CN201701879U - Primary brine refining agent preparation tank - Google Patents

Primary brine refining agent preparation tank Download PDF

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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
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China
Prior art keywords
tank
compressed air
utility
preparation tank
model
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Expired - Fee Related
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CN2010202248244U
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Chinese (zh)
Inventor
周连会
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tangshan Sunfar Silicon Industries Co., Ltd.
Original Assignee
TANGSHAN SUNFAR SILICON INDUSTRY Co Ltd
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Priority to CN2010202248244U priority Critical patent/CN201701879U/en
Application granted granted Critical
Publication of CN201701879U publication Critical patent/CN201701879U/en
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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

A kind of primary brine finishing agent make-up tank
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.
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.Compressed air distributor 2 is fixed on make-up tank 1 and head tank 5 bottoms, and compressed air duct is connected with air feed system.
The utility model adopts water-fast brium carbonate to replace barium chloride and sodium carbonate as new finishing agent.
Figure BSA00000162318600021
Figure BSA00000162318600022
Figure BSA00000162318600023
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.
CN2010202248244U 2010-06-13 2010-06-13 Primary brine refining agent preparation tank Expired - Fee Related CN201701879U (en)

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

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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)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

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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