CN1107071C - Process for preparing phytic acid - Google Patents
Process for preparing phytic acid Download PDFInfo
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- CN1107071C CN1107071C CN00123173A CN00123173A CN1107071C CN 1107071 C CN1107071 C CN 1107071C CN 00123173 A CN00123173 A CN 00123173A CN 00123173 A CN00123173 A CN 00123173A CN 1107071 C CN1107071 C CN 1107071C
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- phytic acid
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- rice bran
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Abstract
The present invention relates to a process method for producing phytic acid. In the process of production, a bran cake is ground and sieved by 40 meshes, and rice bran is prepared; ionized water of 60DEG C.is slowly added to hydrochloric acid, pH value is regulated to 2.0, the prepared rice bran and water are added, and the weight ratio of the rice bran to the water is 1:8. The rice bran is soaked for 4 to 6 hours and is stirred once every 30 minutes. After solution is stood for two hours, supernatant liquid is extracted; according to a proportion of 1:4, water is added to deposits for the second soak, the pH value is regulated to 2.0, the deposits are soaked for two hours, solution is stood for one hour, and supernatant liquid is extracted. The two extracted supernatant liquids are merged and filtered, and mother solution is obtained; a finished product of high-quality phytic acid is prepared by washing, acidifying, exchanging and concentrating the mother solution.
Description
The present invention relates to a kind of production method of phytic acid.
Phytic acid is a myo-Inositol hexaphosphate, extensively is present in the oil grain, particularly presses oily grouts, more as content in rice bran cake, soya-bean cake, rapeseed cake, linseed meal, cotton seed cake, wheat bran, wheat bran, the maize germ.The phytic acid of occurring in nature does not exist with free form, but exists with the form of phytic acid ca (Fei Ting).Phytic acid is faint yellow or isabelline thickness body, is strongly-acid, and is soluble in water.The feature of phytic acid is with metal ion extremely strong complex ability and oxidation-resistance to be arranged; complexing power is similar to EDTA; and belong to the safety non-toxic natural nutriment; in developed country; phytic acid has been widely used in industries such as food, medicine, chemical industry; in wine manufacturing industry, the adding phytic acid can be removed Ca, Fe, Cu and other metallic element in the wine, and the protection HUMAN HEALTH is had good action.Phytic acid also can be used as the preservation agent of fishery products, fruit and vegetable, flowers, the tinned pre-colour-protecting stabilizing agent, and fatty foods, meat, cake, the anticorrosion preservatives of salad, beverage remove metal agent.In fermentative Production lactic acid, riboflavin, gentamicin, the antibiotic process of amino glycoside, add phytic acid and can improve output.Pharmaceutically, can make oxidation inhibitor, also can be used as the therapeutical agent of scanning imagery agent, gastritis and enteritis, black xanthodont special efficacy clean-out system.The production method of phytic acid is a lot of at present, as calcium Fei Tingfa, ammonia Fei Tingfa, Na Feitingfa etc.Wherein, Na Feitingfa produces the comparatively reliable and advanced method of phytic acid.But also have weak point, its main drawback has:
1, to adopt tap water to soak, contain the extraction yield of metal ion, phytic acid low for this kind method, has only 7---and 10%.
2, there is not anion column: sulfate radical, the residues of chloride amount is big, reaches 3---and 5%, influence quality.
Purpose of the present invention provides the phytic acid production technique that a kind of phytic acid content height, inorganic phosphorus do not exceed standard.
The producing and manufacturing technique of phytic acid of the present invention is:
1, acidleach
The chaff cake was pulverized 40 mesh sieves, and it is standby to make rice bran.60 ℃ ionized waters are slowly added hydrochloric acid, pH value is transferred to 2.0, add the rice bran of preparation then, the weight ratio of rice bran and water is 1: 8.Rice bran soaks 4---and 6 hours, stirred once in per 30 minutes, after stirring, also to survey pH value, remaining on pH value is 2.0, inaccessiblely will add hydrochloric acid.After leaving standstill two hours like this, extract supernatant liquid.
Secondary soaks, and adds water by 1: 4 in sediment, water temperature 60 degree, pH value is transferred to 2.0, stirs once every 30 minutes, soaks two hours, leave standstill one hour after, the extraction supernatant liquid.
2, merge
The secondary supernatant liquor merges, and it should be as clear as crystal filtering the mother liquor that flows out.Mother liquor is opaque, filters again, till as clear as crystal.
3, neutralization
Transparent mother liquor neutralizes with alkali.With solid sodium hydroxide, use a spot of water dissolution, Yi Bian slowly add in the mother liquor, stir on one side, approximately the 100kg mother liquor is with 200---and 250 gram sodium hydroxide add after the alkali, transparent mother liquor has become oyster white, and surveying pH value with test paper is 8, just stops to add sodium hydroxide.Fei Ting just precipitates after adding alkali reaction.If it is too much that sodium hydroxide adds, luxuriant and rich with fragrance spit of fland is fully precipitated, but color burn causes the washing difficulty; If the sodium hydroxide dosage is not enough, can not fully react, the precipitation capacity of phytic acid composition is just few.In and the time add how much sodium hydroxide, specifically be to decide with pH value.After the neutralization reaction, staticly settled two hours, then yellow waste water is taken out, extract the luxuriant and rich with fragrance spit of fland of lower sediment thing.
4, washing
The luxuriant and rich with fragrance spit of fland of precipitation is placed in the Da Chi, and pH value is transferred to 8.Fei Ting wants complete dissolved particles just can touch water, just can reach the purpose of washing, dissolves later Fei Ting and is placed on centrifuge dehydration on the whizzer, repetitive scrubbing three times.
5, wash with pure water
After repeatedly sodium hydroxide washs, wash with pure water again.Luxuriant and rich with fragrance spit of fland stirring and dissolving (water no longer adds any medicine) in water is washed neutrality to luxuriant and rich with fragrance spit of fland to be as the criterion.During the pure water washing, at first measure the pure water pH value,, just wash 6.5 if the pure water pH value is 6.5; The pH value of water is 7.0 just to wash 7.0.After the pure water washing, centrifuge dehydration.
6, acidifying
732 types handled well sun resin, washing pH value with pure water is 3.5---4, behind the filter solid carbon dioxide,, put resin earlier into by the i.e. two parts of luxuriant and rich with fragrance spits of fland of resins portion of 2: 1 ratios, after put Fei Ting.Fei Ting runs into resin and becomes liquid with regard to dissolving, and should be 1.5 with precision test paper test PH this moment, is the best pH-value of acidifying.If basicity is higher, increase resin, basicity is on the low side, adds luxuriant and rich with fragrance spit of fland.Dissolve in basin and left standstill two hours, with cloth bag resin filter is separated then, filtrate also is acidizing fluid.
7, exchange
Positive resin after the manipulation of regeneration installs to exchange king-post the inside together with the salt sour water.6 centimeters of king-post internal diameters, long 1.2 meters, 3 is positive post, same two is cloudy post.Use the resin drip washing in the pure water coupled columns then, the water that flows out, pH value reaches 3.5---and 4, stop drip washing, after doing, the current for the treatment of bottom in the post just can feed acidizing fluid, and the control flow velocity is at per minute 50---and 60 milliliters.The exchange that enters two cloudy king-posts again after the exchange of three posts is intact just draws purer thin planting acid like this.
8, concentrate
Dilute phytic acid solution is poured in the evaporation tank, and concentrated degree Beaume is 12 when spending, and carries out the decolouring first time, under temperature at that time, add 1% activated carbon, after stirring, use the middling speed filter paper filtering, the black active carbon filtration is come out, the phytic acid that leaches carries out concentrating the second time, temperature is controlled at below 60 ℃, when degree Beaume reaches 41---in the time of 43, carry out the decolouring second time, add activated carbon 1% equally, use the middling speed filter paper filtering equally, effusive should be clear, colorless or weak yellow liquid, and this liquid is the phytic acid finished product.
The present invention has been owing to adopted the novel process of acidleach, thereby improved the content and the extraction yield of phytic acid greatly, removed metal ion simultaneously.The present invention is by making colourless or flaxen phytic acid with novel process in the alkali.Particularly adopt novel concentrating process of the present invention to pass through secondary concentration, temperature is controlled at below 60 ℃, and the colourless or flaxen phytic acid of producing has kept the pure natural true qualities, has reduced muriatic residual quantity, and the content that can make inorganic phosphorus reaches the specified standards requirement, improved the quality of phytic acid.
Embodiment
The chaff cake was pulverized 40 mesh sieves, and to make the 1kg rice bran standby.The ionized water of 60 ℃ of 8kg is slowly added hydrochloric acid, pH value is transferred to 2.0, add the 1kg rice bran of preparation then, soaked 4 hours, stirred once every 30 minutes, and inspection side pH value, PH does not reach 2.0 and adds the small amount of hydrochloric acid adjusting again, reaches till 2.0 up to pH value.Soaked 4 hours, left standstill 2 hours, extract supernatant liquid then.Secondary soaks, and adds 4kg water in sediment, and water temperature is 60 ℃, and pH value is transferred to 2.0, stirs once every 30 minutes, soaks 2 hours, leaves standstill after 1 hour and extracts supernatant liquid.The supernatant liquid of second decimation is merged, and be filled into infuse clearly transparent till.The transparent mother liquor of infusing clearly that filters out closes in carrying out with alkali, solid-state sodium hydroxide with the less water dissolving after, slowly add in the mother liquor on one side, stirring on one side, pH value is transferred at 8 o'clock, stop adding sodium hydroxide.This moment, milky luxuriant and rich with fragrance spit of fland was fully precipitated.Leave standstill after two hours yellow waste water is taken out, the luxuriant and rich with fragrance spit of fland of the lower sediment thing that extracts is placed on and uses pure cerium hydroxide sodium repetitive scrubbing three times in the Da Chi, and use centrifuge dewatering, wash with pure water again, neutrality is washed in luxuriant and rich with fragrance spit of fland to be as the criterion, centrifuge dehydration is put into the 732 types sun resin of handling well and is carried out acidifying, and the luxuriant and rich with fragrance spit of fland that will become liquid is fully stirred and made pH value reach 1.5.Leave standstill after two hours and with cloth bag resin filter is separated, filtrate is that acidizing fluid is stand-by.Positive resin after handling and salt sour water are installed to exchange king-post the inside together.With pure water the resin in the king-post is carried out drip washing then, the pH value of the water that flows out reaches at 3.5 o'clock and stops drip washing, just can feed after the current for the treatment of bottom in the post are done and refilter transparent back acidizing fluid.Through entering two positive king-post exchanges after three positive post exchanges again, just can obtain purer thin planting acid.Dilute phytic acid solution poured in the evaporation tank concentrate, when concentrating degree Beaume 12 and spending, carry out decolouring first time, add 1% activated carbon, stir, use the middling speed filter paper filtering, the black active carbon filtration is come out, and the phytic acid that leaches carries out concentrating the second time, and temperature is controlled at below 60 ℃.When degree Beaume reaches 41---in the time of 43, carry out the decolouring second time, add activated carbon 1% equally, filter with the middling speed filter paper at last and just make the phytic acid finished product.
Claims (1)
1, a kind of producing and manufacturing technique of phytic acid is characterized in that:
A, the chaff cake was pulverized 40 mesh sieves, and to make rice bran standby, and 60 ℃ ionized waters are slowly added hydrochloric acid, and pH value is transferred to 2.0, add the rice bran of preparation then, the weight ratio of rice bran and water is 1: 8, soaks 4-6 hour, stirred once every 30 minutes, leave standstill after two hours and extract supernatant liquid;
B, secondary soak, and in sediment, add water by 1: 4, and water temperature is 60 ℃, and pH value is transferred to 2.0, stir once every 30 minutes, soak two hours, leave standstill one hour after, the extraction supernatant liquid; The supernatant liquid of second decimation is merged, through filtering, obtains transparent mother liquor again:
C, transparent mother liquor neutralize with alkali.The a spot of water dissolution of pure cerium hydroxide sodium slowly adds in the mother liquor, and pH value is transferred at 8 o'clock, stops hydro-oxidation sodium, after the neutralization reaction, staticly settles two hours, extracts the luxuriant and rich with fragrance spit of fland of lower sediment thing;
D, first with washing with pure water again after the soda ash washing, then with centrifuge dehydration sedimentary luxuriant and rich with fragrance spit of fland;
Acidifying is carried out with the 732 types sun resin of handling well in luxuriant and rich with fragrance spit of fland after E, the washing, it is 3.5 that 732 types sun resin washes pH value with water---4, after the filter solid carbon dioxide divides, mix with luxuriant and rich with fragrance spit of fland in 2: 1 ratios, best pH value after the acidifying is 1.5, with cloth bag resin and acidizing fluid are separated then, refiltered transparent back acidizing fluid after the exchange column exchange, obtain thin planting acid;
F, rare value acid solution is poured in the evaporation tank, when concentrated degree Beaume is 12 ℃, carried out the decolouring first time, add 1% activated carbon, after stirring, use the middling speed filter paper filtering, the black active carbon filtration is come out, filtrate carries out concentrating the second time, and temperature is controlled at below 60 ℃, when degree Beaume reaches 41---and in the time of 43, carry out the decolouring second time, and add 1% activated carbon equally, and use the middling speed filter paper filtering again, just can be made into the phytic acid finished product.
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CN00123173A CN1107071C (en) | 2000-10-30 | 2000-10-30 | Process for preparing phytic acid |
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CN00123173A CN1107071C (en) | 2000-10-30 | 2000-10-30 | Process for preparing phytic acid |
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CN1294128A CN1294128A (en) | 2001-05-09 |
CN1107071C true CN1107071C (en) | 2003-04-30 |
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Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101624399B (en) * | 2009-08-11 | 2012-02-22 | 贵州大学 | Method for extracting phytic acid from jatropha curcas seed cake or jatropha curcas seeds |
CN102030773B (en) * | 2010-10-27 | 2013-04-24 | 江南大学 | Technique for coproducing phytic acid and oligopeptide from defatted rice bran |
CN102106500B (en) * | 2011-01-25 | 2012-10-03 | 郭玉军 | Dandelion low-sugar beverage and preparation method thereof |
CN103626799B (en) * | 2013-12-03 | 2016-02-24 | 广西新方向化学工业有限公司 | A kind of preparation of composite phytic acid sugar alcohol sugar alcohol ester sequestrant |
CN114369116A (en) * | 2021-12-22 | 2022-04-19 | 厦门世达膜科技有限公司 | Method for extracting high-purity phytic acid |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1037515A (en) * | 1988-05-14 | 1989-11-29 | 周定华 | The production technique of myo-Inositol hexaphosphate |
CN1026693C (en) * | 1986-03-01 | 1994-11-23 | 敷岛淀粉株式会社 | Process for preparing inositol |
JPH09278782A (en) * | 1996-04-08 | 1997-10-28 | Fuji Oil Co Ltd | Production of phytic acid |
CN1167768A (en) * | 1997-04-12 | 1997-12-17 | 包昌年 | Method for extracting phytin from rice bran |
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2000
- 2000-10-30 CN CN00123173A patent/CN1107071C/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1026693C (en) * | 1986-03-01 | 1994-11-23 | 敷岛淀粉株式会社 | Process for preparing inositol |
CN1037515A (en) * | 1988-05-14 | 1989-11-29 | 周定华 | The production technique of myo-Inositol hexaphosphate |
JPH09278782A (en) * | 1996-04-08 | 1997-10-28 | Fuji Oil Co Ltd | Production of phytic acid |
CN1167768A (en) * | 1997-04-12 | 1997-12-17 | 包昌年 | Method for extracting phytin from rice bran |
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