CN105441186A - Process for removing AFB1 in edible vegetable oil - Google Patents
Process for removing AFB1 in edible vegetable oil Download PDFInfo
- Publication number
- CN105441186A CN105441186A CN201510784851.4A CN201510784851A CN105441186A CN 105441186 A CN105441186 A CN 105441186A CN 201510784851 A CN201510784851 A CN 201510784851A CN 105441186 A CN105441186 A CN 105441186A
- Authority
- CN
- China
- Prior art keywords
- vegetable oil
- oil
- edible vegetable
- afb1
- afb
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B3/00—Refining fats or fatty oils
- C11B3/10—Refining fats or fatty oils by adsorption
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
- A23D9/04—Working-up
Abstract
The invention discloses a process for removing AFB1 in edible vegetable oil, which comprises the following steps: mixing silicon dioxide, hydrated alumina, sodium hydroxide and water in a mass ratio of (25-35%): (0.5-1%): (5-9%): (55-65%), and heating the obtained mixture for 1-10h in an autoclave so as to separate out molecular sieve crystals; weighting 90-99% of edible oil, heating to 40-80 DEG C, adding 1-10% of the molecular sieve crystals, uniformly mixing, continuing to stir, and filtering the obtained object while the object is hot, so that edible vegetable oil from which AFB1 is removed is obtained, wherein the heating time is 10 min-2 h. According to the invention, AFB1 in edible vegetable oil can be significantly reduced, thereby effectively ensuring the edible security of oil products; the process is simple in operation, and can be implemented without adding more equipment, therefore, the process can be energetically popularized; and through the process, the AFB1 removal rate can reach 90%.
Description
Technical field
The invention belongs to edible vegetable oil complete processing field, be specifically related to AFB in a kind of removal edible vegetable oil
1technique.
Background technology
Aflatoxin is the toxin of growth and breeding after flavus and Aspergillus parasiticus contaminated food.These two kinds of moulds, at occurring in nature ubiquity, are easy to contaminated food products.Aflatoxin affects the pollution of food and degree thereof the different condition by area and seasonal factor and plant growth, results, storage, processing.The farm crop such as peanut, corn are very easy to infected by Aspergillus flavus, aflatoxin is the toxoid produced by flavus and Aspergillus parasiticus metabolism, within 1999, is delimited as one of the strongest known carcinogenic chemical by the Agency for Research on Cancer of the World Health Organization (WHO).The aflatoxin identified at present has B
1, B
2, G
1, G
2, M
1, M
2, P
1, Q
1deng kind more than ten, wherein with AFB
1toxicity and carinogenicity the strongest.
On August 1st, 2003 rises, all enterprises being engaged in rice, face, oil, soy sauce, vinegar process for processing in China within the border, and its product must through going on the market after the assay was approved, AFB
1must detect.National standard " edible vegetable oil hygienic standard " GB2716-2005 specifies: AFB in peanut oil, Semen Maydis oil
1must not more than 20 μ g/Kg, AFB in other plant oil
1must not more than 10 μ g/Kg; State food pharmaceuticals administration general bureau surveys sample edible vegetable oil, AFB in peanut oil
1again and again occur exceeding standard.
AFB in current removal edible vegetable oil
1method mainly contain: physical method, chemical process, biological method.Physical method comprises absorption method and irradiation method.Absorption method adds sorbent material in peanut oil, the AFB in absorption peanut oil
1.The sorbent material of current employing has carclazyte, gac composite adsorption and Special adsorbent product, carclazyte, gac composite adsorption, because it is brought bilgy odour into and needs further high temperature, high vacuum deodorization process after adsorbing, are restricted at pressed oil and giving off a strong fragrance oil use.Pressed oil remains the intrinsic functional ingredient of grease in low temperature liquefaction process, and giving off a strong fragrance oil has strong fragrance, dark liking by consumers in general.Therefore, industry is badly in need of a kind of efficient, safe AFB1 removal sorbent material of exploitation and technique thereof.
Summary of the invention
The object of this invention is to provide AFB in a kind of removal edible vegetable oil
1technique, AFB
1clearance reaches 90%.
In order to realize above object, sorbent material used in the present invention is the molecular sieve crystal after hydrothermal synthesis method process.
AFB in a kind of removal edible vegetable oil
1technique, specifically implement according to following steps:
Step 1: silicon-dioxide, hydrated aluminum oxide, sodium hydroxide, water 25%-35%:0.5%-1%:5%-9%:55%-65% mixing in mass ratio, heats 1h-10h and separates out molecular sieve crystal in autoclave;
Step 2: the edible oil taking 90%-99%, heat 40 DEG C-80 DEG C, the molecular sieve crystal adding 1%-10% mixes, continue stir, heat-up time 10min-2h;
Step 3: after stirring, filtered while hot, obtains removing AFB
1edible vegetable oil.
The present invention adopts the SiO 2 molecular sieve crystal of independent development effectively can remove AFB in grease as sorbent material
1, this adsorbent amount is little, and filtration velocity is fast, and residual oil content is low, does not affect the local flavor of pressed oil and giving off a strong fragrance oil.Technological operation is simple, can realize, can widely popularize without the need to increasing more equipment.Remove AFB
1after good, the product of edible vegetable oil clear, taste flavor meet edible vegetable oil hygienic standard, AFB
1clearance can reach 90%.
Embodiment
Embodiment 1
By the 26%:1%:8%:65% ratio mixing in mass ratio of silicon-dioxide, hydrated aluminum oxide, sodium hydroxide and water, in autoclave, heat 3h separate out molecular sieve crystal.Take 0.99kg containing AFB
1peanut oil, be heated to 50 DEG C, add 0.01kg molecular sieve crystal and mix, continue stir, heat-up time 20min, filtered while hot obtain remove AFB
1peanut oil.
The result of front and back removed by table 1
Result (μ g/kg) before process | Result (μ g/kg) after process | Clearance |
42.68 | 3.37 | 92.1% |
Embodiment 2
By the 30%:0.5%:8%:61.5% ratio mixing in mass ratio of silicon-dioxide, hydrated aluminum oxide, sodium hydroxide and water, in autoclave, heat 5h separate out molecular sieve crystal.Take 0.90kg containing AFB
1semen Maydis oil, be heated to 70 DEG C, add 0.1kg molecular sieve crystal and mix, continue stir, heat-up time 80min, filtered while hot obtain remove AFB
1semen Maydis oil.
The result of front and back removed by table 2
Result (μ g/kg) before process | Result (μ g/kg) after process | Clearance |
47.95 | 3.07 | 93.6% |
Embodiment 3
By the 35%:0.7%:6%:58.3% ratio mixing in mass ratio of silicon-dioxide, hydrated aluminum oxide, sodium hydroxide and water, in autoclave, heat 8h separate out molecular sieve crystal.Take 0.94kg containing AFB
1semen Maydis oil, be heated to 65 DEG C, add 0.06kg molecular sieve crystal and mix, continue stir, heat-up time 1.5h, filtered while hot obtain remove AFB
1semen Maydis oil.
The result of front and back removed by table 3
Result (μ g/kg) before process | Result (μ g/kg) after process | Clearance |
40.19 | 2.68 | 93.3% |
Claims (1)
1. remove AFB in edible vegetable oil for one kind
1technique, it is characterized in that, implement according to following steps:
Step 1: by the 25%-35%:0.5%-1%:5%-9%:55%-65% mixing in mass ratio of silicon-dioxide, hydrated aluminum oxide, sodium hydroxide, water, heat 1h-10h and separate out molecular sieve crystal in autoclave;
Step 2: the edible oil taking 90%-99%, heat 40 DEG C-80 DEG C, the molecular sieve crystal adding 1%-10% mixes, continue stir, heat-up time 10min-2h;
Step 3: after stirring, filtered while hot, obtains removing AFB
1edible vegetable oil.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510784851.4A CN105441186A (en) | 2015-11-16 | 2015-11-16 | Process for removing AFB1 in edible vegetable oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510784851.4A CN105441186A (en) | 2015-11-16 | 2015-11-16 | Process for removing AFB1 in edible vegetable oil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105441186A true CN105441186A (en) | 2016-03-30 |
Family
ID=55551835
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510784851.4A Pending CN105441186A (en) | 2015-11-16 | 2015-11-16 | Process for removing AFB1 in edible vegetable oil |
Country Status (1)
Country | Link |
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CN (1) | CN105441186A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109988671A (en) * | 2019-04-26 | 2019-07-09 | 盛廷新 | A kind of edible oil dry method alkali refining agent and preparation method thereof and application method |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1570056A (en) * | 2004-05-14 | 2005-01-26 | 东南大学 | Detergent adjuvant 4 zeolite molecular sieve preparation method |
CN101172244A (en) * | 2006-11-01 | 2008-05-07 | 中国石油化工股份有限公司 | Montmorillonite/Ymolecular sieve composite material and preparation method thereof |
CN101468801A (en) * | 2007-12-27 | 2009-07-01 | 中国石油化工股份有限公司 | Method for preparing Y type molecular sieve containing mesoporous |
CN102989416A (en) * | 2012-11-30 | 2013-03-27 | 中国农业科学院油料作物研究所 | Aflatoxin adsorbent and method for removing aflatoxins in edible vegetable oil |
CN103209606A (en) * | 2010-10-06 | 2013-07-17 | 塞拉尼斯醋酸纤维有限公司 | Smoke filters for smoking devices with porous masses having a carbon particle loading and an encapsulated pressure drop |
CN103420394A (en) * | 2013-09-01 | 2013-12-04 | 山东理工大学 | Method for preparing X-type molecular sieve with rice husks serving as silicon source |
-
2015
- 2015-11-16 CN CN201510784851.4A patent/CN105441186A/en active Pending
Patent Citations (6)
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CN1570056A (en) * | 2004-05-14 | 2005-01-26 | 东南大学 | Detergent adjuvant 4 zeolite molecular sieve preparation method |
CN101172244A (en) * | 2006-11-01 | 2008-05-07 | 中国石油化工股份有限公司 | Montmorillonite/Ymolecular sieve composite material and preparation method thereof |
CN101468801A (en) * | 2007-12-27 | 2009-07-01 | 中国石油化工股份有限公司 | Method for preparing Y type molecular sieve containing mesoporous |
CN103209606A (en) * | 2010-10-06 | 2013-07-17 | 塞拉尼斯醋酸纤维有限公司 | Smoke filters for smoking devices with porous masses having a carbon particle loading and an encapsulated pressure drop |
CN102989416A (en) * | 2012-11-30 | 2013-03-27 | 中国农业科学院油料作物研究所 | Aflatoxin adsorbent and method for removing aflatoxins in edible vegetable oil |
CN103420394A (en) * | 2013-09-01 | 2013-12-04 | 山东理工大学 | Method for preparing X-type molecular sieve with rice husks serving as silicon source |
Non-Patent Citations (2)
Title |
---|
叶盛群等: "食用油吸附脱色剂对植物油中黄曲霉毒素含量的影响", 《精细与专用化学品》 * |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109988671A (en) * | 2019-04-26 | 2019-07-09 | 盛廷新 | A kind of edible oil dry method alkali refining agent and preparation method thereof and application method |
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TA01 | Transfer of patent application right | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20191021 Address after: No. 86, Zaolin Road, Anning District, Lanzhou City, Gansu Province Applicant after: Lanzhou Runmin grain and Oil Co., Ltd Address before: 710082 No. 118 labour Road, Shaanxi, Xi'an Applicant before: Company limited of engineering research designing institute of Xi'an China Oil and Food Import and Export Corporation |
|
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20160330 |