CN202356035U - Salt dissolving device used for producing saturated brine - Google Patents

Salt dissolving device used for producing saturated brine Download PDF

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Publication number
CN202356035U
CN202356035U CN2011205075472U CN201120507547U CN202356035U CN 202356035 U CN202356035 U CN 202356035U CN 2011205075472 U CN2011205075472 U CN 2011205075472U CN 201120507547 U CN201120507547 U CN 201120507547U CN 202356035 U CN202356035 U CN 202356035U
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CN
China
Prior art keywords
salt
salt dissolving
water
saturated brine
pond
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 - Lifetime
Application number
CN2011205075472U
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Chinese (zh)
Inventor
李文华
赵营峰
李伟
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.)
China Salt Jintan Co Ltd
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China Salt Jintan Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by China Salt Jintan Co Ltd filed Critical China Salt Jintan Co Ltd
Priority to CN2011205075472U priority Critical patent/CN202356035U/en
Application granted granted Critical
Publication of CN202356035U publication Critical patent/CN202356035U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

The utility model relates to a salt dissolving device used for producing saturated brine. The salt dissolving device mainly comprises a main salt dissolving tank, an auxiliary salt dissolving tank and an adjusting tank which are connected with each other by overflow weirs, wherein water distributors connected with a water inflow pipeline are respectively installed in the main salt dissolving tank, the auxiliary salt dissolving tank and the adjusting tank. Unsaturated brine firstly enters into the main salt dissolving tank from the bottom of the main salt dissolving tank, and solid disperse wet salt is added to the main salt dissolving tank for sufficiently dissolving salt; and the saturated brine obtained after the salt is sufficiently dissolved in the main salt dissolving tank flows to the auxiliary salt dissolving tank from the overflow weir and finally enters the adjusting tank, and the saturated brine in the salt dissolving tank is transported by a pump machine. By adopting the salt dissolving device provided by the utility model, brine saturation can be effectively performed and floating salt loss is prevented.

Description

Be used to produce the change salt device of saturated brine
Technical field
The utility model relates to a kind ofization salt device, relates in particular to a kind of change salt device that is used to produce saturated brine.
Background technology
Traditionization salt device be with unsaturated salt solution by pump through delivering to of pipeline salt pond, the solid wet salt that looses is added in salt pond top, and unsaturated salt solution is directly contacted with diffusing wet salt, thus change salt.Owing to need salt deposit to keep certain height in the production process, therefore must add the wet salt that looses continuously, cause floating salt to run off easily, increase salt consumption and production cost.
The utility model content
The technical problem that the utility model will solve is that the floating salt of existingization salt device runs off seriously, causes salt consumption and production cost excessive.
The utility model provides a kind of change salt device that is used to produce saturated brine, mainly comprises masterization salt pond, pairization salt pond, regulating reservoir; Connect by downflow weir between each pond, the water-locator that connects inlet channel all is housed in each pond.
Traditionization salt device salt distance is short, and it is short to change the salt time, causes floating salt to run off easily.After increasing pairization salt pond, regulating reservoir; Change salt distance and time effectively prolong; And can turn down or close according to the unsaturated salt solution that salt deposit height in the pair salt pond will get into the masterization salt pond; Switch to pairization salt pond salt, therefore at utmost reduce floating salt and get into regulating reservoir, prevented that effectively floating salt runs off.And salt solution is in major and minorization salt pond during salt; The too high situation of salt solution salt content can occur, main cause is that unsaturated brine temp is high and the salt pond salt deposit is too high, feeds undersaturated salt solution through the regulating reservoir water-locator; The one, the salt content according to Flow-rate adjustment salt solution reaches quality requirement; The 2nd, further melt the floating salt that is deposited in the regulating reservoir.
As preferably, water-locator has at least one road water distributor, and a plurality of nozzles are arranged on each water distributor.The water-locator of many water inlet pipes in the masterization salt pond, multiinjector design can enlarge solid salt and unsaturated salt solution contact area, and not only part, preventing salt pond salt deposit is low, and the salt water saturation is not enough, and has guaranteed that wholeization salt pond do not change the salt dead angle.The water-locator of many water inlet pipes in pairization salt pond and the regulating reservoir, multiinjector design can be used for the dissolving usefulness when water flow velocity is taken away the part solid salt too soon during with salt in the masterization salt pond; And; When sodium chloride content is higher than designated value in the salt solution, can regulate its salt content through the salt solution that adds low concentration.
As preferably, the side perforate of binding of the nozzle of water-locator.When using common top to add the cap nozzle, salt and water engaging surface are long-pending little, occur piping easily, and it is many to change the salt dead angle; And nozzle binds after the perforate of side, and unsaturated salt solution delivers into the nozzle ejection through the pump machine, and current are in the lifting that makes progress of following whole salt deposit of certain pressure, and whole salt deposit is in flow regime.Can appearance salt dead angle, obtained sufficient saturated after unsaturated salt solution arrives the top from the salt deposit bottom.
As preferably, on the water-locator in the regulating reservoir flowmeter is arranged.The water yield that gets into water-locator can be effectively regulated in the installation of water-locator and flowmeter, thus the salt content of fine control salt solution.Can in storage tank and transportation,, temperature separate out when the salt solution salt content is too high owing to reducing; Increased the salt consumption like this, also caused very big waste, through the salt content of control salt solution; Not only satisfy the salt solution customer requirements well, and practiced thrift the production cost of enterprise.Reduce the solid salt consumption simultaneously, created social benefit.
As preferably, water-locator adopts steel lining sebific duct spare to connect, and nozzle is with the making of 316L stainless steel tube, pool wall fiber glass epoxy.With this raising salt device antiseptic property, increase the service life.
The technique effect that the utility model is used to produce the change salt device of saturated brine is: unsaturated salt solution at first gets into masterization salt pond from the water-locator in masterization salt pond, and the diffusing wet salt of interpolation solid is fully changed salt in the masterization salt pond; The saturated brine that the floating salt of part is carried in the masterization salt pond secretly flows into the pairization salt pond through downflow weir, and floating salt settling regularly feeds undersaturated salt solution in the water-locator in pair salt pond in the pair salt pond, effectively melt floating salt; Salt solution in the pairization salt pond gets into regulating reservoir at last; Feed undersaturated salt solution through the regulating reservoir water-locator; According to the salt content of Flow-rate adjustment salt solution, and further melt the floating salt that is deposited in the regulating reservoir, the saturated brine that will change in the salt pond through the pump machine at last is delivered to the salt water storage tank.
Description of drawings
Fig. 1 be the utility model be used for production saturated salt aquation salt schematic representation of apparatus.
Among the figure: 1. masterization salt pond, 2. pairization salt pond, 3. regulating reservoir.
The specific embodiment
Be used to produce the change salt device of saturated brine shown in the accompanying drawing 1, comprise masterization salt pond 1, pairization salt pond 2, regulating reservoir 3, connect by downflow weir between each pond, water-locator all is housed in each pond.Masterization salt pond 1, pairization salt pond 2, regulating reservoir 3 have at least one road inlet channel, and a plurality of water-locators are distributed on the inlet channel.The side perforate of binding of the nozzle of water-locator.On the water-locator in the regulating reservoir flowmeter is arranged.
Use and be somebody's turn to do when changing salt device salt: unsaturated salt solution at first gets into masterization salt pond 1 from the water-locator in masterization salt pond 1, adds the diffusing wet salt of solid in the masterization salt pond 1, fully changes salt; The saturated brine that the floating salt of part is carried in masterization salt pond 1 secretly flows into pairization salt pond 2 through downflow weir, and floating salt settling regularly feeds undersaturated salt solution in the water-locator in pair salt pond 2 in pair salt pond 2, melt floating salt; Salt solution in the pairization salt pond 2 gets into regulating reservoir 3 at last; Feed undersaturated salt solution through the water-locator in the regulating reservoir 3; According to the salt content of Flow-rate adjustment salt solution, and further melt the floating salt that is deposited in the regulating reservoir 3, the saturated brine that will change in the salt pond through the pump machine at last is delivered to the salt water storage tank.
With above-mentioned desirable embodiment according to the utility model is enlightenment, and through above-mentioned description, the related work personnel can carry out various change and modification fully in the scope that does not depart from this utility model technological thought.The technical scope of this utility model is not limited to the content on the specification, must confirm its technical scope according to the claim scope.

Claims (5)

1. a change salt device that is used to produce saturated brine is characterized in that: mainly comprise masterization salt pond (1), pairization salt pond (2), regulating reservoir (3), connected by downflow weir between each pond, the water-locator that connects inlet channel all is housed in each pond.
2. the described change salt device that is used to produce saturated brine of claim 1, it is characterized in that: water-locator has at least one road water distributor, and a plurality of nozzles are arranged on each water distributor.
3. the described change salt device that is used to produce saturated brine of claim 2 is characterized in that: the side perforate of binding of the nozzle of water-locator.
4. the described change salt device that is used to produce saturated brine of claim 1 is characterized in that: on the water-locator in the regulating reservoir (3) flowmeter is arranged.
5. the described change salt device that is used to produce saturated brine of claim 1 is characterized in that: water-locator adopts steel lining sebific duct spare to connect, and nozzle is made with stainless steel tube, the pool wall fiber glass epoxy.
CN2011205075472U 2011-12-08 2011-12-08 Salt dissolving device used for producing saturated brine Expired - Lifetime CN202356035U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011205075472U CN202356035U (en) 2011-12-08 2011-12-08 Salt dissolving device used for producing saturated brine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011205075472U CN202356035U (en) 2011-12-08 2011-12-08 Salt dissolving device used for producing saturated brine

Publications (1)

Publication Number Publication Date
CN202356035U true CN202356035U (en) 2012-08-01

Family

ID=46567254

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011205075472U Expired - Lifetime CN202356035U (en) 2011-12-08 2011-12-08 Salt dissolving device used for producing saturated brine

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CN (1) CN202356035U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105126659A (en) * 2015-07-31 2015-12-09 许继集团有限公司 Solution continuous production system and solution production method
CN106378017A (en) * 2016-08-30 2017-02-08 江苏永冠给排水设备有限公司 Saturated saline water preparation device with ladder type salt bin structure
CN107285430A (en) * 2016-04-05 2017-10-24 亚太森博(山东)浆纸有限公司 A kind of salt dissolving pond, chlor-alkali salt water treating system and chlor-alkali saline treatment technique

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105126659A (en) * 2015-07-31 2015-12-09 许继集团有限公司 Solution continuous production system and solution production method
CN107285430A (en) * 2016-04-05 2017-10-24 亚太森博(山东)浆纸有限公司 A kind of salt dissolving pond, chlor-alkali salt water treating system and chlor-alkali saline treatment technique
CN106378017A (en) * 2016-08-30 2017-02-08 江苏永冠给排水设备有限公司 Saturated saline water preparation device with ladder type salt bin structure

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CX01 Expiry of patent term

Granted publication date: 20120801

CX01 Expiry of patent term