CN107216946A - The minimizing technology of plasticiser in a kind of fish oil - Google Patents

The minimizing technology of plasticiser in a kind of fish oil Download PDF

Info

Publication number
CN107216946A
CN107216946A CN201610165422.3A CN201610165422A CN107216946A CN 107216946 A CN107216946 A CN 107216946A CN 201610165422 A CN201610165422 A CN 201610165422A CN 107216946 A CN107216946 A CN 107216946A
Authority
CN
China
Prior art keywords
fish oil
organic solvent
eluent
plasticiser
silica gel
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.)
Pending
Application number
CN201610165422.3A
Other languages
Chinese (zh)
Inventor
代志凯
王义永
李祥清
吕红萍
许新德
邵斌
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.)
Zhejiang Medicine Co Ltd Xinchang Pharmaceutical Factory
Original Assignee
Zhejiang Medicine Co Ltd Xinchang Pharmaceutical Factory
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 Zhejiang Medicine Co Ltd Xinchang Pharmaceutical Factory filed Critical Zhejiang Medicine Co Ltd Xinchang Pharmaceutical Factory
Priority to CN201610165422.3A priority Critical patent/CN107216946A/en
Publication of CN107216946A publication Critical patent/CN107216946A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/10Refining fats or fatty oils by adsorption
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/02Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
    • A23D9/04Working-up

Abstract

The invention discloses the method that plasticiser in a kind of fish oil is removed, 1) fish oil after refining is dissolved in low polar organic solvent under conditions of 20~50 DEG C, to obtain sample solution;2) silica gel column chromatography first loaded is balanced with the low polar organic solvent, 1) the middle sample solution dissolved is pumped into silica gel column chromatography;3) after after end of the sample, using gradient elution, successively with No. 1, No. 2, No. 3 eluents, preceding part is with No. 1 eluent, and positive part is with No. 2 eluents, and rear part is with No. 3 eluents, finally balanced again with No. 1 eluant, eluent, the chromatographic column after balance may be reused;4) after eluent Fractional Collections, preceding part and rear part are discarded, positive part eluent is collected, the recycling design that is concentrated under reduced pressure obtains plasticiser after deodorization and detects qualified food-grade fish oil again.The content that effectively removes polyunsaturated fatty acid glyceride in most of impurity, fish oil by the inventive method can improve 3~5%.

Description

The minimizing technology of plasticiser in a kind of fish oil
Technical field
It is more particularly to a kind of to remove fish the present invention relates to a kind of method for removing the impurity in fish oil The method of plasticiser in oil, belongs to fats and oils processing and technical field of food safety.
Background technology
Fish oil is a kind of natural health product extracted out of marine fishes body, and fish oil is rich in ω -3 types polyunsaturated fatty acid (PUFA), particularly eicosapentaenoic acid (EPA) and two Dodecahexaene acid (DHA), is to health and intelligence with abundant nutritive value Power, which is developed, the physiological activator of significant impact, with regulation blood fat, suppress platelet aggregation, Prevention of arterial atherosis, prevention cardiovascular and cerebrovascular disease, reduction blood viscosity, prevention brain blood All multiactions such as bolt and cerebral infarction, antithrombotic, vasodilator and improvement eyesight.Therefore, it is rich in EPA and DHA fish oil has highly important nutrition and medical value.
Plasticiser is also known as plasticizer, and they are the systems of about 30 kinds of esters of phthalic acid formation Claim, current phthalate plasticiser (PAEs) is the main body of plasticiser, its yield Plasticiser total output 80% is accounted for, plastic shaping is industrially widely used in, particularly for polychlorostyrene Copolymer from ethylene and vinyl chloride, is also used for the products such as rubber, cellulose, dyestuff, dispersant. Due to production, using and processing procedure in release, therefore it can pass through number of ways Contaminated food, such as water, soil, air, packaging material for food.Phthalate thing Matter at normal temperatures be water white transparency oily liquids, be insoluble in water, be soluble in methanol, ethanol, A variety of organic solvents such as ether, belong to liposoluble substance, are easily detected in oily food.
Phthalate has estrogenic effect, hepatotoxicity wind agitation, renal toxicity, endangers men and women Reproductive system, triggers infant's hormonal imbalance, causes sex premature, in some instances it may even be possible to carcinogenic.Due to To the potential hazard of the mankind, European Union, the U.S., Japan, China are successively to phthalate Material is included in priority pollutants.DEHP (O-phthalics in phthalate plasticiser Sour two (2- ethyls) own esters), DBP (dibutyl phthalate) be major pollutants, grain Middle DEHP recall rates highest.China, which defends, does (2011) No. 551 file regulations of supervision letter, food, DEHP (phthalic acid two (2- ethylhexyls), DINP (phthalic acids in food additives Dinonyl), DBP (dibutyl phthalate) maximum allowable residual quantity be respectively 1.5mg/kg, 9.0mg/kg and 0.3mg/kg.
It is extra large in the last few years due to being influenceed by environmental factors such as surface soil, water source and air Pollute in the continuous cumulative function of food chain between gradually serious and marine organisms, hair fish oil in ocean Inevitably contain all kinds of environmental contaminants.These environmental contaminants for example residues of pesticides, heavy metal, Bioxin, BaP and plasticiser etc. constantly invade ocean, cause the marine eco-environment continuous Deteriorate, this kind of material is permanently present in fish oil and serious toxicity consequence caused by human body has been drawn Play the highest attention in the field.In consideration of it, as there is serious danger known to a class to health Harmful material, can remove this to greatest extent with a kind of convenient, the economic technique of industrial production Pollutant, minimum is reduced to by the content of plasticiser in fish oil, or even makes to examine in fish oil Measure this pollutant, it is clear that be very important.
On removing the environment such as removing heavy metals, agricultural chemicals, bioxin and BaP in current oil prodution industry The research of pollutant and report are more, and the technique study report removed to plasticiser is then less.
As open source literature " attributional analysis of food-grade deep sea fish oil and control " [Chinese oil, 2012,37 (5):44-47] in describe heavy metal, agriculture in fish oil refinery practice in detail The research of the method for analysis, control and the removal of medicine, bioxin and BaP and report, still The research on plasticiser control and pollution is not reported.Open source literature " plasticiser in edible oil Pollution channel and analysis method progress " [Chinese oil, 2013,38 (5):1-5] In describe in the plasticiser contamination phenomenon and edible oil of generally existing in current edible oil and plastify The ways and means of agent detection, but do not report the research method that plasticiser is removed in edible oil And means.Open source literature " safety of plasticiser and grain and oil product " [Chinese oil, 2013, 38(4):1-4] in describe plasticiser harm, grain and oil processing in plasticiser source and The method and approach of pollution are controlled, the grease that plasticiser has not been polluted equally yet removes modeling The method and means of agent.
Chinese patent CN103710153A discloses adjacent benzene two in a kind of quick removal peppermint oil The method of formate ester plasticiser, changes method by peppermint oil, alkali and water Hybrid Heating, utilizes alkali Phthalate plasticiser is hydrolyzed, then divides liquid to remove water layer, reaches in oil removing and plastifies The purpose of agent., will not water in alkaline aqueous solution but the main component of peppermint oil is menthol Solution, and the main component of fish oil is triglycerides, is added after alkaline aqueous solution in hydrolysis plasticiser While also can hydrolyzing triglyceride, can more seriously emulsify causes to be layered, thus should Method is not suitable for the removal of plasticiser in fish oil.
The B of Chinese patent CN 102965192 disclose a kind of remove in ganoderma lucidum spore oil raw material and moulded The method that agent is remained and polluted, this method is using hyperlink carbon dioxide in different pressures and temperature Plasticiser in the change in polarity of degree, selective extraction grease, but the process equipment requires high, Investment is big, and cost is high, without industrial value.
Chinese patent CN104705419A discloses a kind of side for removing plasticiser in edible oil Method, this method carries out multiple liquid-liquid extraction, extraction to edible oil using a large amount of methanol as solvent Methanol and edible oil are separated after taking, last recycling methanol.Due to phthalate modeling Agent is fat-soluble compound in itself, and the solubility in vegetable oil is more than dissolving in methyl alcohol Degree, so it is low, it is necessary to a large amount of molten to remove plasticiser efficiency using the raw material of above-mentioned liquid-liquid extraction Agent is extracted repeatedly, and solvent consumption is big, wastes time and energy, and can greatly increase being produced into for fish oil This.
Chinese patent CN102295989A discloses phthalic acid ester in removal vegetable and animals oils The molten of phthalate material can be dissolved and be adsorbed to the method for class plasticiser, this method utilization Agent utilizes work(of the back washing agent to dissolving and the absorption of phthalate material as back washing agent Can, realize the purpose for removing phthalate plasticiser in animal and plant fat.Equally, by Fat-soluble in phthalate plasticiser determines that its solubility in oil is big, needs Substantial amounts of organic solvent is extracted repeatedly to be removed, and efficiency is low, and technique is cumbersome, remove cost high.
In view of to there is technical process on plasticiser in grease is removed cumbersome for above-mentioned prior art, it is raw Produce cost height, industrial applications and be worth low defect, fish can be removed to greatest extent by finding one kind Plasticiser in oil, and technical process is easy, production cost is low, be adapted to large-scale industrial production Fish oil technique be very important.
The content of the invention
The method that the present invention removes plasticiser in food-grade fish oil for a kind of silica gel column chromatography of offer.
The separation principle of silica gel column chromatography is different and obtain according to absorption affinity of the material on silica gel To separation, the larger material of polarity is easily by silica gel absorption, and the weaker material of polarity is difficult by silica gel Absorption, whole chromatography process is Adsorption and desorption, adsorb again, desorption process again.Adjacent benzene two Formate ester plasticiser due to be macromolecular Ester, its polarity is weaker, phthalic acid The polarity of esters is less than the polarity of the triglycerides in grease, it is considered to utilize phthalate Plasticiser and polyunsaturated fatty acid triglycercide polarity difference in fish oil, utilize opposed polarity Organic solvent gradient elution, to reach the purpose of removing plasticiser.
The technical problem to be solved in the present invention is to provide for a kind of removal of plasticiser in fish oil Method, the minimizing technology comprises the following steps:Step 1):Fish oil after refining is existed It is dissolved under conditions of 20~50 DEG C in low polar organic solvent, to obtain sample solution;Wherein, institute State the one kind of low polar organic solvent in n-hexane, hexamethylene, petroleum ether and normal heptane; Step 2):The silica gel column chromatography first loaded is balanced with the low polar organic solvent, so Afterwards by step 1) in the sample solution that has dissolved be pumped into the speed of 0.1~1 times of column volume/hour In silica gel column chromatography;Step 3):After after end of the sample, using gradient elution, successively with 1 Number eluant, eluent, No. 2 eluant, eluents, No. 3 eluents, (preceding part refers to that rudimentary polarity is miscellaneous to preceding part Matter component, is eluted out at first) with No. 1 eluent, (positive part refers to medium pole to positive part Property impurity composition, i.e., required for component, median elution comes out) with No. 2 eluents, Part (rear part refers to highly polar impurity composition, is finally eluted out) is with No. 3 eluents afterwards, Finally balanced again with No. 1 eluant, eluent, the chromatographic column after balance may be reused;And step 4):After eluent Fractional Collections, preceding part and rear part are discarded, positive part eluent, decompression is collected Concentration and recovery solvent obtains plasticiser after deodorization and detects qualified food-grade fish oil again.
In the preferred technical solution of the present invention, it is preferable that the chromatographic stationary phases are nonbonding silicon Glue, particle diameter is 60~400 mesh indefinite form silica gel.It is highly preferred that the particle diameter is 100~200 Mesh indefinite form silica gel.
In the preferred technical solution of the present invention, it is preferable that the quality of fish oil is in the sample solution 0.05~0.5 times of silica gel chromatographic column filling material.It is highly preferred that the quality of fish oil is in the sample solution 0.1~0.2 times of silica gel chromatographic column filling material.
In the preferred technical solution of the present invention, it is preferable that No. 1 eluant, eluent is that low polarity has Machine solvent;No. 2 eluant, eluents and No. 3 eluant, eluents be respectively low polar organic solvent with The mixed solvent of highly polar organic solvent;Wherein, low polarity is organic molten in No. 2 eluant, eluents Percent by volume >=60% that agent is accounted for, >=70%, >=80% or >=90%, No. 3 elutions Highly polar organic solvent percentage >=60% in agent, >=70%, >=80% or >=90%.
In the preferred technical solution of the present invention, it is preferable that the low polar organic solvent is selected from just One kind in hexane, hexamethylene, normal heptane, petroleum ether.It is highly preferred that the low polarity has Machine solvent is normal heptane.
In the preferred technical solution of the present invention, it is preferable that the highly polar organic solvent is selected from second One kind in acetoacetic ester, isopropanol, acetone and methyl tertiary butyl ether(MTBE).It is highly preferred that the height Polar organic solvent is acetone.
According to the minimizing technology of the present invention, alkali refining fish oil can be alkali refining oil, bleached oil, deodorization Oil or winterized oil, preferably bleached oil.Bleached oil is removed after plasticiser by above-mentioned silica gel column chromatography, Obtain meeting the product oil of plasticiser quality standard after deodorization again.The alkali refining oil refers to hair Oil of the fish oil after degumming and depickling processing;The bleached oil refer to mao fish oil by degumming, Oil after depickling and decolorization;The deodorised oil refers to that mao fish oil passes through degumming, depickling, taken off Oil after color and deodorization processing.The winterized oil refer to mao fish oil by degumming, depickling, decolouring, Oil after deodorization and winterization processing;
A kind of Advantageous effect for removing the method for plasticiser in edible oil provided by the present invention It is really:1) removal efficiency is high, and the inventive method removes plasticiser effect in fish oil significantly, can The exceeded fish oil of all kinds of plasticisers is effectively handled, is detected through third party testing agency, after processing Fish oil meets the standard requirement of national plasticiser, effectively removes most of low polarity and height The content of polyunsaturated fatty acid glyceride can improve 3~5% in the impurity of polarity, fish oil,.2) With strong points, the inventive method targetedly removes the plasticiser in grease, in grease Other compositions are substantially without influence, mild condition, the grease outward appearance after processing, color, physics and chemistry Matter is significantly lifted.3) processing speed is fast, cost is low, the inventive method disposal ability Greatly, method is simple, quick and with low cost, and silica gel column chromatography and organic solvent can be followed Ring is used, it is easy to the large-scale production of industrialization.
Brief description of the drawings
Fig. 1 represents the process chart of the present invention.
Embodiment
Below with reference to drawings and examples, the present invention will be further described, implementation of the invention Example is merely to illustrate technical scheme, and the non-limiting present invention.
Embodiment 1
Chromatographic column 60 × 800mm, the interior mesh silica gel 500g of filling 100~200, column volume is 800mL, i.e. 1BV=800ml, are first balanced using preceding with 2BV normal heptane.
Take 100g decolourize after fish oil (EPA and DHA content are 29.5% or so in the fish oil, Plasticiser detection DBP is 1.5mg/kg, and DEHP is 24mg/kg, other not detect), plus Enter 100ml normal heptane in after 20~30 DEG C of stirring and dissolvings to obtain sample solution, will by preparing pump The sample solution is pumped into silica gel column chromatography with the speed of 0.1~1 times of column volume/hour, loading knot Shu Hou, then uses 2BV normal heptane, 2BV 10% acetone-normal heptane, 2BV70% successively Acetone-normal heptane gradient elution.The preceding part of Fractional Collections, positive part and rear part, wherein positive part is 76.3g, EPA and DHA content are that 32.6%, DEHP is 0.2mg/kg, other not detect;Moulded Agent detects qualified food-grade fish oil.
Embodiment 2
Chromatographic column 60 × 800mm, interior filling 60-100 mesh silica gel 500g, column volume is 800mL, i.e. 1BV=800ml, are first balanced using preceding with 2BV n-hexane.
Taking the fish oil after 75g decolourings, (EPA and DHA content are 29.5% or so in the fish oil, modeling Agent detection DBP is 1.5mg/kg, and DEHP is 24mg/kg, other not detect), add 75ml n-hexanes in after 30~40 DEG C of stirring and dissolvings to obtain sample solution, will be described by preparing pump Sample solution is pumped into silica gel column chromatography with the speed of 0.1~1 times of column volume/hour, after end of the sample, Then 3BV n-hexane, 1.5BV 15% ethyl acetate-hexane, 2BV60% is used successively Ethyl acetate-hexane gradient elution.The preceding part of Fractional Collections, positive part and rear part, wherein positive part For 72.3g, EPA and DHA content are 32.9%, and plasticiser is not detected;Obtain plasticiser inspection Survey qualified food-grade fish oil.
Embodiment 3
Chromatographic column 60 × 800mm, the interior mesh silica gel 500g of filling 200~300, column volume is 800mL, i.e. 1BV=800ml, are first balanced using preceding with 2BV hexamethylene.
Taking the fish oil after 25g deodorizations, (EPA and DHA content are 28.5%, plasticiser in the fish oil Detection DBP is 1.1mg/kg, and DEHP is 7.9mg/kg, other not detect), add 75ml Hexamethylene in after 40~50 DEG C of stirring and dissolvings to obtain sample solution, by preparing pump by the loading Liquid is pumped into silica gel column chromatography with the speed of 0.1~1 times of column volume/hour, after end of the sample, so Afterwards successively with 2BV hexamethylene, 1.5BV 15% isopropanol-hexamethylene, 2BV60% isopropyls Alcohol-hexamethylene gradient elution.The preceding part of Fractional Collections, positive part and rear part, wherein positive part is 21.5g, EPA and DHA content are 31.9%, and plasticiser is not detected;Obtain plasticiser detection qualified Food-grade fish oil.
Embodiment 4
Chromatographic column 60 × 800mm, the interior mesh silica gel 250g of filling 300~400, column volume is 400mL, i.e. 1BV=400ml, are first balanced using preceding with 2BV petroleum ether.
Taking the fish oil after 125g winterization, (EPA and DHA content are 31.4% in the fish oil, plasticizing Agent detection DBP is 0.8mg/kg, and DEHP is 5.8mg/kg, other not detect), add 125ml Normal heptane in after 20~30 DEG C of stirring and dissolvings to obtain sample solution, by preparing pump by the loading Liquid is pumped into silica gel column chromatography with the speed of 0.1~1 times of column volume/hour, after end of the sample, so Use 2BV petroleum ether, 2BV 10% acetone-petroleum ether, 2BV80% acetone-petroleums successively afterwards Ether gradient elution.The preceding part of Fractional Collections, positive part and rear part, wherein positive part is 105.4g, EPA It is 32.9% with DHA content, plasticiser is not detected;Obtain plasticiser and detect qualified food Level fish oil.
Embodiment 5
Chromatographic column 60 × 800mm, the interior mesh silica gel 250g of filling 100~200, column volume is 400mL, i.e. 1BV=400ml, are first balanced using preceding with 2BV normal heptane.
Taking the fish oil after 75g winterization, (EPA and DHA content are 31.4%, plasticiser in the fish oil Detection DBP is 0.8mg/kg, and DEHP is 5.8mg/kg, other not detect), add 755ml Normal heptane in after 25~30 DEG C of stirring and dissolvings to obtain sample solution, by preparing pump by the loading Liquid is pumped into silica gel column chromatography with the speed of 0.1~1 times of column volume/hour, after end of the sample, so Use 2BV normal heptane, 1BV 20% methyl tertiary butyl ether(MTBE)-normal heptane, 1BV90% successively afterwards Methyl tertiary butyl ether(MTBE)-normal heptane gradient elution.The preceding part of Fractional Collections, positive part and rear part, wherein Positive part is 55.6g, and EPA and DHA content are 34.9%, and plasticiser is not detected;Plastified Agent detects qualified food-grade fish oil.
The technical scheme in the embodiment of invention is checked, is fully described by above, described Embodiment be only the present invention a part of embodiment, rather than whole embodiment.It is based on Embodiment in the present invention, those of ordinary skill in the art institute under the premise of creativeness is not made The all other embodiment obtained.

Claims (10)

1. a kind of minimizing technology of plasticiser in fish oil, the minimizing technology comprises the following steps:
Step 1):Fish oil after refining is dissolved in low polarity under conditions of 20~50 DEG C organic molten In agent, to obtain sample solution;Wherein, the low polar organic solvent is selected from n-hexane, hexamethylene One kind in alkane, petroleum ether and normal heptane;
Step 2):The silica gel column chromatography first loaded is balanced with the low polar organic solvent, Then by step 1) in the sample solution that has dissolved with the speed pump of 0.1~1 times of column volume/hour Enter in silica gel column chromatography;
Step 3):After after end of the sample, using gradient elution, successively with No. 1 eluant, eluent, 2 Number eluant, eluent, No. 3 eluents, preceding part is with No. 1 eluent, and positive part is with No. 2 elutions Agent is eluted, and rear part finally balances the height in chromatogram with No. 1 eluant, eluent again with No. 3 eluents Chromatographic column after polar organic solvent, balance may be reused;And
Step 4):After eluent Fractional Collections, preceding part and rear part are discarded, positive part elution is collected Liquid, the recycling design that is concentrated under reduced pressure obtains plasticiser after deodorization and detects qualified food-grade fish again Oil.
2. according to the method described in claim 1, wherein, the chromatographic stationary phases be nonbonding Silica gel, particle diameter is 60~400 mesh indefinite form silica gel.
3. method according to claim 2, wherein, the particle diameter be 100~200 mesh not Sizing silica gel.
4. according to the method described in claim 1, wherein, the matter of fish oil in the sample solution Measure as 0.05~0.5 times of silica gel chromatographic column filling material.
5. according to the method described in claim 1, wherein, the matter of fish oil in the sample solution Measure as 0.1~0.2 times of silica gel chromatographic column filling material.
6. according to the method described in claim 1, wherein, No. 1 eluant, eluent be low pole Property organic solvent;No. 2 eluant, eluents and No. 3 eluant, eluents are respectively that low polarity is organic molten Agent and the mixed solvent of highly polar organic solvent;Wherein, in No. 2 eluant, eluents there be low polarity Percent by volume >=60% that machine solvent is accounted for, >=70%, >=80% or >=90%, described No. 3 Highly polar organic solvent percentage >=60% in eluant, eluent, >=70%, >=80% or >=90%.
7. method according to claim 6, wherein, the low polar organic solvent choosing One kind from n-hexane, hexamethylene, normal heptane, petroleum ether.
8. method according to claim 7, wherein, the low polar organic solvent is Normal heptane.
9. method according to claim 6, wherein, the highly polar organic solvent choosing One kind from ethyl acetate, isopropanol, acetone and methyl tertiary butyl ether(MTBE).
10. method according to claim 9, wherein, the highly polar organic solvent is Acetone.
CN201610165422.3A 2016-03-22 2016-03-22 The minimizing technology of plasticiser in a kind of fish oil Pending CN107216946A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610165422.3A CN107216946A (en) 2016-03-22 2016-03-22 The minimizing technology of plasticiser in a kind of fish oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610165422.3A CN107216946A (en) 2016-03-22 2016-03-22 The minimizing technology of plasticiser in a kind of fish oil

Publications (1)

Publication Number Publication Date
CN107216946A true CN107216946A (en) 2017-09-29

Family

ID=59927340

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610165422.3A Pending CN107216946A (en) 2016-03-22 2016-03-22 The minimizing technology of plasticiser in a kind of fish oil

Country Status (1)

Country Link
CN (1) CN107216946A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112694947A (en) * 2020-12-01 2021-04-23 晨光生物科技集团股份有限公司 Method for removing plasticizer from pepper essential oil and pepper essential oil
CN113122377A (en) * 2019-12-30 2021-07-16 丰益(上海)生物技术研发中心有限公司 Method for removing plasticizer in oil refining process
CN113201397A (en) * 2021-04-08 2021-08-03 四川国为制药有限公司 Method for reducing plasticizer content in fish oil product

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030175401A1 (en) * 2002-02-05 2003-09-18 Kabushiki Kaisha Toshiba Method of treating fats and oils
CN102295989A (en) * 2011-07-26 2011-12-28 中山大学 Method for removing phthalates from animal fat and vegetable oil
CN102586010A (en) * 2011-12-31 2012-07-18 内蒙古金达威药业有限公司 Preparation method of polyunsaturated fatty glyceride winterized oil
CN104705419A (en) * 2013-12-14 2015-06-17 河南省亚临界生物技术有限公司 Edible oil plasticizer removing method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030175401A1 (en) * 2002-02-05 2003-09-18 Kabushiki Kaisha Toshiba Method of treating fats and oils
CN102295989A (en) * 2011-07-26 2011-12-28 中山大学 Method for removing phthalates from animal fat and vegetable oil
CN102586010A (en) * 2011-12-31 2012-07-18 内蒙古金达威药业有限公司 Preparation method of polyunsaturated fatty glyceride winterized oil
CN104705419A (en) * 2013-12-14 2015-06-17 河南省亚临界生物技术有限公司 Edible oil plasticizer removing method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
何东平,等: "《油茶籽加工技术》", 31 July 2015, 中国轻工业出版社 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113122377A (en) * 2019-12-30 2021-07-16 丰益(上海)生物技术研发中心有限公司 Method for removing plasticizer in oil refining process
CN112694947A (en) * 2020-12-01 2021-04-23 晨光生物科技集团股份有限公司 Method for removing plasticizer from pepper essential oil and pepper essential oil
CN113201397A (en) * 2021-04-08 2021-08-03 四川国为制药有限公司 Method for reducing plasticizer content in fish oil product
CN113201397B (en) * 2021-04-08 2024-02-23 四川国为制药有限公司 Method for reducing plasticizer content in fish oil product

Similar Documents

Publication Publication Date Title
CN101379174B (en) Process for production of highly enriched fractions of natural compounds from palm oil with supercritical and near critical fluids
Čmolík et al. Physical refining of edible oils
US11427781B2 (en) Products produced from distillers corn oil
CN107216946A (en) The minimizing technology of plasticiser in a kind of fish oil
WO2020024645A1 (en) Refining process for improving stability and safety of microbial oil
CN111057616A (en) Treatment method for removing impurities from waste animal and vegetable oil
JP2012514470A (en) Cooking oil refining
CN113201397B (en) Method for reducing plasticizer content in fish oil product
KR100972703B1 (en) Improvements in or relating to separation technology
CN104830525B (en) A kind of multi-stage countercurrent of antarctic krill oil continuously leaches and process for purification
CN106966902A (en) A kind of preparation method of alpha linolenic acid ethyl ester
JPH09157684A (en) Purification of highly unsaturated fatty acid ester
CN103382413B (en) Refining process for reducing content of MCPD in tea seed oil
CN110055137B (en) Method for efficiently removing peculiar smell in ethyl ester type polyunsaturated fatty acid oil
CN105481682A (en) Method for preparing high-content conjugated linoleic acid using vegetable oil as raw material by means of purification
CN104673498B (en) Treatment method of adsorbent with grease adsorbed
WO2016037451A1 (en) Fixed bed decolorization process for unsaturated fatty acid
JP2000175696A (en) Extraction of dunaliella alga body
CN108760910B (en) Enzyme-assisted extraction method and detection method of krill phospholipid shrimp sauce
JP6990174B2 (en) Method for Producing Polyunsaturated Fatty Acid-Containing Composition
CN105585552A (en) Decoloration and purification method for vitamin E
CN112430500A (en) Method for reducing anisidine value in polyunsaturated fatty acid oil
Pando et al. Concentrating n-3 fatty acids from crude and refined commercial salmon oil
CN106833887A (en) A kind of production method of healthy grease and products thereof
JPH0780834B2 (en) Carotene recovery method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20170929

RJ01 Rejection of invention patent application after publication