CN201701879U - Primary brine refining agent preparation tank - Google Patents
Primary brine refining agent preparation tank Download PDFInfo
- Publication number
- CN201701879U CN201701879U CN2010202248244U CN201020224824U CN201701879U CN 201701879 U CN201701879 U CN 201701879U CN 2010202248244 U CN2010202248244 U CN 2010202248244U CN 201020224824 U CN201020224824 U CN 201020224824U CN 201701879 U CN201701879 U CN 201701879U
- Authority
- CN
- China
- Prior art keywords
- tank
- compressed air
- utility
- preparation tank
- model
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to a primary brine refining agent preparation tank, which belongs to the technical field of chemical engineering production equipment. The utility model aims at providing the primary brine refining agent preparation tank capable of using water-insoluble barium carbonate as refining agents. The utility model has the technical scheme that the primary brine refining agent preparation tank consists of a preparation tank, a high-position tank and a compressed air distributor, wherein a lifting pump is arranged between the preparation tank and the high-position tank, a discharge opening of the high-position tank is connected with the refining reaction tank through a pipeline, and the compressed air distributor is fixed at the bottom parts of the preparation tank and the high-position tank, and is connected with an air supply system through a compressed air pipeline. The utility model can use the pressure of the compressed air for stirring liquid in the preparation tank, after the barium carbonate is added, the barium carbonate is sufficiently mixed in water and is pumped into the high-position tank through the lifting pump, the stirring is carried out again through the compressed air in the high-position tank, and the barium carbonate enters the refining reaction tank to react with calcium ions and sulfate ions after being mixed to generate barium sulfate and calcium carbonate precipitates. The utility model reduces the enterprise cost and also improves the process efficiency.
Description
Technical field
The utility model relates to a kind of primary brine finishing agent make-up tank of general practicality in chlor-alkali industry, belongs to the chemical production equipment technical field.
Background technology
In chlor-alkali industry, salt is topmost raw material, ion-exchange membrane electrolysis is higher to calcium in the salt solution, magnesium, the isoionic content requirement of sulfate radical, existing technology is to remove the sulfate radical that contains in the salt solution with barium chloride, remove calcium ion with sodium carbonate, and the barium chloride price is higher, influences the totle drilling cost of product alkali.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of primary brine finishing agent make-up tank that can use water-fast brium carbonate as finishing agent.
The technical scheme that solves the problems of the technologies described above is:
A kind of primary brine finishing agent make-up tank, it is made up of make-up tank, head tank, compressed air distributor, make-up tank and head tank are respectively square or rectangle, elevator pump is installed between them, the outlet of head tank has pipeline to be connected with the refining reaction groove, the compressed air distributor is fixed on make-up tank and head tank bottom, and compressed air duct is connected with air feed system.
Above-mentioned primary brine finishing agent make-up tank, described compressed air distributor is made up of a trunk line and some subtubes, is evenly equipped with a plurality of pores on subtube.
Adopt the primary brine finishing agent make-up tank of this structure, can utilize compressed-air actuated pressure, with the liquid agitation in the make-up tank, add after the brium carbonate, brium carbonate is fully mixed in water, squeeze into head tank by elevator pump, stir by compressed air once more at head tank, enter refining reaction groove and calcium ion, sulfate ion reaction after fully mixing, generate barium sulfate and precipitation of calcium carbonate, it is water insoluble to have solved brium carbonate with this, can not be as the problem of finishing agent, both reduce entreprise cost, also improved process efficiency.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation of compressed air distributor.
Mark is as follows among the figure: make-up tank 1, compressed air distributor 2, pore 3, elevator pump 4, head tank 5, refining reaction groove 6.
The specific embodiment
Show among the figure that the utility model is by being made up of make-up tank 1, head tank 5, compressed air distributor 2.
Make-up tank 1 and head tank 5 are respectively square or rectangle, and elevator pump 4 is installed between them.The outlet of head tank 5 has pipeline to be connected with refining reaction groove 6.
The utility model adopts water-fast brium carbonate to replace barium chloride and sodium carbonate as new finishing agent.
Because brium carbonate is water insoluble, adopt the utility model can solve the water-fast problem of brium carbonate.
The course of work of the present utility model is as follows:
At first utilize compressed-air actuated pressure,, add after the brium carbonate, brium carbonate is fully mixed in water the liquid agitation in the make-up tank 1; Squeeze into head tank 5 by elevator pump 4 then, stir by compressed air once more, enter refining reaction groove 6 after fully mixing at head tank 5; In refining reaction groove 6, react at last, generate barium sulfate and precipitation of calcium carbonate with calcium ion, sulfate ion.
Claims (2)
1. primary brine finishing agent make-up tank, it is characterized in that: it is made up of make-up tank [1], head tank [5], compressed air distributor [2], make-up tank [1] and head tank [5] are respectively square or rectangle, elevator pump [4] is installed between them, the outlet of head tank [5] has pipeline to be connected with refining reaction groove [6], compressed air distributor [2] is fixed on make-up tank [1] and head tank [5] bottom, and compressed air duct is connected with air feed system.
2. primary brine finishing agent make-up tank according to claim 1 is characterized in that: described compressed air distributor [2] is made up of a trunk line and some subtubes, is evenly equipped with a plurality of pores [3] on subtube.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010202248244U CN201701879U (en) | 2010-06-13 | 2010-06-13 | Primary brine refining agent preparation tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2010202248244U CN201701879U (en) | 2010-06-13 | 2010-06-13 | Primary brine refining agent preparation tank |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201701879U true CN201701879U (en) | 2011-01-12 |
Family
ID=43439024
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2010202248244U Expired - Fee Related CN201701879U (en) | 2010-06-13 | 2010-06-13 | Primary brine refining agent preparation tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201701879U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104609505A (en) * | 2015-01-30 | 2015-05-13 | 东利科技(上海)有限公司 | Anti-hardening device of brine tank for water softener and water softener comprising same |
USD838229S1 (en) * | 2016-09-26 | 2019-01-15 | Paragon Tank Truck Equipment, Llc | Hydraulic oil cooler having steps |
-
2010
- 2010-06-13 CN CN2010202248244U patent/CN201701879U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104609505A (en) * | 2015-01-30 | 2015-05-13 | 东利科技(上海)有限公司 | Anti-hardening device of brine tank for water softener and water softener comprising same |
USD838229S1 (en) * | 2016-09-26 | 2019-01-15 | Paragon Tank Truck Equipment, Llc | Hydraulic oil cooler having steps |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110282637B (en) | Method for increasing usage amount of mirabilite type brine in ion membrane caustic soda production | |
CN102689999A (en) | Resourceful treatment method for silica gel waste water | |
CN110395749A (en) | A method of lithium chloride is prepared using the displacement reaction electrodialysis of four compartments | |
CN201701879U (en) | Primary brine refining agent preparation tank | |
CN102241448B (en) | Comprehensive utilization method of sodium sulfate wastewater | |
CN103880042A (en) | Brine refinement technique | |
CN104445337B (en) | A kind of ammonia alkali slops and bittern produce the method for low chlorine gypsum | |
CN108300855A (en) | A kind of process of the joint of double-flow containing zinc oxide leaching and mixed liquid electrolytic zinc | |
CN205347592U (en) | Processing apparatus is decomposed with light salt aquatic chlorate to electrolysis | |
CN107973330A (en) | Alkaline residue supernatant and anhydrous sodium sulphate prepare calcium sulphate dihydrate, the device of strong brine and its production method | |
CN108467044B (en) | Bipolar membrane electrolytic tank for preparing silica sol by pulping and electrolyzing silica powder | |
CN102605383A (en) | Method and device for hydrogen-circulating electrolysis and application of the method and device in production of aluminum oxide | |
CN204022953U (en) | A kind of production equipment of high purity sodium hydroxide | |
CN205892766U (en) | Contain caldo refining treatment system | |
CN101691213B (en) | Novel process for removing metal ions in wet-process phosphoric acid | |
CN205740360U (en) | A kind of isatoic anhydride waste liquid reclaims the equipment of sodium chloride | |
CN209721800U (en) | Oil water mixture efficient process equipment | |
CN204589359U (en) | The molten zinc groove of a kind of Quick uniform | |
CN101235510A (en) | Method for removing SO4(2-) ion in ionic film electrolysis sodium hydroxide light salt water | |
CN104445329B (en) | A kind of production equipment of Tai-Ace S 150 and production method | |
CN105417669A (en) | Chlor alkali production waste acid recycling method | |
CN203959955U (en) | Crude brine removal of impurities treatment unit for electrolysis | |
CN209507611U (en) | Chlor-alkali salt water primary purification system | |
CN206701066U (en) | A kind of calcium method denitrification apparatus | |
CN205988690U (en) | A kind of new saturation saline solution generating meanss |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20111130 Address after: 063305 Nanpu Development Zone, Hebei, Tangshan City Patentee after: Tangshan Sunfar Silicon Industries Co., Ltd. Address before: 063305 Nanpu Development Zone, Hebei, Tangshan City Patentee before: Tangshan Sunfar Silicon Industry Co., Ltd. |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110112 Termination date: 20170613 |
|
CF01 | Termination of patent right due to non-payment of annual fee |