CN104150456A - Method for producing calcium phosphate salt and sodium phosphate salt by using sodium sulfate wastewater - Google Patents
Method for producing calcium phosphate salt and sodium phosphate salt by using sodium sulfate wastewater Download PDFInfo
- Publication number
- CN104150456A CN104150456A CN201410396598.0A CN201410396598A CN104150456A CN 104150456 A CN104150456 A CN 104150456A CN 201410396598 A CN201410396598 A CN 201410396598A CN 104150456 A CN104150456 A CN 104150456A
- Authority
- CN
- China
- Prior art keywords
- phosphate salt
- sodium
- sodium sulfate
- value
- calcium phosphate
- 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.)
- Granted
Links
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
The invention relates to a method for producing calcium phosphate salt and sodium phosphate salt by using sodium sulfate wastewater. According to the method, wastewater comprising sodium sulfate is adopted as a raw material; 5-15% excessive phosphoric acid with a mass concentration of 80-90% is added to the raw material sodium sulfate wastewater, such that the solution is acidic, and sodium sulfate is completely acidified; lime cream is added into the material, and a pH value is controlled at 2.6-3.2, such that calcium sulfate precipitate is produced, and sulfate radicals in the solution are removed; filtration is carried out; lime cream is continued to be added into a filtrate, and a pH value is controlled at 6.5-7.0; when a reaction is finished, obtained solid is calcium hydrogen phosphate, and obtained liquid is mainly sodium phosphate salt. The method provided by the invention has the advantages of simple and reasonable process, high operability, and high conversion rate. With the method, wastewater is treated, resource is saved, environment is protected, and resource recycling is realized. As a result of experiments, 80-90% of sodium sulfate can be converted.
Description
Technical field
The present invention relates to a kind of method for production of phosphate salt, particularly a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater.
Background technology
Sodium sulfate, mineral compound, Disodium sulfate decahydrate has another name called saltcake, and white, odorless, the crystallization that has bitter taste or powder, have water absorbability.Profile is colourless, transparent, large crystallization or the little crystallization of graininess.Be mainly used in water glass processed, glass, enamel, paper pulp, refrigeration mixture, washing composition, siccative, dye-dilution agent, analytical chemistry reagent, pharmaceuticals etc.Sodium sulfate is extensively present in nature and chemical spent material.In silicon-dioxide production process, can produce the waste water that contains in a large number sodium sulfate, in prior art, can not utilize well this waste water, cause certain wasting of resources.
Summary of the invention
Technical problem to be solved by this invention is for the deficiencies in the prior art, and a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater is provided, and the method is reasonable in design, easy to operate, and cost is low, has effectively utilized waste resource.
Technical problem to be solved by this invention is to realize by following technical scheme.The present invention is a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, is characterized in: the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 80-90% to the mass concentration that adds excessive 5-15% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 2.6 ~ 3.2, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.5 ~ 7.0, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
The raw material of the inventive method can be the waste water that contains sodium sulfate producing in the waste water that contains sodium sulfate producing in technique, particularly silicon-dioxide production process.
In method and technology scheme of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater of the present invention, further preferred technical scheme or technical characterictic are: be excessive 8-12% to the phosphoric acid adding in raw material sulphuric acid sodium waste water, and most preferably 10%; The mass concentration of phosphoric acid is 84-86%, most preferably 85%.
In method and technology scheme of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater of the present invention, further preferred technical scheme or technical characterictic are: while adding milk of lime first, control pH value 2.8 ~ 3.0, most preferably pH value 2.9; While continuing to add milk of lime, control pH value 6.6 ~ 6.8, most preferably pH value 6.7.
Technical solution of the present invention is to adopt in metabisulfite solution, to add a kind of weak acid and milk of lime to react, and under acidic conditions, driving a reaction carries out.The present invention utilizes calcium hydroxide and phosphoric acid, displaces the sodium ion in sodium sulfate wastewater under sour environment, and produces calcium phosphate salt and sodium phosphate salt.Its reaction equation is as follows:
2?Na2SO4?+?3?Ca(OH)2?+?2H3PO4?=?2CaSO4?+?CaHPO4?+?Na2HPO4
The present invention adopts at sodium sulfate and calcium hydroxide and phosphatase reaction and makes calcium phosphate salt and sodium phosphate salt, and because sodium sulfate and calcium hydroxide are all alkaline matters, under general condition, this reaction is difficult to carry out.By add suitable phosphoric acid in solution, solution is transformed into sour environment, molecular balance is moved to left, wherein sulfate radical and calcium ion more easily generate calcium sulfate precipitation.
Compared with prior art, technique advantages of simple of the present invention, workable, transformation efficiency is high.It has been processed waste water and has saved resource, has not only protected environment also to realize the recycling of resource.Through experimental verification, the present invention can transform 80 ~ 90% sodium sulfate.
Embodiment
Below further describe concrete technical scheme of the present invention, so that those skilled in the art understands the present invention further, and do not form the restriction to its right.
Embodiment 1, a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 80% to the mass concentration that adds excessive 5% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 2.6, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.5, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
Embodiment 2, a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 90% to the mass concentration that adds excessive 15% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 3.2, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 7.0, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
Embodiment 3, a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 85% to the mass concentration that adds excessive 10% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 2.9, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.7, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.This programme can be realized the sodium sulfate that transforms 90%.
Embodiment 4, a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 84% to the mass concentration that adds excessive 8% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 2.8, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.6, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
Embodiment 5, a kind of method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 86% to the mass concentration that adds excessive 12% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 3.0, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.8, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
In method described in embodiment 1-5, raw material is the waste water that contains sodium sulfate to produce in silicon-dioxide production process.
Claims (6)
1. a method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater, is characterized in that: the method is taking the waste water that contains sodium sulfate as raw material; The phosphoric acid that is first 80-90% to the mass concentration that adds excessive 5-15% in raw material sulphuric acid sodium waste water, makes solution be acid, makes the complete acidifying of sodium sulfate; Then add wherein milk of lime, control pH value 2.6 ~ 3.2, generate calcium sulfate precipitation, and remove the sulfate radical in solution; Filter, in filtrate, continue to add milk of lime, control pH value 6.5 ~ 7.0, after reaction finishes, obtaining solid is secondary calcium phosphate, and liquid is mainly sodium phosphate salt.
2. method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater according to claim 1, is characterized in that: the method is taking the waste water that contains sodium sulfate that produces in silicon-dioxide production process as raw material.
3. method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater according to claim 1, is characterized in that: be excessive 8-12% to the phosphoric acid adding in raw material sulphuric acid sodium waste water, the mass concentration of phosphoric acid is 84-86%.
4. method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater according to claim 1, is characterized in that: be excessive 10% to the phosphoric acid adding in raw material sulphuric acid sodium waste water, the mass concentration of phosphoric acid is 85%.
5. method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater according to claim 1, is characterized in that: while adding milk of lime first, control pH value 2.8 ~ 3.0; While continuing to add milk of lime, control pH value 6.6 ~ 6.8.
6. method of producing calcium phosphate salt and sodium phosphate salt with sodium sulfate wastewater according to claim 1, is characterized in that: while adding milk of lime first, control pH value 2.9; While continuing to add milk of lime, control pH value 6.7.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410396598.0A CN104150456B (en) | 2014-08-13 | 2014-08-13 | The method producing synthos and sodium ascorbyl phosphate with sodium sulfate wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410396598.0A CN104150456B (en) | 2014-08-13 | 2014-08-13 | The method producing synthos and sodium ascorbyl phosphate with sodium sulfate wastewater |
Publications (2)
Publication Number | Publication Date |
---|---|
CN104150456A true CN104150456A (en) | 2014-11-19 |
CN104150456B CN104150456B (en) | 2016-06-08 |
Family
ID=51876127
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410396598.0A Active CN104150456B (en) | 2014-08-13 | 2014-08-13 | The method producing synthos and sodium ascorbyl phosphate with sodium sulfate wastewater |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104150456B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106241851A (en) * | 2016-07-26 | 2016-12-21 | 四川高绿平环境科技有限公司 | A kind of processing method of useless phosphoric acid,diluted |
CN117902610A (en) * | 2024-01-19 | 2024-04-19 | 天津大学 | Method for recycling sodium sulfate high-salt wastewater |
CN117902610B (en) * | 2024-01-19 | 2024-07-05 | 天津大学 | Method for recycling sodium sulfate high-salt wastewater |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87103218A (en) * | 1987-04-26 | 1988-11-23 | 杜良才 | Novel method with saltcake production SODIUMNITRATE |
CN1285312A (en) * | 1999-08-22 | 2001-02-28 | 李怀然 | novel process for preparing fodder grade calcium hydrophosphate and by-product calcium carbonate and ammonium chloride by hydrochloric acid method |
CN103880209A (en) * | 2014-03-12 | 2014-06-25 | 广东宇星阻燃新材有限公司 | Processing method of sodium sulfate wastewater |
-
2014
- 2014-08-13 CN CN201410396598.0A patent/CN104150456B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN87103218A (en) * | 1987-04-26 | 1988-11-23 | 杜良才 | Novel method with saltcake production SODIUMNITRATE |
CN1285312A (en) * | 1999-08-22 | 2001-02-28 | 李怀然 | novel process for preparing fodder grade calcium hydrophosphate and by-product calcium carbonate and ammonium chloride by hydrochloric acid method |
CN103880209A (en) * | 2014-03-12 | 2014-06-25 | 广东宇星阻燃新材有限公司 | Processing method of sodium sulfate wastewater |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106241851A (en) * | 2016-07-26 | 2016-12-21 | 四川高绿平环境科技有限公司 | A kind of processing method of useless phosphoric acid,diluted |
CN106241851B (en) * | 2016-07-26 | 2018-01-05 | 四川高绿平环境科技有限公司 | A kind of processing method of useless phosphoric acid,diluted |
CN117902610A (en) * | 2024-01-19 | 2024-04-19 | 天津大学 | Method for recycling sodium sulfate high-salt wastewater |
CN117902610B (en) * | 2024-01-19 | 2024-07-05 | 天津大学 | Method for recycling sodium sulfate high-salt wastewater |
Also Published As
Publication number | Publication date |
---|---|
CN104150456B (en) | 2016-06-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105060545A (en) | System and method for softening treatment of desulfurization wastewater of coal-fired power plant | |
CN104628206A (en) | Recycling technique of lithium iron phosphate production wastewater | |
CN103880209B (en) | A kind for the treatment of process of sodium sulfate wastewater | |
CN103408460B (en) | Recovery method of secondary products of iminodiacetonitrile and mother liquid treatment method | |
CN105585179A (en) | Recycling method for mold release waste liquor of aluminum profile factory | |
CN103509063A (en) | Glucosamine sulfate production method | |
CN103011641B (en) | Method for preparing high-activity alpha type hemihydrate gypsum cementing materials by using reaction of chlorine-alkali waste liquid treating ardealite | |
CN102432046A (en) | Utilization method of chloride type salt lake brine | |
MA27370A1 (en) | PROCESS AND INSTALLATION FOR THE PRODUCTION OF LIME WATER FROM DEIONIZED WATER | |
CN109264761B (en) | Method for recycling calcium and magnesium ions in desulfurization wastewater by lime milk method | |
CN107416863B (en) | Method for preparing industrial-grade ammonium salt from wastewater generated in iron phosphate production | |
CN104016357B (en) | A kind of manganese slag for comprehensive utilizes the method for producing industrial chemicals | |
CN105293796A (en) | Method for co-production of sodalumite and gypsum through activated clay production mother liquid | |
CN103241720B (en) | Method for preparing amorphous iron phosphate by using phosphate sludge | |
CN104150456A (en) | Method for producing calcium phosphate salt and sodium phosphate salt by using sodium sulfate wastewater | |
CN102745841B (en) | Novel brown algae chemical waste calcium water recycling process | |
CN109851096B (en) | Chemical treatment method of hydrolysis process wastewater in ethyl chloride production process capable of being recycled | |
RU2550188C1 (en) | Method for producing silicate sorbent | |
CN104692557A (en) | Chemical pretreatment method and device thereof for treating high-salinity wastewater | |
CN103738967A (en) | Method for production of sodium fluosilicate from fluorine-containing acidic wastewater | |
CN209338324U (en) | A kind of system based on magnesium processes desulfurization wastewater high-purity magnesium hydroxide | |
CN106745114A (en) | A kind of method of utilization waste sulfuric acid from alkylation production magnesium sulfate and fertiliser containing magnesium | |
CN105314782A (en) | Method for cooperatively producing sodium alum and gypsum through activated clay industrial wastewater | |
CN102965722B (en) | By-product aqueous sodium persulfate solution micro emulsion method produces calcium sulfate whisker | |
CN113104869A (en) | Method for producing magnesium hydroxide and coproducing dihydrate gypsum |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20191112 Address after: No.66, Huanghe Road, Donghai Economic Development Zone, Lianyungang City, Jiangsu Province Patentee after: Jiangsu Debang Doling Health Technology Co., Ltd. Address before: 222000 No. 180, new sea road, Haizhou District, Jiangsu, Lianyungang Patentee before: Lianyungang Debang Fine Chemical Co., Ltd. |