CN104689793A - Special aflatoxin efficient adsorbent for peanut oil and preparation method thereof - Google Patents
Special aflatoxin efficient adsorbent for peanut oil and preparation method thereof Download PDFInfo
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- 235000019483 Peanut oil Nutrition 0.000 title claims abstract description 34
- 239000000312 peanut oil Substances 0.000 title claims abstract description 34
- 229930195730 Aflatoxin Natural products 0.000 title claims abstract description 31
- 239000005409 aflatoxin Substances 0.000 title claims abstract description 31
- XWIYFDMXXLINPU-UHFFFAOYSA-N Aflatoxin G Chemical compound O=C1OCCC2=C1C(=O)OC1=C2C(OC)=CC2=C1C1C=COC1O2 XWIYFDMXXLINPU-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 239000003463 adsorbent Substances 0.000 title claims abstract description 29
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 claims abstract description 61
- 229910052901 montmorillonite Inorganic materials 0.000 claims abstract description 34
- 239000003607 modifier Substances 0.000 claims abstract description 32
- 239000002994 raw material Substances 0.000 claims abstract description 6
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 150000003839 salts Chemical class 0.000 claims abstract description 4
- 239000008367 deionised water Substances 0.000 claims description 31
- 229910021641 deionized water Inorganic materials 0.000 claims description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 239000000725 suspension Substances 0.000 claims description 12
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical group [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 10
- 238000012986 modification Methods 0.000 claims description 9
- 230000004048 modification Effects 0.000 claims description 9
- VBIIFPGSPJYLRR-UHFFFAOYSA-M Stearyltrimethylammonium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCCCC[N+](C)(C)C VBIIFPGSPJYLRR-UHFFFAOYSA-M 0.000 claims description 6
- 239000002244 precipitate Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 239000006228 supernatant Substances 0.000 claims description 6
- 238000005342 ion exchange Methods 0.000 claims description 5
- 239000011259 mixed solution Substances 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 5
- WOWHHFRSBJGXCM-UHFFFAOYSA-M cetyltrimethylammonium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCC[N+](C)(C)C WOWHHFRSBJGXCM-UHFFFAOYSA-M 0.000 claims description 4
- CEYYIKYYFSTQRU-UHFFFAOYSA-M trimethyl(tetradecyl)azanium;chloride Chemical compound [Cl-].CCCCCCCCCCCCCC[N+](C)(C)C CEYYIKYYFSTQRU-UHFFFAOYSA-M 0.000 claims description 4
- DDXLVDQZPFLQMZ-UHFFFAOYSA-M dodecyl(trimethyl)azanium;chloride Chemical group [Cl-].CCCCCCCCCCCC[N+](C)(C)C DDXLVDQZPFLQMZ-UHFFFAOYSA-M 0.000 claims description 3
- 238000001179 sorption measurement Methods 0.000 abstract description 11
- -1 alkyl quaternary ammonium salts Chemical class 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000446 fuel Substances 0.000 abstract description 3
- 235000015097 nutrients Nutrition 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 8
- 235000019198 oils Nutrition 0.000 description 8
- 239000000243 solution Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 5
- 235000013305 food Nutrition 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 101710134784 Agnoprotein Proteins 0.000 description 3
- 229960000892 attapulgite Drugs 0.000 description 3
- 239000000440 bentonite Substances 0.000 description 3
- 229910000278 bentonite Inorganic materials 0.000 description 3
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 3
- 239000004927 clay Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 239000012065 filter cake Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229910052625 palygorskite Inorganic materials 0.000 description 3
- 239000000049 pigment Substances 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 229910052570 clay Inorganic materials 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910017053 inorganic salt Inorganic materials 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000003053 toxin Substances 0.000 description 2
- 231100000765 toxin Toxicity 0.000 description 2
- 108700012359 toxins Proteins 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 241001553178 Arachis glabrata Species 0.000 description 1
- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 241000228197 Aspergillus flavus Species 0.000 description 1
- 241000228230 Aspergillus parasiticus Species 0.000 description 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- CQBLUJRVOKGWCF-UHFFFAOYSA-N [O].[AlH3] Chemical compound [O].[AlH3] CQBLUJRVOKGWCF-UHFFFAOYSA-N 0.000 description 1
- OBNDGIHQAIXEAO-UHFFFAOYSA-N [O].[Si] Chemical compound [O].[Si] OBNDGIHQAIXEAO-UHFFFAOYSA-N 0.000 description 1
- 230000007059 acute toxicity Effects 0.000 description 1
- 231100000403 acute toxicity Toxicity 0.000 description 1
- OQIQSTLJSLGHID-WNWIJWBNSA-N aflatoxin B1 Chemical compound C=1([C@@H]2C=CO[C@@H]2OC=1C=C(C1=2)OC)C=2OC(=O)C2=C1CCC2=O OQIQSTLJSLGHID-WNWIJWBNSA-N 0.000 description 1
- 125000005211 alkyl trimethyl ammonium group Chemical group 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 230000034994 death Effects 0.000 description 1
- 231100000517 death Toxicity 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 201000007270 liver cancer Diseases 0.000 description 1
- 208000014018 liver neoplasm Diseases 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- NNFCIKHAZHQZJG-UHFFFAOYSA-N potassium cyanide Chemical compound [K+].N#[C-] NNFCIKHAZHQZJG-UHFFFAOYSA-N 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 229930000044 secondary metabolite Natural products 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/305—Addition of material, later completely removed, e.g. as result of heat treatment, leaching or washing, e.g. for forming pores
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/46—Materials comprising a mixture of inorganic and organic materials
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Fats And Perfumes (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
本发明涉及一种花生油专用黄曲霉毒素高效吸附剂及其制备方法;是以蒙脱土原土为原料,先通过无机盐进行无机改性,再利用有机烷基季氨盐进行有机改性,最后过滤、干燥制得。各组分按重量比为:蒙脱土75-85%、无机改性剂2-5%、有机改性剂10-20%。本发明制备的黄曲霉毒素吸附剂,能专一性的高效吸附花生油中污染的黄曲霉毒素,具有生产成本低、吸附效率高、营养成分损失少、油耗低等优点。
The invention relates to a high-efficiency aflatoxin adsorbent for peanut oil and a preparation method thereof. The raw material is montmorillonite, which is firstly modified inorganically by inorganic salts, and then organically modified by organic alkyl quaternary ammonium salts. Finally, it is obtained by filtering and drying. The weight ratio of each component is: 75-85% of montmorillonite, 2-5% of inorganic modifier, and 10-20% of organic modifier. The aflatoxin adsorbent prepared by the invention can specifically and efficiently adsorb the aflatoxin contaminated in peanut oil, and has the advantages of low production cost, high adsorption efficiency, less loss of nutrients, low fuel consumption, and the like.
Description
(一)技术领域(1) Technical field
本发明涉及一种花生油专用黄曲霉毒素高效吸附剂及其制备方法,属于食品加工与安全控制领域。The invention relates to a special aflatoxin high-efficiency adsorbent for peanut oil and a preparation method thereof, belonging to the field of food processing and safety control.
(二)背景技术(2) Background technology
黄曲霉毒素是由黄曲霉和寄生曲霉产生次生代谢产物,对人和动物具有很强的毒性和致癌性,尤其是黄曲霉毒素B1,其急性毒性是氰化钾的10倍,砒霜的68倍,是迄今发现的最强的化学致癌物。花生是最易受其污染的粮油作物之一,其制品花生油污染黄曲霉毒素的情况一直引起人们的关注。近几年,国内外因食用黄曲霉毒素污染的粮油制品而导致的肝癌患病人数和死亡人数逐年增加,并造成巨大的经济损失,严重阻碍了粮油食品的进出口。因此,研究并开发预防和控制花生油中黄曲霉毒素的技术和产品是非常必要的。Aflatoxins are secondary metabolites produced by Aspergillus flavus and Aspergillus parasiticus, which are highly toxic and carcinogenic to humans and animals, especially aflatoxin B 1 , whose acute toxicity is 10 times that of potassium cyanide, and arsenic 68 times, is the strongest chemical carcinogen found so far. Peanut is one of the most susceptible grain and oil crops to be contaminated by aflatoxins, and the contamination of aflatoxin in peanut oil, its product, has always attracted people's attention. In recent years, the number of liver cancer patients and deaths caused by eating aflatoxin-contaminated grain and oil products at home and abroad has increased year by year, causing huge economic losses and seriously hindering the import and export of grain, oil and food. Therefore, it is very necessary to research and develop technologies and products for the prevention and control of aflatoxins in peanut oil.
目前,减少黄曲霉毒素最有效、可行、成本低的方法就是使用毒素吸附剂。将吸附剂添加在食物中吸附毒素,然后再将吸附剂通过过滤或离心法去除。当前,利用吸附剂来脱除饲料中污染的黄曲霉毒素已得到广泛研究和应用,但在食用油中应用很少。At present, the most effective, feasible and low-cost method to reduce aflatoxins is to use toxin adsorbents. Adsorbents are added to food to absorb toxins, and then the adsorbents are removed by filtration or centrifugation. At present, the use of adsorbents to remove aflatoxin from feed contamination has been widely studied and applied, but it is rarely used in edible oil.
然而,专用于花生油中黄曲酶毒素高效吸附剂研究开发的很少,并且已有的吸附剂存在吸附性能低、吸附种类少、且吸附后的花生油营养及重量损失大。以蒙脱土为主要原料,通过无机和有机混合改性后,可以显著提高蒙脱土对黄曲霉毒素的吸附性能,减少花生油中微量元素和维生素的损失,减少油的损耗。However, there are few high-efficiency adsorbents dedicated to the research and development of aflatoxin in peanut oil, and the existing adsorbents have low adsorption performance, few adsorption types, and large nutritional and weight loss of peanut oil after adsorption. Using montmorillonite as the main raw material, after inorganic and organic mixed modification, can significantly improve the adsorption performance of montmorillonite to aflatoxin, reduce the loss of trace elements and vitamins in peanut oil, and reduce the loss of oil.
(三)发明内容(3) Contents of the invention
本发明提供一种花生油专用黄曲霉毒素高效吸附剂及其制备方法。本发明制备的黄曲霉毒素吸附剂,能专一性的高效吸附花生油中污染的黄曲霉毒素,具有生产成本低、吸附效率高、营养成分损失少、油耗低等优点。The invention provides a special aflatoxin high-efficiency adsorbent for peanut oil and a preparation method thereof. The aflatoxin adsorbent prepared by the invention can specifically and efficiently adsorb the aflatoxin polluted in peanut oil, and has the advantages of low production cost, high adsorption efficiency, less loss of nutrients, low fuel consumption, and the like.
一种花生油专用黄曲霉毒素高效吸附剂,各组分按重量比为:蒙脱土75-85%、无机改性剂2-5%、有机改性剂10-20%,各组分重量百分比之和为100%。A special aflatoxin high-efficiency adsorbent for peanut oil, the weight ratio of each component is: montmorillonite 75-85%, inorganic modifier 2-5%, organic modifier 10-20%, the weight percentage of each component The sum is 100%.
所述的无机改性剂是NaCl、Na2CO3或AlCl3。The inorganic modifier is NaCl, Na 2 CO 3 or AlCl 3 .
所述的有机改性剂为有机烷基季氨盐,包括C12-C20脂肪族季氨盐,即十二烷基三甲基氯化铵、十四烷基三甲基氯化铵、十六烷基三甲基氯化铵或十八烷基三甲基氯化铵等烷基季氨盐。The organic modifier is organic alkyl quaternary ammonium salt, including C 12 -C 20 aliphatic quaternary ammonium salt, namely dodecyl trimethyl ammonium chloride, tetradecyl trimethyl ammonium chloride, Alkyl quaternary ammonium salts such as cetyltrimethylammonium chloride or octadecyltrimethylammonium chloride.
所述蒙脱土的主要成分蒙脱石属于2:1型三层结构的层状硅酸盐粘土矿物,其单位晶胞由两层硅氧四面体夹一层铝氧八面体组成。四面体与八面体通过共用氧原子相连接,晶胞平行叠置,晶格中Al3+和Si4+离子容易被其他低价阳离子所取代,发生同晶置换。The main component of the montmorillonite is montmorillonite, which is a layered silicate clay mineral with a 2:1 three-layer structure, and its unit cell is composed of two layers of silicon-oxygen tetrahedron sandwiching a layer of aluminum-oxygen octahedron. The tetrahedron and octahedron are connected by sharing oxygen atoms, and the unit cells are stacked in parallel. Al 3+ and Si 4+ ions in the lattice are easily replaced by other low-valent cations, resulting in isomorphic replacement.
本发明还涉及一种花生油专用黄曲霉毒素高效吸附剂的制备方法,是以蒙脱土为原料,先通过无机盐进行无机改性,再利用有机烷基季氨盐进行有机改性,最后过滤、干燥制得。各组分按重量比为:蒙脱土75-85%、无机改性剂2-5%、有机改性剂10-20%,各组分重量百分比之和为100%;具体包括以下步骤:The present invention also relates to a preparation method of a special aflatoxin high-efficiency adsorbent for peanut oil, which uses montmorillonite as the raw material, first carries out inorganic modification with inorganic salt, then uses organic alkyl quaternary ammonium salt for organic modification, and finally filters the , obtained by drying. The weight ratio of each component is: 75-85% of montmorillonite, 2-5% of inorganic modifier, 10-20% of organic modifier, and the sum of the weight percentages of each component is 100%; specifically, the following steps are included:
1、无机改性:去离子水升温至60℃,按照蒙脱土:去离子水=1:5(W/V)比例将蒙脱土缓慢加入到去离子水中,转速300r/min搅拌均匀,形成蒙脱土悬浮液。将蒙脱土重量比2-5%的无机改性剂使用60℃去离子水(不超过本步骤前面所述去离子水体积比的1/10,能将无机改性剂溶解即可)溶解,并缓慢、均匀的加入到蒙脱土悬浮液中,保温反应2h,离子交换后的混合液于3000r/min离心10min,弃去上清液,沉淀用去离子水清洗并离心除去过量的无机盐,获得无机改性蒙脱土;所述的无机改性剂是NaCl、Na2CO3或AlCl3。1. Inorganic modification: heat up the deionized water to 60°C, slowly add the montmorillonite to the deionized water according to the ratio of montmorillonite: deionized water = 1:5 (W/V), and stir evenly at a speed of 300r/min. A montmorillonite suspension is formed. Dissolve the inorganic modifier with a weight ratio of 2-5% of the montmorillonite using 60°C deionized water (not exceeding 1/10 of the volume ratio of the deionized water described above in this step, as long as the inorganic modifier can be dissolved) , and slowly and evenly added to the montmorillonite suspension, kept for 2 hours, the ion-exchanged mixture was centrifuged at 3000r/min for 10 minutes, the supernatant was discarded, the precipitate was washed with deionized water and centrifuged to remove excess inorganic salt to obtain inorganic modified montmorillonite; the inorganic modifier is NaCl, Na 2 CO 3 or AlCl 3 .
2、有机改性:将步骤1中获得的无机改性蒙脱土,按照无机改性蒙脱土:去离子水=1:5(W/V)比例加入去离子水中,调节温度至60℃,搅拌转速300r/min,并制成均匀的无机改性蒙脱土悬浮液。再将无机改性蒙脱土重量比5-15%的有机改性剂使用60℃去离子水(不超过本步骤前面所述去离子水体积比的1/10,能将有机改性剂溶解即可)溶解,再缓慢加入到无机改性蒙脱土悬浮液中反应2h进行离子交换,离子交换后的混合液于3000r/min离心10min,弃去上清液,沉淀用去离子水清洗并离心除去过量的有机改性剂,获得无机-有机改性蒙脱土;所述的有机改性剂为有机烷基季氨盐,包括C12-C20脂肪族季氨盐,即十二烷基三甲基氯化铵、十四烷基三甲基氯化铵、十六烷基三甲基氯化铵或十八烷基三甲基氯化铵等烷基季氨盐。2. Organic modification: add the inorganic modified montmorillonite obtained in step 1 to deionized water according to the ratio of inorganic modified montmorillonite: deionized water=1:5 (W/V), and adjust the temperature to 60°C , the stirring speed is 300r/min, and a uniform inorganic modified montmorillonite suspension is prepared. Then use 60 DEG C of deionized water (not more than 1/10 of the volume ratio of deionized water described earlier in this step to dissolve the organic modifier with the weight ratio of inorganic modified montmorillonite 5-15%) can be) dissolved, then slowly added to the inorganic modified montmorillonite suspension and reacted for 2h to carry out ion exchange, the mixed solution after ion exchange was centrifuged at 3000r/min for 10min, the supernatant was discarded, the precipitate was washed with deionized water and The excess organic modifier is removed by centrifugation to obtain inorganic-organic modified montmorillonite; the organic modifier is an organic alkyl quaternary ammonium salt, including C 12 -C 20 aliphatic quaternary ammonium salt, i.e. dodecane Alkyl trimethyl ammonium chloride, tetradecyl trimethyl ammonium chloride, cetyl trimethyl ammonium chloride or octadecyl trimethyl ammonium chloride and other alkyl quaternary ammonium salts.
3、过滤和干燥:将步骤2)获得的无机-有机混合改性的蒙脱土,60℃烘干至颜色由灰色变成纯白色,过200目筛,得到花生油专用黄曲霉毒素高效吸附剂。3. Filtration and drying: Dry the inorganic-organic mixed modified montmorillonite obtained in step 2) at 60°C until the color changes from gray to pure white, and pass through a 200-mesh sieve to obtain a high-efficiency aflatoxin adsorbent for peanut oil .
本发明具有如下优点:The present invention has the following advantages:
1、本发明中使用的蒙脱土为天然硅铝酸盐,原料来源丰富,生产成本低。1. The montmorillonite used in the present invention is natural aluminosilicate, which has abundant sources of raw materials and low production cost.
2、本发明制备的花生油专用黄曲霉毒素高效吸附剂具有投资小、制备简单、污染小、生产效率高、可重复利用等优势。2. The special aflatoxin high-efficiency adsorbent for peanut oil prepared by the present invention has the advantages of small investment, simple preparation, low pollution, high production efficiency, and reusability.
3、本发明制备的花生油专用黄曲霉毒素高效吸附剂具有较高的吸附性能、专一性强、营养损失少、油耗低等优点。3. The special-purpose aflatoxin high-efficiency adsorbent for peanut oil prepared by the present invention has the advantages of high adsorption performance, strong specificity, less nutrient loss, and low fuel consumption.
(四)附图说明(4) Description of drawings
图1为常见吸附剂与本发明制备的改性蒙脱土对AFB1吸附效果比较图Fig. 1 is common adsorbent and the modified montmorillonite prepared by the present invention compares the adsorption effect of AFB 1
图1中的试验结果说明常用吸附剂(白土、蒙脱土、膨润土和凹凸棒)都能有效去除花生油中的黄曲霉毒素,但仍达不到国家对花生油中黄曲霉毒素残留的限量要求(20ug/kg);而经过本发明制备的改性蒙脱土能将黄曲霉毒素降低到20ug/kg以下。The test results in Fig. 1 show that commonly used adsorbents (clay, montmorillonite, bentonite and attapulgite) can effectively remove aflatoxin in peanut oil, but still fall short of the national limit requirements for aflatoxin residues in peanut oil ( 20ug/kg); and the modified montmorillonite prepared by the present invention can reduce aflatoxin to below 20ug/kg.
(五)具体实施方式(5) Specific implementation methods
本发明所述的无机改性剂均为分析纯,所述的蒙脱土为蒙脱土原土,均可市购得到。The inorganic modifiers described in the present invention are all analytically pure, and the described montmorillonite is montmorillonite raw soil, which can be purchased commercially.
实施例1:量取7.5L去离子水加入到反应釜中,设置并升温至60℃,调节转速至300r/min;将400g蒙脱土缓慢加入到反应釜中,形成蒙脱土悬浮液。取16g NaCl溶于60℃、0.5L去离子水中,并缓慢、均匀的加入到反应釜中,待反应2h后,离子交换后的混合液于3000r/min离心10min,弃去上清液,沉淀用去离子水清洗并离心除去过量的无机盐,获得无机改性的蒙脱土。向无机改性后的蒙脱土中加入7.5L的60℃的去离子水制成分散悬浮液;取68g十八烷基三甲基氯化铵溶于60℃的去离子水中,再将该有机改性剂溶液缓慢加入到反应釜中,搅拌转速300r/min,60℃处理2h。将反应液离心,清洗至用0.1mol/L的AgNO3未能检测出氯离子的存在。将滤饼置于60℃烘箱中干燥24h,过200目筛,取筛下物于密闭容器内存放。Example 1: Measure 7.5L of deionized water into the reactor, set and raise the temperature to 60°C, and adjust the rotation speed to 300r/min; slowly add 400g of montmorillonite into the reactor to form a montmorillonite suspension. Dissolve 16g NaCl in 0.5L deionized water at 60°C, and slowly and evenly add it to the reactor. After 2 hours of reaction, centrifuge the ion-exchanged mixture at 3000r/min for 10 minutes, discard the supernatant, and precipitate Rinse with deionized water and centrifuge to remove excess inorganic salts to obtain inorganically modified montmorillonite. Add 7.5L of deionized water at 60°C to the inorganically modified montmorillonite to make a dispersion suspension; dissolve 68g of octadecyltrimethylammonium chloride in deionized water at 60°C, and then The organic modifier solution was slowly added into the reaction kettle, the stirring speed was 300r/min, and the treatment was carried out at 60°C for 2h. The reaction solution was centrifuged and washed until the presence of chloride ions could not be detected with 0.1mol/L AgNO 3 . Dry the filter cake in an oven at 60°C for 24 hours, pass through a 200-mesh sieve, and store the under-screened material in an airtight container.
实施例2:量取7.5L去离子水加入到反应釜中,设置并升温至60℃,调节转速至300r/min;将250g蒙脱土缓慢加入到反应釜中,形成蒙脱土悬浮液。取12.5g Na2CO3溶于60℃、0.5L去离子水中,并缓慢、均匀的加入到反应釜中,待反应2h后,离子交换后的混合液于3000r/min离心10min,弃去上清液,沉淀用去离子水清洗并离心除去过量的无机盐,获得无机改性的蒙脱土。向无机改性后的蒙脱土中加入7.5L的60℃的去离子水制成分散悬浮液;取45g十八烷基三甲基氯化铵溶于0.5L、60℃的去离子水中,再将该有机改性剂溶液缓慢加入到反应釜中,搅拌转速300r/min,60℃处理2h。将反应液离心,清洗至用0.1mol/L的AgNO3未能检测出氯离子的存在。将滤饼置于60℃烘箱中干燥24h,过200目筛,取筛下物于密闭容器内存放。Example 2: Measure 7.5L of deionized water into the reactor, set and raise the temperature to 60°C, and adjust the rotation speed to 300r/min; slowly add 250g of montmorillonite into the reactor to form a montmorillonite suspension. Dissolve 12.5g Na 2 CO 3 in 0.5L deionized water at 60°C, and slowly and evenly add it to the reaction kettle. After 2 hours of reaction, the ion-exchanged mixture is centrifuged at 3000r/min for 10 minutes, and discarded. The supernatant liquid and the precipitate were washed with deionized water and centrifuged to remove excess inorganic salts to obtain inorganically modified montmorillonite. Add 7.5L of deionized water at 60°C to the inorganically modified montmorillonite to make a dispersion suspension; dissolve 45g of octadecyltrimethylammonium chloride in 0.5L of deionized water at 60°C, Then the organic modifier solution was slowly added into the reaction kettle, the stirring speed was 300r/min, and the mixture was treated at 60°C for 2h. The reaction solution was centrifuged and washed until the presence of chloride ions could not be detected with 0.1mol/L AgNO 3 . Dry the filter cake in an oven at 60°C for 24 hours, pass through a 200-mesh sieve, and store the under-sieve in an airtight container.
实施例3:0.5M的Na2CO3缓慢加入到1.0M的AlCl3溶液中,并快速搅拌24h,并最终使OH-/Al3+=2.4,得到Al13溶液;再将5g的十六烷基三甲基氯化铵(1631)缓慢加入到上述Al13溶液中,并快速搅拌2h,得到Al-OH-1631混合溶液;取30g蒙脱土缓慢加入到Al-OH-1631混合溶液中,并快速搅拌24h;反应后的溶液过滤,再用60℃的去离子水洗涤至用0.1mol/L的AgNO3未能检测出氯离子的存在。将滤饼置于60℃烘箱中干燥24h,过200目筛,取筛下物于密闭容器内存放。Example 3: 0.5M Na 2 CO 3 was slowly added to 1.0M AlCl 3 solution, and stirred rapidly for 24 hours, and finally made OH - /Al 3+ =2.4 to obtain Al 13 solution; Alkyltrimethylammonium chloride (1631) was slowly added to the above Al 13 solution, and stirred rapidly for 2 hours to obtain a mixed solution of Al-OH-1631; 30g of montmorillonite was slowly added to the mixed solution of Al-OH-1631 , and stirred rapidly for 24 hours; the reacted solution was filtered, and then washed with deionized water at 60°C until the presence of chloride ions could not be detected with 0.1mol/L AgNO 3 . Dry the filter cake in an oven at 60°C for 24 hours, pass through a 200-mesh sieve, and store the under-sieve in an airtight container.
验证例:Verification example:
为了更好的阐述本发明花生油专用黄曲霉毒素高效吸附剂(即改性蒙脱土)的优势和特点,我们比较了油脂企业常用吸附剂与本发明产品在吸附性能方面的优势。In order to better illustrate the advantages and characteristics of the high-efficiency aflatoxin adsorbent for peanut oil (i.e. modified montmorillonite) of the present invention, we compared the adsorption properties of the commonly used adsorbents used by oil companies and the product of the present invention.
在油脂精炼环节,油脂企业常用白土、蒙脱土、膨润土、凹凸棒做为色素吸附剂,这些吸附剂在吸附油中色素的同时,也将部分黄曲霉毒素除去。常见吸附剂与改性蒙脱土对花生油中AFB1吸附效果见如图1(上述四种色素吸附剂添加量均为花生油重量比的2.5%)。花生油原料中AFB1为389.09ug/kg,经白土吸附后,花生油中AFB1的含量降低到23.30ug/kg;经蒙脱土吸附后,花生油中AFB1的降低到24.53ppb;经膨润土附后,花生油中AFB1的含量降低到21.60ug/kg;经凹凸棒吸附后,花生油中AFB1的含量降低到36.46ug/kg;经膨润土附后,花生油中AFB1的含量降低到21.60ug/kg;而经本发明制备的改性蒙脱土吸附后,花生油中AFB1的降低到11.81ug/kg。试验结果说明常用吸附剂都能有效去除花生油中的黄曲霉毒素,但仍达不到国家对花生油中黄曲霉毒素残留的限量要求(20ug/kg);而经过本发明制备的改性蒙脱土能将黄曲霉毒素降低到20ug/kg以下。这说明经过改性后的蒙脱土更能有效脱除花生油中黄曲霉毒素,满足食品安全的要求。In the oil refining process, oil companies often use white clay, montmorillonite, bentonite, and attapulgite as pigment adsorbents. These adsorbents can also remove part of aflatoxin while adsorbing pigments in oil. The adsorption effects of common adsorbents and modified montmorillonite on AFB 1 in peanut oil are shown in Figure 1 (the addition amount of the above four pigment adsorbents is 2.5% of the weight ratio of peanut oil). AFB 1 in peanut oil raw material is 389.09ug/kg, after being adsorbed by white clay, the content of AFB 1 in peanut oil is reduced to 23.30ug/kg; after being adsorbed by montmorillonite, the content of AFB 1 in peanut oil is reduced to 24.53ppb; , the content of AFB 1 in peanut oil decreased to 21.60ug/kg; after being adsorbed by attapulgite, the content of AFB 1 in peanut oil decreased to 36.46ug/kg; after being attached by bentonite, the content of AFB 1 in peanut oil decreased to 21.60ug/kg and after the adsorption of modified montmorillonite prepared by the present invention, AFB 1 in peanut oil was reduced to 11.81ug/kg. Result of the test shows that commonly used adsorbents can effectively remove the aflatoxin in peanut oil, but still fall short of the country's limit requirement (20ug/kg) to aflatoxin residues in peanut oil; and through the modified montmorillonite prepared by the present invention Can reduce aflatoxin to below 20ug/kg. This shows that the modified montmorillonite can more effectively remove aflatoxin from peanut oil and meet the requirements of food safety.
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CN108342252A (en) * | 2018-01-19 | 2018-07-31 | 中山职业技术学院 | A kind of method of high efficiency extraction agilawood essential oil |
CN108342252B (en) * | 2018-01-19 | 2021-05-28 | 中山职业技术学院 | Method for efficiently extracting agilawood essential oil |
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