CN101239897A - Method for producing diformate of monovalence cation used for feedstuff - Google Patents
Method for producing diformate of monovalence cation used for feedstuff Download PDFInfo
- Publication number
- CN101239897A CN101239897A CNA2007100085936A CN200710008593A CN101239897A CN 101239897 A CN101239897 A CN 101239897A CN A2007100085936 A CNA2007100085936 A CN A2007100085936A CN 200710008593 A CN200710008593 A CN 200710008593A CN 101239897 A CN101239897 A CN 101239897A
- Authority
- CN
- China
- Prior art keywords
- diformate
- feedstuff
- formate
- production method
- mother liquor
- 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
Links
Landscapes
- Fodder In General (AREA)
Abstract
Disclosed is a production method of feedstuff enebenzobisoxazole with monovalent cation, which comprises: preparing saturated aqueous solution by adding water to industrial formate, adding aulfuration natrium, mixing and heating to 60-100 DEG C, agitating equably, depositing heavy metal ions in the sollution, filtering the clean liquid, cooling to the room temperature, adding formic acid with the same amount of the formate, agitating equably, centrifugal separating to obtain enebenzobisoxazole crystal, vacuum-drying at 50-70 DEG C to obtain enebenzobisoxazole products. Compared with the prior art, the invention has the advantages that, the enebenzobisoxazole prepared in the invention removes the heavy metal in the material, accords with the feedstuff enebenzobisoxazole specification, is useful as feedstuff additives and other industrial/agricultural production materials; the total yield of the invention can reach 95-98% of the idea value, the material utilization rate is high, the product quality is improved, and production cost is reduced.
Description
Technical field
The present invention relates to the production method of diformate of monovalence cation used for feedstuff.
Background technology
In recent years, diformate is widely used as fodder additives, and intestinal bacteria, Salmonellas etc. are had effect preferably.
The technology of producing diformate at present both at home and abroad is generally " neutralisation ", promptly adds in carbonate or the highly basic and manufacturing with formic acid, and there are shortcomings such as raw material availability is low, the production cycle is long, energy consumption is high, production cost height in this technology.
Also have by formate directly is dissolved in the report that formic acid prepares diformate, obtain the crystallization diformate by reducing temperature or evaporating excessive formic acid.The diformate non-technical diformate that this method adopts, cost is too high, is unsuitable for industrial production.And contain heavy metal in the industrial formate usually, if this method adopts industrial diformate as raw material, then make product use and have certain risk as fodder additives because can't remove heavy metal.
Summary of the invention
Main purpose of the present invention is to overcome the shortcoming of prior art, and the production method of a kind of high yield, oligosaprobic diformate of monovalence cation used for feedstuff is provided.
The present invention adopts following technical scheme: the production method of diformate of monovalence cation used for feedstuff: industrial formate is added water be mixed with saturated aqueous solution, add sodium sulphite, be mixed and heated to 60-100 ℃, stir, make the heavy metal ion precipitation in the solution, filtered while hot goes out clear liquid, be cooled to room temperature, add the formic acid that is complementary with the formate consumption, stir, centrifugation obtains the diformate crystal, and 50-70 ℃ of vacuum-drying obtains the diformate finished product.
Aforementioned formate is a kind of in sodium formiate, potassium formiate, the ammonium formiate, or its combination.
Aforementioned centrifugation obtains diformate crystalline method, at first will add the clear liquid that leaches after the sodium sulphite reaction and be cooled to room temperature, add the formic acid that is complementary with the formate consumption, stir, centrifugation obtains xln diformate and primary crystallization mother liquor, primary crystallization mother liquor vacuum concentration is extremely saturated, put into the crystallizer stirring and be cooled to room temperature, centrifugation obtains xln diformate and secondary crystal mother liquor, with all xln diformate vacuum-drying, obtain the diformate finished product; The secondary crystal mother liquor is sneaked into the primary crystallization mother liquor vacuum concentration of next time producing.
The production method of aforementioned diformate of monovalence cation used for feedstuff, the heavy metal content of industrial formate detects in elder generation before producing, the theoretical value of the sodium sulphite that calculating adds according to detected result, the amount of the sodium sulphite of described adding is the 110-130% of its theoretical value.
The mol ratio of aforementioned formate and formic acid is 1: 0.5-1.5.
By the above-mentioned description of this invention as can be known, compared with prior art, the present invention has following advantage: the diformate that the present invention makes has been removed the heavy metal in the raw material, meets feed diformate specification, can be used as fodder additives, also can be used as the raw material of other industrial and agricultural production; Total recovery of the present invention can reach the 95-98% of theoretical value, and the raw material availability height has improved quality product simultaneously, has reduced production cost.
Embodiment
The specific embodiment of the present invention, the feed production method of the Potassium hydrogen diformate of monovalent cation:
Extract the heavy metal content that detects industrial potassium formiate before producing earlier, calculate the amount of the sodium sulphite that adds according to detected result; Take by weighing industrial potassium formiate 100kg, add water 50kg, processing industry is with sodium sulphite 0.01-0.1kg (occurrence is the 110-130% with the amount of detected heavy metal complete reaction), thorough mixing, be heated to 80-90 ℃, stir, the filtered while hot waste is got clear liquor and is cooled to room temperature, adds 60 kilograms in formic acid, stir, centrifugation obtains xln diformate and primary crystallization mother liquor, and primary crystallization mother liquor vacuum concentration is put into the crystallizer stirring and is cooled to room temperature to saturated, centrifugation obtains xln Potassium hydrogen diformate and secondary crystal mother liquor, and the secondary crystal mother liquor is sneaked into the primary crystallization mother liquor vacuum concentration of next time producing.All xln Potassium hydrogen diformates place Vacuumdrier 50-70 ℃ of vacuum-drying to water content less than 1%, cooling back is taken out packing and is the finished product Potassium hydrogen diformate.The total recovery of present method can reach the 95-98% of theoretical value, the Potassium hydrogen diformate place to go that present method makes the heavy metal in the raw material, meet the Potassium hydrogen diformate specification that feed is used, can be used as fodder additives, also can be used as the raw material of other industrial and agricultural production.
Certainly, present embodiment has only been introduced the production method of Potassium hydrogen diformate, and the production method and the present embodiment of sodium diformate, dioctyl phthalate ammonium and three's combination are similar.
Above-mentioned only is a specific embodiment of the present invention, but design concept of the present invention is not limited thereto, and allly utilizes this design that the present invention is carried out the change of unsubstantiality, all should belong to the behavior of invading protection domain of the present invention.
Claims (5)
1. the production method of diformate of monovalence cation used for feedstuff, it is characterized in that: industrial formate is added water be mixed with saturated aqueous solution, add sodium sulphite, be mixed and heated to 60-100 ℃, stir, make the heavy metal ion precipitation in the solution, filtered while hot goes out clear liquid, is cooled to room temperature, add the formic acid that is complementary with the formate consumption, stir, centrifugation obtains the diformate crystal, and 50-70 ℃ of vacuum-drying obtains the diformate finished product.
2. the production method of diformate of monovalence cation used for feedstuff as claimed in claim 1 is characterized in that: described formate is a kind of in sodium formiate, potassium formiate, the ammonium formiate, or its combination.
3. the production method of diformate of monovalence cation used for feedstuff as claimed in claim 1, it is characterized in that: described centrifugation obtains diformate crystalline method and is, at first will add the clear liquid that leaches after the sodium sulphite reaction and be cooled to room temperature, add the formic acid that is complementary with the formate consumption, stir, centrifugation obtains xln diformate and primary crystallization mother liquor, primary crystallization mother liquor vacuum concentration is extremely saturated, put into the crystallizer stirring and be cooled to room temperature, centrifugation obtains xln diformate and secondary crystal mother liquor, with all xln diformate vacuum-drying, obtain the diformate finished product; The secondary crystal mother liquor is sneaked into the primary crystallization mother liquor vacuum concentration of next time producing.
4. the production method of diformate of monovalence cation used for feedstuff as claimed in claim 1, it is characterized in that: the heavy metal content that detects industrial formate before producing earlier, the theoretical value of the sodium sulphite that calculating adds according to detected result, the amount of described adding sodium sulphite is the 110-130% of its theoretical value.
5. the production method of diformate of monovalence cation used for feedstuff as claimed in claim 1, it is characterized in that: the mol ratio of described formate and formic acid is 1: 0.5-1.5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100085936A CN101239897A (en) | 2007-02-09 | 2007-02-09 | Method for producing diformate of monovalence cation used for feedstuff |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007100085936A CN101239897A (en) | 2007-02-09 | 2007-02-09 | Method for producing diformate of monovalence cation used for feedstuff |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101239897A true CN101239897A (en) | 2008-08-13 |
Family
ID=39931783
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2007100085936A Pending CN101239897A (en) | 2007-02-09 | 2007-02-09 | Method for producing diformate of monovalence cation used for feedstuff |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101239897A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111574358A (en) * | 2020-06-16 | 2020-08-25 | 重庆万盛川东化工有限公司 | Preparation process of potassium diformate |
| CN113754529A (en) * | 2021-08-31 | 2021-12-07 | 潍坊加易加生物科技有限公司 | Method for preparing potassium diformate and sodium diformate by using organic potassium carboxylate |
-
2007
- 2007-02-09 CN CNA2007100085936A patent/CN101239897A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111574358A (en) * | 2020-06-16 | 2020-08-25 | 重庆万盛川东化工有限公司 | Preparation process of potassium diformate |
| CN113754529A (en) * | 2021-08-31 | 2021-12-07 | 潍坊加易加生物科技有限公司 | Method for preparing potassium diformate and sodium diformate by using organic potassium carboxylate |
| CN113754529B (en) * | 2021-08-31 | 2024-05-10 | 潍坊加易加生物科技有限公司 | Method for preparing potassium diformate and sodium diformate by using organic carboxylic acid potassium |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104445276B (en) | A kind of efficient method preparing cyanamide solution | |
| CN103787293A (en) | Method for preparing sodium dihydrogen phosphate by utilizing phosphoric acid by wet process | |
| CN101857210B (en) | Method for producing industrial grade diammonium phosphate from wet-process phosphoric acid | |
| CN103879980B (en) | The method of potassium primary phosphate is produced with calcium hydrophosphate fodder | |
| CN101857213A (en) | Method for preparing food-grade diammonium phosphate from wet-process phosphoric acid | |
| CN101973995A (en) | Method for recycling waste water in production of folic acid | |
| CN102502721A (en) | Method for preparing lithium carbonate through extracting lithium from lithium ore | |
| CN101781264B (en) | Production method of 1-methyl-5-mercapto-1,2,3,4-tetrazole | |
| CN101857212B (en) | Method for preparing food-grade monoammonium phosphate from wet-process phosphoric acid | |
| CN101239897A (en) | Method for producing diformate of monovalence cation used for feedstuff | |
| CN109437980B (en) | Method for producing acid potassium dihydrogen phosphate | |
| CN104445281A (en) | Waste residue comprehensive utilization method for trichlorosilane leaching system | |
| CN104230800A (en) | Preparation method of copper 8-hydroxyquinoline | |
| CN103879981B (en) | A kind of method utilizing phosphoric acid raffinate to prepare potassium primary phosphate | |
| CN107459447A (en) | A kind of processing method of sodium gluconate waste liquor | |
| CN104341001A (en) | Method for producing food-grade zinc sulfate with industrial-grade zinc sulfate as raw material | |
| CN111620353A (en) | Method for extracting potassium salt from potassium feldspar | |
| CN103360235A (en) | Preparation method of barium acetate | |
| CN102417192B (en) | Process for processing potassium chloride raw material for making ion membrane potassium hydroxide | |
| CN106554267A (en) | The method for improving gallic acid extraction ratio | |
| CN107285993A (en) | A kind of ketoside solid waste resource recovery processing method | |
| CN115490541B (en) | Method for continuously producing ammonium potassium phosphate | |
| CN114605700B (en) | Method for preparing aluminum hydroxide and magnesium hydroxide composite flame retardant and combining ammonium chloride | |
| CN104447290A (en) | Method for preparing 2,4-dichlorophenoxyacetic acid | |
| CN101016239A (en) | Method of extracting calcium gluconate from mother liquid after calcium gluconate crystallization |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20080813 |