CN102964381A - Production process of high-purity solid phytic acid - Google Patents

Production process of high-purity solid phytic acid Download PDF

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Publication number
CN102964381A
CN102964381A CN2012104934533A CN201210493453A CN102964381A CN 102964381 A CN102964381 A CN 102964381A CN 2012104934533 A CN2012104934533 A CN 2012104934533A CN 201210493453 A CN201210493453 A CN 201210493453A CN 102964381 A CN102964381 A CN 102964381A
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CN
China
Prior art keywords
phytic acid
liquid
value
purity
filtrate
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Pending
Application number
CN2012104934533A
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Chinese (zh)
Inventor
王少林
张红
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TONGXINAG XINYANG FOOD ADDITIVES CO Ltd
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TONGXINAG XINYANG FOOD ADDITIVES CO Ltd
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Priority to CN2012104934533A priority Critical patent/CN102964381A/en
Publication of CN102964381A publication Critical patent/CN102964381A/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Abstract

The invention discloses a production process of high-purity solid phytic acid. Degreased rice bran or corn meal is adopted, hydrochloric acid is used for soaking and leaching filtrate, filtering is carried out after NaOH or KOH is used for adjusting the pH value, and high-purity solid phytic acid is obtained by virtue of an anion exchange column, a cation exchange column and crystallization. According to the production process disclosed by the invention, technological innovation is realized, the purity of the prepared phytic acid can be up to more than 98%, and the problem that liquid phytic acid is darkened in a storage process can be effectively solved. The solid phytic acid produced by virtue of the production process is high in purity and white in colour, contains less impurities and is one of good additives in the food industry, and the solid phytic acid product has good oxidation resistance and is safe and non-toxic, so that the solid phytic acid is widely used as food preservative and antiseptic.

Description

A kind of high-purity solid phytic acid production technique
Technical field
The present invention relates to a kind of manufacture method of foodstuff additive, specifically refer to a kind of high-purity solid phytic acid production technique.
Background technology
Phytic acid is that a kind of important organophosphorus is additive, has unique physiological function and chemical property, has widespread use at aspects such as food, medicine, daily-use chemical industry, metal processing, textile industry, Polymeric Industry and plastic working industry.
In view of phytic acid has been widely used and higher economic worth, the research and development dynamics is all being strengthened in countries in the world.The phytic acid of selling on the market now mostly is greatly liquid phytic acid, and the liquid phytic acid of pure natural is difficult for storing.The liquid phytic acid the inside exists the materials such as protein, polysaccharide, natural pigment, potential pigment, iron ion so that phytic acid color and luster in storage process affects phytic acid outward appearance and application by the faint yellow Vandyke brown that becomes.Solid phytic acid purity is high, can not variable color, be convenient to store, convenient transportation, be the preferred product in following phytic acid market.
That high-purity solid phytic acid has solved is easy to change in the liquid phytic acid storage process, transportation inconvenience and the not high defective of purity.And liquid phytic acid very difficult application inside oil, solid phytic acid has solved this problem.Because phytic acid is to extract from natural rice bran, corn, so this product is nontoxic.Phytic acid is low as its addition of foodstuff additive, and the effect but additive than general chemosynthesis is good, therefore can replace the foodstuff additive of some chemosynthesis to be widely used in foodstuffs industry.Solid phytic acid is soluble in water, and the client can oneself allocate concentration and addition according to the variant production needs.
Summary of the invention
The present invention is in order to remedy the deficiency of existing air filter, a kind of high-purity solid phytic acid production technique is provided, has solved liquid phytic acid and in storage process, held allochroic problem, and improved greatly the purity of phytic acid, the convenient storage transported, and reduced transportation cost.
A kind of high-purity solid phytic acid production technique of the present invention is achieved through the following technical solutions:
A kind of high-purity solid phytic acid production technique may further comprise the steps successively:
(1) defatted rice bran or the corn dregs of rice are adjusted pH value to 3 with 6% hydrochloric acid, soak and quench 6-8 hour, and filtrate adds lime slurry neutralization, regulate pH value to 6 ~ 6.5 with NaOH, filter, abandon filtrate, and filter residue is phytin sodium crude product;
(2) in the water of phytin sodium crude product adding 6-10 doubly being measured, adjust pH value to 2.5 with hydrochloric acid soln, treat to dissolve fully, add activated carbon decolorizing filtration, desugar; Filtrate adds NaOH and adjusts the pH value to 3-4.5, separates out albumen, adopts filter method to separate and separates out albumen, gets filtrate;
(3) gained filtrate is advanced the exchange of weakly-basic anion exchange column, washing; Then use 4-8% alkali lye wash-out; Elutriant is adjusted the pH value to 12-14 with 4-8%NaOH or KOH solution, and sediment separate out contains iron ion in the throw out;
(4) liquid after the separation is crossed the cationic exchange coloum exchange, and effluent liquid advances macroporous anion exchange resin chromatography column chromatography, and it is concentrated that chromatographic solution advances upgrading tower, is concentrated to phytic acid content 50-70%, and concentrated solution adds activated carbon decolorizing, filters, and gets filtrate;
(5) liquid end product phytic acid: liquid phytic acid is concentrated into proportion 1.390, and adjusting pH value is 2, then puts into crystallizer and clarifies;
(6) overcritical stable: it is stable that liquid phytic acid is placed in the crystallizer clarification;
(7) alcohol wash-out: put into the alcohol washing in the liquid phytic acid, destroy the heteropolar bond of phytic acid and water, under the whipped state, decrease temperature crystalline leaches crystal, and is repeated multiple times, obtains the crystallization phytic acid.
As preferably, described alkali lye refers to NaOH or KOH solution.
As preferably, described gac dosage is 3 ~ 5%.
Compared with prior art, the beneficial effect of a kind of high-purity solid phytic acid production technique of the present invention is: can effectively solve the problem that liquid phytic acid darkens in storage process.The solid phytic acid purity of this explained hereafter is high, few, the white color of impurity, is one of additive good in the foodstuffs industry, and this product has good oxidation-resistance, and safety non-toxic, therefore is widely used as food preservative and sanitas.
Embodiment
Below by embodiment and the prescription the present invention is specifically described, the present invention includes, but be not limited to following listed embodiment.
Process program: defatted rice bran or the corn dregs of rice are adjusted pH value to 3 with 6% hydrochloric acid, soak and quench 6-8 hour, and filtrate adds lime slurry neutralization, regulate pH value to 6 ~ 6.5 with NaOH, filter, abandon filtrate, and filter residue is phytin sodium crude product; Phytin sodium crude product is added in the water of 8 times of amounts, adjust pH value to 2.5 with hydrochloric acid soln, treat to dissolve fully, add 4% activated carbon decolorizing filtration, desugar; Filtrate adds NaOH and adjusts the pH value to 3-4.5, separates out albumen, adopts filter method to separate and separates out albumen, gets filtrate;
Gained filtrate is advanced the exchange of weakly-basic anion exchange column, washing; Then use 4-8% alkali lye (NaOH or KOH) wash-out; Elutriant is adjusted the pH value to 12-14 with 4-8% NaOH or KOH solution, and sediment separate out contains iron ion in the throw out; Liquid after the separation is crossed the cationic exchange coloum exchange, and effluent liquid advances macroporous anion exchange resin chromatography column chromatography, and it is concentrated that chromatographic solution advances upgrading tower, is concentrated to phytic acid content 50-70%, and concentrated solution adds 4% activated carbon decolorizing, filters, and gets filtrate;
Liquid phytic acid is concentrated into proportion 1.390, and adjusting pH value is 2, then puts into crystallizer and clarifies; It is stable that liquid phytic acid is placed in the crystallizer clarification; Put into the alcohol washing in the liquid phytic acid, destroy the heteropolar bond of phytic acid and water, under the whipped state, decrease temperature crystalline leaches crystal, and is repeated multiple times, obtains the crystallization phytic acid.
It is centrifugal that the phytic acid powder is put into whizzer, and the setting centrifuge speed is 3500r/min; Phytic acid after centrifugal sieves, and some macrobeads or Impurity removal, guarantees that the phytic acid powder is even; Carry out 65 ℃ of dry oven dry of constant temperature and obtain final solid phytic acid, the baking tool is carried out cleaning, prevent from bringing into impurity, pollute phytic acid.The phytic acid powder is uniformly distributed in 65 ℃ of oven dry of constant temperature on the pallet; Chemically examine qualified product by every barrel of 25Kg packing.The package lining plastics bag should meet the foodstuff additive quality standard.Use the sealing of hot rolling sealing machine behind the every bag dress, to prevent that product is because of the moisture absorption caking that gets damp again.
Adopt high-purity solid phytic acid content that production technique of the present invention makes greater than 98%, content of inorganic phosphorus is less than 80ppm, and chloride content is below 100ppm, sulphate content is less than 100ppm, calcium salt content is less than 100ppm, and heavy metal content is below 30ppm, and arsenic content is below 3ppm.

Claims (3)

1. high-purity solid phytic acid production technique is characterized in that: may further comprise the steps successively:
(1) defatted rice bran or the corn dregs of rice are adjusted pH value to 3 with 6% hydrochloric acid, soak and quench 6-8 hour, and filtrate adds lime slurry neutralization, regulate pH value to 6 ~ 6.5 with NaOH, filter, abandon filtrate, and filter residue is phytin sodium crude product;
(2) in the water of phytin sodium crude product adding 6-10 doubly being measured, adjust pH value to 2.5 with hydrochloric acid soln, treat to dissolve fully, add activated carbon decolorizing filtration, desugar; Filtrate adds NaOH and adjusts the pH value to 3-4.5, separates out albumen, adopts filter method to separate and separates out albumen, gets filtrate;
(3) gained filtrate is advanced the exchange of weakly-basic anion exchange column, washing; Then use 4-8% alkali lye wash-out; Elutriant is adjusted the pH value to 12-14 with 4-8% NaOH or KOH solution, and sediment separate out contains iron ion in the throw out;
(4) liquid after the separation is crossed the cationic exchange coloum exchange, and effluent liquid advances macroporous anion exchange resin chromatography column chromatography, and it is concentrated that chromatographic solution advances upgrading tower, is concentrated to phytic acid content 50-70%, and concentrated solution adds activated carbon decolorizing, filters, and gets filtrate;
(5) liquid end product phytic acid: liquid phytic acid is concentrated into proportion 1.390, and adjusting pH value is 2, then puts into crystallizer and clarifies;
(6) overcritical stable: it is stable that liquid phytic acid is placed in the crystallizer clarification;
(7) alcohol wash-out: put into the alcohol washing in the liquid phytic acid, destroy the heteropolar bond of phytic acid and water, under the whipped state, decrease temperature crystalline leaches crystal, and is repeated multiple times, obtains the crystallization phytic acid.
2. a kind of high-purity solid phytic acid production technique according to claim 1, it is characterized in that: described alkali lye refers to NaOH or KOH solution.
3. a kind of high-purity solid phytic acid production technique according to claim 1, it is characterized in that: described gac dosage is 3 ~ 5%.
CN2012104934533A 2012-11-28 2012-11-28 Production process of high-purity solid phytic acid Pending CN102964381A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104193780A (en) * 2014-08-01 2014-12-10 刘秀丽 Extraction method of solid phytic acid
CN107298693A (en) * 2017-07-21 2017-10-27 安康世茂生物科技有限公司 A kind of preparation method of High-purity Phytic Acid calcium and magnesium
CN110372127A (en) * 2019-07-31 2019-10-25 赛普特环保技术(厦门)有限公司 The extraction element and technique of a kind of complete-dihydrogen orthophosphate of inositol six
CN113307825A (en) * 2021-05-24 2021-08-27 浙江工业大学 Method for extracting calcium phytate from rice bran waste residues
EP4015494A1 (en) 2020-12-15 2022-06-22 Sanifit Therapeutics S.A. Processes for the preparation of soluble salts of inositol phosphates

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1563019A (en) * 2004-04-09 2005-01-12 夏红 Method of technique of ion exchange for extracting phytic acid
CN101602776A (en) * 2009-02-23 2009-12-16 杜江 The production method of high-purity solid phytic acid

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1563019A (en) * 2004-04-09 2005-01-12 夏红 Method of technique of ion exchange for extracting phytic acid
CN101602776A (en) * 2009-02-23 2009-12-16 杜江 The production method of high-purity solid phytic acid

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
杨文玉: "植酸制取工艺研究现状与展望", 《中国油脂》, vol. 28, no. 4, 20 April 2003 (2003-04-20), pages 46 - 48 *
肖传豪 等: "米糠制植酸的工艺研究和进展", 《化工时刊》, vol. 23, no. 8, 25 August 2009 (2009-08-25), pages 57 - 59 *
胡乔生 等: "用离子交换法从米糠中提取植酸的研究", 《赣南师范学院学报》, no. 3, 30 June 2001 (2001-06-30), pages 52 - 55 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104193780A (en) * 2014-08-01 2014-12-10 刘秀丽 Extraction method of solid phytic acid
CN107298693A (en) * 2017-07-21 2017-10-27 安康世茂生物科技有限公司 A kind of preparation method of High-purity Phytic Acid calcium and magnesium
CN110372127A (en) * 2019-07-31 2019-10-25 赛普特环保技术(厦门)有限公司 The extraction element and technique of a kind of complete-dihydrogen orthophosphate of inositol six
EP4015494A1 (en) 2020-12-15 2022-06-22 Sanifit Therapeutics S.A. Processes for the preparation of soluble salts of inositol phosphates
WO2022129148A1 (en) 2020-12-15 2022-06-23 Sanifit Therapeutics, S.A. Processes for the preparation of soluble salts of inositol phosphates
CN113307825A (en) * 2021-05-24 2021-08-27 浙江工业大学 Method for extracting calcium phytate from rice bran waste residues

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Application publication date: 20130313