100 parts of above-mentioned dehydrated oils, 105 ℃ of temperature, pressure 10Pa, feeding rate 80mL/h, the continuous depickling of blade applicator rotating speed 150r/min, light constituent is for removing free fatty acids, and reorganization is divided into processed oil.
Embodiment 2
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is filtered with filter cloth, remove mechanical impurity;
(2), come unstuck
With 100 parts of above-mentioned pretreated idesia oils, add in the three-necked flask, in 80 ℃ of temperature, add 2.0 parts of heavy phosphoric acid of oil, stir 35min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, acquires the root or bark of Nepal Mallotus degummed oil;
(3), dehydration
With above-mentioned degummed oil in vacuum tightness 5000Pa, 60 ℃ of temperature dehydration 20min;
(4), depickling
With 100 parts of above-mentioned dehydrated oils, 130 ℃ of temperature, pressure 20Pa, feeding rate 120mL/h, the continuous depickling of blade applicator rotating speed 200r/min, light constituent is for removing free fatty acids, and reorganization is divided into processed oil.
Embodiment 3
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is filtered with filter cloth, remove mechanical impurity;
(2), come unstuck
With 100 parts of above-mentioned pretreated idesia oils, add in the three-necked flask, in 77 ℃ of temperature, add 1.5 parts of heavy phosphoric acid of oil, stir 25min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, acquires the root or bark of Nepal Mallotus degummed oil;
(3), dehydration
With above-mentioned degummed oil in vacuum tightness 4500Pa, 75 ℃ of temperature dehydration 25min;
(4), depickling
With 100 parts of above-mentioned dehydrated oils, 110 ℃ of temperature, pressure 15Pa, feeding rate 100mL/h, the continuous depickling of blade applicator rotating speed 170r/min, light constituent is for removing free fatty acids, and reorganization is divided into processed oil.
Embodiment 4
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is filtered with filter cloth, remove mechanical impurity;
(2), come unstuck
With 100 parts of above-mentioned pretreated idesia oils, add in the three-necked flask, in 78 ℃ of temperature, add 2.0 parts of heavy citric acids of oil, stir 35min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, acquires the root or bark of Nepal Mallotus degummed oil;
(3), dehydration
With above-mentioned degummed oil in vacuum tightness 5000Pa, 70 ℃ of temperature dehydration 30min;
(4), depickling
With 100 parts of above-mentioned dehydrated oils, 120 ℃ of temperature, pressure 17Pa, feeding rate 110mL/h, the continuous depickling of blade applicator rotating speed 190r/min, light constituent is for removing free fatty acids, and reorganization is divided into processed oil.
Claims (4)
1. the preparation method of an idesia oil is characterized in that this method may further comprise the steps:
(1), pre-treatment
The root or bark of Nepal Mallotus crude oil is removed by filter mechanical impurity with filter cloth;
(2), come unstuck
With 100 parts of the root or bark of Nepal Mallotus crude oils after the above-mentioned filtration, in temperature 75-80 ℃, add the degumming agent of 0.5-2.0 part, stir 20-35min, cooling back centrifugation lower floor colloid, the upper strata idesia oil is washed till neutrality with deionized water, obtains the root or bark of Nepal Mallotus degummed oil;
(3), dehydration
With above-mentioned degummed oil in vacuum tightness 4000-5000Pa, temperature 60-80 ℃ the dehydration 20-30min;
(4), depickling
With the idesia oil after the above-mentioned dehydration, at temperature 105-130 ℃, pressure 10-20Pa, feeding rate 80-120mL/h, the continuous depickling of blade applicator rotating speed 150-200r/min, light constituent is for removing free fatty acids, and reorganization is divided into processed oil.
2. the preparation method of idesia oil according to claim 1, its feature is phosphoric acid or citric acid at degumming agent.
3. the idesia oil for preparing of method according to claim 1.
4. use in food oil as idesia oil as described in the claim 3.
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CN201110114765A CN102191128B (en) | 2011-05-05 | 2011-05-05 | Method for preparing edible idesia oil |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102417860A (en) * | 2011-10-17 | 2012-04-18 | 四川省仁德制药有限公司 | Method for decoloration and deodorization of idesia polycarpa maxim.var.vestita diels oil |
CN103173283A (en) * | 2013-04-15 | 2013-06-26 | 四川省林业科学研究院 | Solvent de-acidifying method for edible idesia oil |
CN103478290A (en) * | 2013-09-30 | 2014-01-01 | 管天球 | Calcium-supplementing and health-care idesia oil |
CN105861140A (en) * | 2016-04-27 | 2016-08-17 | 四川森迪科技发展股份有限公司 | Refining method of Idesia polycarpa edible oil |
CN106497675A (en) * | 2016-11-16 | 2017-03-15 | 四川省林业科学研究院 | A kind of Degumming method of idesia oil |
CN107057832A (en) * | 2017-04-10 | 2017-08-18 | 陕西金油农林科技开发有限公司 | A kind of method that oily grape fruit oil prepares edible oil |
CN109111989A (en) * | 2018-10-23 | 2019-01-01 | 湖北旭舟林农科技有限公司 | A kind of method of refining of pair of idesia oil color protection |
CN109722337A (en) * | 2019-02-18 | 2019-05-07 | 湖北旭舟林农科技有限公司 | A kind of deodour method of idesia oil |
CN110643420A (en) * | 2019-11-13 | 2020-01-03 | 贵州航天乌江机电设备有限责任公司 | Process for extracting and refining oil from idesia polycarpa |
CN110903900A (en) * | 2019-12-17 | 2020-03-24 | 湖南林邑新能源有限公司 | Method for refining tung oil |
CN111139134A (en) * | 2019-12-27 | 2020-05-12 | 中粮工科(西安)国际工程有限公司 | Refining method of idesia polycarpa oil with high acid value |
CN112760163A (en) * | 2020-12-18 | 2021-05-07 | 四川省太鸿沅农业集团有限公司 | Preparation process of idesia polycarpa oil |
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US5696278A (en) * | 1993-03-17 | 1997-12-09 | Unilever Patent Holdings B.V. | Degumming of crude glyceride oils not exposed to prior enzymatic activity |
CN102041167A (en) * | 2010-12-10 | 2011-05-04 | 四川省毛叶山桐子科技股份有限公司 | Method for preparing idesia polycarpa edible vegetable oil by immobilized enzyme and hot brine treatment process |
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2011
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Patent Citations (2)
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US5696278A (en) * | 1993-03-17 | 1997-12-09 | Unilever Patent Holdings B.V. | Degumming of crude glyceride oils not exposed to prior enzymatic activity |
CN102041167A (en) * | 2010-12-10 | 2011-05-04 | 四川省毛叶山桐子科技股份有限公司 | Method for preparing idesia polycarpa edible vegetable oil by immobilized enzyme and hot brine treatment process |
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Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102417860A (en) * | 2011-10-17 | 2012-04-18 | 四川省仁德制药有限公司 | Method for decoloration and deodorization of idesia polycarpa maxim.var.vestita diels oil |
CN103173283A (en) * | 2013-04-15 | 2013-06-26 | 四川省林业科学研究院 | Solvent de-acidifying method for edible idesia oil |
CN103478290A (en) * | 2013-09-30 | 2014-01-01 | 管天球 | Calcium-supplementing and health-care idesia oil |
CN103478290B (en) * | 2013-09-30 | 2014-10-22 | 管天球 | Calcium-supplementing and health-care idesia oil |
CN105861140A (en) * | 2016-04-27 | 2016-08-17 | 四川森迪科技发展股份有限公司 | Refining method of Idesia polycarpa edible oil |
CN106497675A (en) * | 2016-11-16 | 2017-03-15 | 四川省林业科学研究院 | A kind of Degumming method of idesia oil |
CN107057832A (en) * | 2017-04-10 | 2017-08-18 | 陕西金油农林科技开发有限公司 | A kind of method that oily grape fruit oil prepares edible oil |
CN109111989A (en) * | 2018-10-23 | 2019-01-01 | 湖北旭舟林农科技有限公司 | A kind of method of refining of pair of idesia oil color protection |
CN109722337A (en) * | 2019-02-18 | 2019-05-07 | 湖北旭舟林农科技有限公司 | A kind of deodour method of idesia oil |
CN110643420A (en) * | 2019-11-13 | 2020-01-03 | 贵州航天乌江机电设备有限责任公司 | Process for extracting and refining oil from idesia polycarpa |
CN110903900A (en) * | 2019-12-17 | 2020-03-24 | 湖南林邑新能源有限公司 | Method for refining tung oil |
CN111139134A (en) * | 2019-12-27 | 2020-05-12 | 中粮工科(西安)国际工程有限公司 | Refining method of idesia polycarpa oil with high acid value |
CN112760163A (en) * | 2020-12-18 | 2021-05-07 | 四川省太鸿沅农业集团有限公司 | Preparation process of idesia polycarpa oil |
CN112760163B (en) * | 2020-12-18 | 2023-06-06 | 四川省太鸿沅农业集团有限公司 | Preparation process of idesia oil |
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