CN1138579A - Method for prepn. of oxidation preventive isoascorbic acid - Google Patents
Method for prepn. of oxidation preventive isoascorbic acid Download PDFInfo
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- CN1138579A CN1138579A CN 96100812 CN96100812A CN1138579A CN 1138579 A CN1138579 A CN 1138579A CN 96100812 CN96100812 CN 96100812 CN 96100812 A CN96100812 A CN 96100812A CN 1138579 A CN1138579 A CN 1138579A
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- acid
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- prepn
- acidifying
- sodium isovitamin
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Abstract
A process for preparing araboascorbic acid comprises acidifying sodium araboascorbate in water with acid. Its advantages is simple technology, short productive period and high purity of product.
Description
The present invention relates to the method for oxidation preventive isoascorbic acid, particularly is the method for feedstock production saccharosonic acid with the saccharosonic acid.
Saccharosonic acid owing to its low production cost, is widely used in fields such as food, medical science as antioxidant.In the prior art, the report (CN1098412A) for preparing through ion exchange resin is arranged, but the spent ion exchange resin preparation, complex process because SODIUM ISOVITAMIN C solubleness in water is very little, thereby must be used big water gaging.Just can produce product through evaporation concentration for a long time, energy consumption is bigger, and production cost also improves thus.Being disclosed in the preparation method of the saccharosonic acid among the CN1106808A, is to be solvent with the lower alcohol, and SODIUM ISOVITAMIN C is dissolved in the alcohol, then with the mineral acid acidifying, according to the little characteristics of inorganic sodium solubleness in lower alcohol, leaches inorganic salt.And then subzero treatment gets product.But this method is defectiveness also, owing to carry out in alcoholic solution, therefore, acidification reaction is affected, and the reaction times is longer, and as not only poisonous with the methyl alcohol equal solvent, cost is also more expensive.
The present invention has overcome the shortcoming that exists in the prior art, is solvent with water, and the acidifying of SODIUM ISOVITAMIN C raw material is obtained saccharosonic acid.
Particularly, method of the present invention comprises mixes saccharosonic acid sodium raw materials and water, adds acidifying, and postcooling is finished in acidifying, separates out different anti-hematic acid crystallization from the aqueous solution.
In the described method, the ratio of saccharosonic acid sodium raw materials and water is generally 1～3: 1, according to the particular case variation of operation, decide according to the situation of using acid simultaneously, and for example, use hydrochloric acid, then can use more a spot of water.
Used acid can be the mineral acid example hydrochloric acid, sulfuric acid and nitric acid, and organic acid such as sulfonic acid, trifluoroacetic acids etc. preferably use mineral acid, wherein use hydrochloric acid better.
The amount of used acid is usually slightly larger than the SODIUM ISOVITAMIN C equivalent.
The acidification reaction temperature can be at 30 °-100 ℃, and preferably at 40 °-80 ℃, common about 1 hour of reaction times can finish, preferably at 20-40 minute.
After acidification reaction is finished, be cooled to 0-10 ℃, a large amount of white crystals saccharosonic acids can be separated out from solution, filtration washing (ice ethanol/water=2-6: 1), promptly before obtain meeting the pure product saccharosonic acid of F.C.C standard.
The inventive method can use the SODIUM ISOVITAMIN C crude product as raw material, adds proper amount of active carbon when acidifying, stir during acidifying, and after acidification reaction is finished, elimination gac, decrease temperature crystalline then while hot.
Mother liquor in the inventive method and washing lotion with in the alkali and after, cooling can be separated out SODIUM ISOVITAMIN C, recycling use.
Below specify the present invention with embodiment.
Embodiment 1:
With 550kg water, the pure product of 1500kg SODIUM ISOVITAMIN C add in the 3000L souring tank, start stirring, from test tank, add 600L hydrochloric acid during with 50 ℃ of steam heating, be incubated steam off after 30 minutes, temperature is 5 ℃ in being cooled to icy salt solution, is incubated 1.5 hours, there is the large-tonnage product crystallization to separate out, drive whizzer and get rid of filter, and ice ethanol/water (4: 1) washing, dry different anti-hematic acid 1000kg with 20L, content 99.89%, [α]
D 25=-17.56 °, other index meets the F.C.C standard.With mother liquor, washings is squeezed in the 2000L crystallizer, transfers it to pH6 with 40% sodium hydroxide solution, is cooled to 5 ℃ with icy salt solution, have mass crystallization to separate out, whizzer gets rid of filter, and is dry with 20L ethanol/water (volume ratio 3: 1) washing, get 228kg SODIUM ISOVITAMIN C finished product, content 99.12%, [α]
D 25=+95.92 °.Other index meets the F.C.C standard.
Embodiment 2
With 1500kg saccharosonic acid crude product (content 94.29%), 450kg water, 500L hydrochloric acid and 5g pharmaceutical grade are applied flexibly charcoal and are added successively in the 3000L acidifying bleacher, open stirring, are steam heated to 75 ℃, are incubated 30 minutes, transfer pH1.5-2.1.Filtered while hot, filtrate are squeezed in the 3000L crystallizer, and cryosel is cooled to 5 ℃ of insulations 1.5 hours, and mass crystallization is separated out, and whizzer gets rid of filter, with the washing of 20L ice ethanol/water, dry 800kg saccharosonic acid finished product, content 99.28%, [α] of getting
D 25=-17.38 °, other index meets the F.C.C standard.Mother liquor and washing lotion get 210kg SODIUM ISOVITAMIN C finished product, content 98.94%, [α] with embodiment 1 same method
D 25=+96.23 °.
Claims (5)
1. one kind prepares the method for different anti-hematic acid by SODIUM ISOVITAMIN C, it is characterized in that raw material SODIUM ISOVITAMIN C and water are mixed, and uses directly acidifying of acid then.
2. according to the method for claim 1, it is characterized in that wherein said raw material SODIUM ISOVITAMIN C is its pure product.
3. according to the method for claim 1, it is characterized in that wherein said acid is hydrochloric acid.
4. according to the method for claim 1, the ratio that it is characterized in that wherein said water and raw material SODIUM ISOVITAMIN C is 1: 1～3.
5. according to the method for claim 1, its acidifying is carried out under 40-80 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100812A CN1053901C (en) | 1996-01-23 | 1996-01-23 | Method for prepn. of oxidation preventive isoascorbic acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96100812A CN1053901C (en) | 1996-01-23 | 1996-01-23 | Method for prepn. of oxidation preventive isoascorbic acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1138579A true CN1138579A (en) | 1996-12-25 |
| CN1053901C CN1053901C (en) | 2000-06-28 |
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ID=5116761
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96100812A Expired - Fee Related CN1053901C (en) | 1996-01-23 | 1996-01-23 | Method for prepn. of oxidation preventive isoascorbic acid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1053901C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103087018A (en) * | 2012-11-14 | 2013-05-08 | 江苏江山制药有限公司 | Preparation method of erythorbic acid |
| CN111374821A (en) * | 2014-06-19 | 2020-07-07 | 加州理工学院 | Small molecule transport device for delivering drugs or removing waste |
| CN115583926A (en) * | 2022-11-04 | 2023-01-10 | 新拓洋生物工程有限公司 | Method for recovering D-sodium erythorbate and D-erythorbic acid by mother liquor centrifugation |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1045292C (en) * | 1994-07-22 | 1999-09-29 | 郑州市生物化工厂 | Method for preparing isoascorbic acid |
-
1996
- 1996-01-23 CN CN96100812A patent/CN1053901C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103087018A (en) * | 2012-11-14 | 2013-05-08 | 江苏江山制药有限公司 | Preparation method of erythorbic acid |
| CN111374821A (en) * | 2014-06-19 | 2020-07-07 | 加州理工学院 | Small molecule transport device for delivering drugs or removing waste |
| CN111374821B (en) * | 2014-06-19 | 2022-05-03 | 加州理工学院 | Small molecule transport device for delivering drugs or removing waste |
| CN115583926A (en) * | 2022-11-04 | 2023-01-10 | 新拓洋生物工程有限公司 | Method for recovering D-sodium erythorbate and D-erythorbic acid by mother liquor centrifugation |
| CN115583926B (en) * | 2022-11-04 | 2024-03-19 | 新拓洋生物工程有限公司 | Method for centrifugally recovering D-sodium erythorbate and D-erythorbic acid by using mother solution |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1053901C (en) | 2000-06-28 |
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