CN203065171U - Brine purification treatment system - Google Patents
Brine purification treatment system Download PDFInfo
- Publication number
- CN203065171U CN203065171U CN 201220714051 CN201220714051U CN203065171U CN 203065171 U CN203065171 U CN 203065171U CN 201220714051 CN201220714051 CN 201220714051 CN 201220714051 U CN201220714051 U CN 201220714051U CN 203065171 U CN203065171 U CN 203065171U
- Authority
- CN
- China
- Prior art keywords
- outlet
- bittern
- entrance
- pump
- pipe filter
- 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
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a brine purification treatment system. The brine purification treatment system comprises a brine storage tank, and is characterized by further comprising a liquid supply pump, a pipeline mixer with a flocculant adding port, a hydrocyclone separator, a booster pump, a pipe filter and a clear water tank, wherein the outlet of the brine storage tank is connected with an inlet of the liquid supply pump, the outlet of the pipeline mixer is connected with the inlet of the hydrocyclone separator, the outlet of the hydrocyclone separator is connected with the inlet of the booster pump, the outlet of the booster pump is connected with the inlet of the pipe filter, and the outlet of the pipe filter is connected with the clear water tank. The whole set of the system has the advantages of compact structure, small floor area, high filtration efficiency, good quality of outlet water and high degree of automation.
Description
Technical field
The utility model relates to a kind of cleaning treatment system, particularly bittern purifying treatment system in a kind of salt refining process.
Background technology
Salt also is important chemical material as the indispensable part of human lives simultaneously, occupies very important position in national economy.The source of salt mainly is sea salt, well mine salt and lake salt.From preparation method, vacuum salt production is one of main method of producing purified salt and high-purity Industrial Salt.Bittern purifying is one of critical process in the vacuum process process, is to utilize physics and chemical method to remove a kind of technology of the impurity in the bittern.Owing to contain impurity such as calcium ion, magnesium ion, carbanion, organism in the raw brine, these foreign ions exist except quality product is affected, and also can cause equipment scaling, obstruction, and influence is normally used.Domestic enterprise is in order to improve product quality and input-output rate, and energy efficient has all been introduced different bittern purifying technology, and main process for purification has barium chloride method, freezing denitration method etc.In vacuum salt technology, require high to brine quality.At present, adopt calcium method and two alkaline process to cooperate and remove sulfate radical and calcium ions and magnesium ions, reach the purpose of brine refining, throw out adopts subsider to carry out separating treatment, supernatant liquid directly enters next processing unit, and the water outlet quality is low, influences quality and the output of product, the easy fouling of equipment, the salt making equipment lost of life.
Summary of the invention
Technical problem to be solved in the utility model provides a kind of water outlet quality better, rate of recovery height, the bittern purifying treatment system that environmental pollution is little, level of automation is high, the technical scheme that it adopts is: a kind of bittern purifying treatment system comprises that bittern storage tank, solution feed pump, band flocculation agent add the line mixer of entrance, wet cyclone, topping-up pump, pipe filter and water purification jar; The outlet of wherein said bittern storage tank connects the solution feed pump entrance, the outlet of described line mixer connects the entrance of wet cyclone, the outlet of described wet cyclone connects the entrance of topping-up pump, the entrance of the outlet connecting pipe formula strainer of described topping-up pump, the outlet of pipe filter connects the water purification jar.
The utility model further technical characterictic is:
Described solution feed pump liquid supply pressure is 0.3～0.4MPa.
The filtering accuracy of described pipe filter is 5 microns.
In actual applications, bittern in the bittern storage tank injects the line mixer that the band flocculation agent adds entrance through solution feed pump, add entrance by flocculation agent simultaneously and add flocculation agent, bittern mixes with flocculation agent in line mixer, suspended substance in the flocculation agent planar water, bittern is separated rapidly with throw out, tangentially enter wet cyclone through the line mixer mixed bittern that flocculates, under centrifugal action, big and heavy particulate matter is thrown to wall and rotation is discharged through the wet cyclone slag-drip opening downwards, and thinner particulate matter is discharged through the wet cyclone outlet; Enter pipe filter again after the topping-up pump supercharging, tiny particulate matter is through the interception of pipe filter filtering element, and clean bittern enters the water purification jar through the water purification mouth of pipe filter, to enter next stage salt manufacturing unit.
The beneficial effects of the utility model are: because the utility model adopts bittern storage tank, solution feed pump, band flocculation agent to add line mixer, wet cyclone, topping-up pump, pipe filter and a whole set of cleaning treatment system of water purification jar of entrance, do not changing the bittern quality in principle, the filtration efficiency height, the water outlet quality better, and whole system compact construction not only, floor space is little, the level of automation height.
Description of drawings
Fig. 1 is the utility model structure and process flow sheet.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment one:
As shown in Figure 1, a kind of bittern purifying treatment system comprises that bittern storage tank 1, solution feed pump 2, band flocculation agent add line mixer 3, wet cyclone 4, topping-up pump 5, pipe filter 6 and the water purification jar 7 of entrance; The outlet of wherein said bittern storage tank 1 connects solution feed pump 2 entrances, the outlet of described line mixer 3 connects the entrance of wet cyclone 4, the outlet of described wet cyclone 4 connects the entrance of topping-up pump 5, the entrance of the outlet connecting pipe formula strainer 6 of described topping-up pump 5, the outlet of pipe filter 6 connects water purification jar 7.In the present embodiment, described solution feed pump 2 liquid supply pressures are 0.3MPa.The filtering accuracy of described pipe filter 6 is 5 microns.In actually operating, bittern in the bittern storage tank 1 injects the line mixer 3 that the band flocculation agent adds entrance through solution feed pump 2, add entrance by flocculation agent simultaneously and add flocculation agent, bittern mixes with flocculation agent in line mixer 3, suspended substance in the flocculation agent planar water, bittern is separated rapidly with throw out, tangentially enter wet cyclone 4 through the line mixer mixed bittern that flocculates, under centrifugal action, big and heavy particulate matter is thrown to wall and rotation is discharged through the wet cyclone slag-drip opening downwards, and thinner particulate matter is discharged through wet cyclone 4 outlets; Enter pipe filter 6 again after topping-up pump 5 superchargings, tiny particulate matter is through the interception of pipe filter 6 filtering elements, and clean bittern enters water purification jar 7 through the water purification mouth of pipe filter, to enter next stage salt manufacturing unit.
Because the utility model adopts bittern storage tank, solution feed pump, band flocculation agent to add line mixer, wet cyclone, topping-up pump, pipe filter and a whole set of cleaning treatment system of water purification jar of entrance, do not changing the bittern quality in principle, the filtration efficiency height, the water outlet quality better, and whole system compact construction not only, floor space is little, the level of automation height.
Embodiment two:
As shown in Figure 1, a kind of bittern purifying treatment system comprises that bittern storage tank 1, solution feed pump 2, band flocculation agent add line mixer 3, wet cyclone 4, topping-up pump 5, pipe filter 6 and the water purification jar 7 of entrance; The outlet of wherein said bittern storage tank 1 connects solution feed pump 2 entrances, the outlet of described line mixer 3 connects the entrance of wet cyclone 4, the outlet of described wet cyclone 4 connects the entrance of topping-up pump 5, the entrance of the outlet connecting pipe formula strainer 6 of described topping-up pump 5, the outlet of pipe filter 6 connects water purification jar 7.In the present embodiment, described solution feed pump 2 liquid supply pressures are 0.35MPa.The filtering accuracy of described pipe filter 6 is 5 microns.In actually operating, bittern in the bittern storage tank 1 injects the line mixer 3 that the band flocculation agent adds entrance through solution feed pump 2, add entrance by flocculation agent simultaneously and add flocculation agent, bittern mixes with flocculation agent in line mixer 3, suspended substance in the flocculation agent planar water, bittern is separated rapidly with throw out, tangentially enter wet cyclone 4 through the line mixer mixed bittern that flocculates, under centrifugal action, big and heavy particulate matter is thrown to wall and rotation is discharged through the wet cyclone slag-drip opening downwards, and thinner particulate matter is discharged through wet cyclone 4 outlets; Enter pipe filter 6 again after topping-up pump 5 superchargings, tiny particulate matter is through the interception of pipe filter 6 filtering elements, and clean bittern enters water purification jar 7 through the water purification mouth of pipe filter, to enter next stage salt manufacturing unit.
Because the utility model adopts bittern storage tank, solution feed pump, band flocculation agent to add line mixer, wet cyclone, topping-up pump, pipe filter and a whole set of cleaning treatment system of water purification jar of entrance, do not changing the bittern quality in principle, the filtration efficiency height, the water outlet quality better, and whole system compact construction not only, floor space is little, the level of automation height.
Embodiment three:
As shown in Figure 1, a kind of bittern purifying treatment system comprises that bittern storage tank 1, solution feed pump 2, band flocculation agent add line mixer 3, wet cyclone 4, topping-up pump 5, pipe filter 6 and the water purification jar 7 of entrance; The outlet of wherein said bittern storage tank 1 connects solution feed pump 2 entrances, the outlet of described line mixer 3 connects the entrance of wet cyclone 4, the outlet of described wet cyclone 4 connects the entrance of topping-up pump 5, the entrance of the outlet connecting pipe formula strainer 6 of described topping-up pump 5, the outlet of pipe filter 6 connects water purification jar 7.In the present embodiment, described solution feed pump 2 liquid supply pressures are 0.4MPa.The filtering accuracy of described pipe filter 6 is 5 microns.In actually operating, bittern in the bittern storage tank 1 injects the line mixer 3 that the band flocculation agent adds entrance through solution feed pump 2, add entrance by flocculation agent simultaneously and add flocculation agent, bittern mixes with flocculation agent in line mixer 3, suspended substance in the flocculation agent planar water, bittern is separated rapidly with throw out, tangentially enter wet cyclone 4 through the line mixer mixed bittern that flocculates, under centrifugal action, big and heavy particulate matter is thrown to wall and rotation is discharged through the wet cyclone slag-drip opening downwards, and thinner particulate matter is discharged through wet cyclone 4 outlets; Enter pipe filter 6 again after topping-up pump 5 superchargings, tiny particulate matter is through the interception of pipe filter 6 filtering elements, and clean bittern enters water purification jar 7 through the water purification mouth of pipe filter, to enter next stage salt manufacturing unit.
Because the utility model adopts bittern storage tank, solution feed pump, band flocculation agent to add line mixer, wet cyclone, topping-up pump, pipe filter and a whole set of cleaning treatment system of water purification jar of entrance, do not changing the bittern quality in principle, the filtration efficiency height, the water outlet quality better, and whole system compact construction not only, floor space is little, the level of automation height.
Though the utility model has been described embodiment herein; but coverage of the present utility model is not limited thereto; the utility model is contained all and falls in fact on literal or under the instruction in equivalents all technical schemes within the scope of the claims, and protection domain of the present utility model is as the criterion with claims.
Claims (3)
1. a bittern purifying treatment system comprises the bittern storage tank, it is characterized in that also comprising that solution feed pump, band flocculation agent add line mixer, wet cyclone, topping-up pump, pipe filter and the water purification jar of entrance; The outlet of wherein said bittern storage tank connects the solution feed pump entrance, the outlet of described line mixer connects the entrance of wet cyclone, the outlet of described wet cyclone connects the entrance of topping-up pump, the entrance of the outlet connecting pipe formula strainer of described topping-up pump, the outlet of pipe filter connects the water purification jar.
2. bittern purifying treatment system according to claim 1, it is characterized in that: described solution feed pump liquid supply pressure is 0.3～0.4MPa.
3. bittern purifying treatment system according to claim 1, it is characterized in that: the filtering accuracy of described pipe filter is 5 microns.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220714051 CN203065171U (en) | 2012-12-21 | 2012-12-21 | Brine purification treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220714051 CN203065171U (en) | 2012-12-21 | 2012-12-21 | Brine purification treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203065171U true CN203065171U (en) | 2013-07-17 |
Family
ID=48763985
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220714051 Expired - Fee Related CN203065171U (en) | 2012-12-21 | 2012-12-21 | Brine purification treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203065171U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517248A (en) * | 2016-08-29 | 2017-03-22 | 天津膜天膜科技股份有限公司 | Refining system and refining process of brine for production of salt from sea water |
-
2012
- 2012-12-21 CN CN 201220714051 patent/CN203065171U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106517248A (en) * | 2016-08-29 | 2017-03-22 | 天津膜天膜科技股份有限公司 | Refining system and refining process of brine for production of salt from sea water |
| CN106517248B (en) * | 2016-08-29 | 2018-05-22 | 天津膜天膜科技股份有限公司 | A kind of preparing salt by working up seawater brine refining system and process for refining |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103663547B (en) | The process of acid waste water and recovery process in production process of titanium pigment | |
| CN103553246A (en) | Device and method for softening hard water by using carbon dioxide in flue gas | |
| CN202754866U (en) | Device for treating sewage in ceramic factory | |
| CN106517624B (en) | Desulfurization wastewater treatment method and system based on multistage fluidized bed crystallization | |
| CN101805075B (en) | Method for purification treatment of underground wastewater of coal mine | |
| CN103349859B (en) | Ceramic filter apparatus for separating calcium carbonate solution, and process thereof | |
| CN202016917U (en) | Secondary landfill leachate treatment system | |
| CN201610402U (en) | Recycling and deep treatment device for electronic electroplating wastewater | |
| CN102633378A (en) | Method and system for recycling catalyst from coal chemical liquid waste | |
| CN203065171U (en) | Brine purification treatment system | |
| CN103304072B (en) | Recycling method of industrial waste water | |
| CN205419995U (en) | Groundwater water processing system | |
| CN202072561U (en) | Polychlorinated biphenyl (PCB) copper-containing waste water reclaiming and treating system | |
| CN104086011A (en) | Zero discharge process suitable for waste water of viscose fiber industrial acid station | |
| CN201648139U (en) | Pure water production equipment with high recovery ratio | |
| CN201395536Y (en) | Electroplating comprehensive cleaning wastewater treatment and recovery system | |
| CN218058649U (en) | Municipal reclaimed water high-efficiency hardness-removing softening and turbidity-reducing pretreatment process device | |
| CN203346197U (en) | Integrated water purification device | |
| CN214060100U (en) | Novel reverse osmosis of high rate of recovery device | |
| CN105481142B (en) | Copper sheet abrasive waste water treatment for reuse system | |
| CN201010598Y (en) | Multifunctional water processor | |
| CN208378609U (en) | A kind of container-type water treatment equipment | |
| CN203715415U (en) | Advanced treatment system of mine water | |
| CN203976527U (en) | Deleading equipment for lead storage battery waste water | |
| CN204848509U (en) | Mud water processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20181221 |