CN204265576U - A kind of sea water desalinization strong brine zero discharge treatment device - Google Patents
A kind of sea water desalinization strong brine zero discharge treatment device Download PDFInfo
- Publication number
- CN204265576U CN204265576U CN201420623193.1U CN201420623193U CN204265576U CN 204265576 U CN204265576 U CN 204265576U CN 201420623193 U CN201420623193 U CN 201420623193U CN 204265576 U CN204265576 U CN 204265576U
- Authority
- CN
- China
- Prior art keywords
- sea water
- brine
- light salt
- connects
- electrodialysis
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a kind of sea water desalinization strong brine discharging processing device.Be made up of sea water desalinating plant, electrodialysis unit and electrodialysis light salt brine treatment unit; Sea water desalinating plant is provided with sea water desaltination suction culvert, the saliferous strong brine tube outlet of sea water desalinating plant connects strong brine dashpot; Dashpot connects the fresh feed pump of electrodialysis unit, and electrodialysis unit arranges the outer row pipeline of saturated brine, and the light salt brine outlet of electrodialysis unit connects light salt brine dashpot; The fresh feed pump of light salt brine dashpot connection handling device; Fresh feed pump connects the reaction unit of light salt brine treatment unit, and reacting material outlet connects sedimentation device, and the light salt brine of sedimentation device returns sea water desalinating plant through the circulation of circulating backwater pipeline.Adopt batch production mode to carry out emission treatment to sea water desalinization strong brine, all sea water desalinization strong brines are all recovered utilization, do not discharge sewage with high salinity.In seawater, the rate of recovery of fresh water can reach more than 75%.
Description
Technical field
The present invention relates to sea water desaltination and calculate field, particularly relate to a kind of sea water desalinization strong brine zero discharge treatment device.
Background technology
Along with the development of sea water desaltination industry, desalination by-product strong brine emission problem becomes more and more outstanding.Current sea water desalinization strong brine process is mainly adopted in two ways, and a kind of mode directly enters ocean, and second is utilize Tan Shai soil, local salt pan directly to carry out a day solar salt shan.But along with the continuous increase of sea water desaltination scale, enter marine strong brine constantly to increase, offshore pollution will be inevitable, on the other hand, along with strong brine quantity discharged continues to increase, Land Demand is shone on the beach of saltern also constantly to be increased, and with development aspect, coastland contradiction, this seriously constrains the development of sea water desaltination industry.Therefore, adopt a kind of novel sea water desalinization strong brine Zero emission device, when not a large amount of land occupation area, the amount of drawing of seawater resources is reduced by improving sea water desaltination water rate, realize the zero release of sea water desalinization strong brine, this is the inevitable choice solving sea water desaltination restraining factors.
Summary of the invention
For above demand, propose a kind of sea water desalinization strong brine zero discharge treatment device, the sealing and circulating loop that its core is made up of sea water desalinating plant, electrodialysis unit and electrodialysis light salt brine treatment unit.
Technical scheme of the present invention is as follows:
A kind of sea water desalinization strong brine Zero emission device of the present invention, is made up of sea water desalinating plant, electrodialysis unit and electrodialysis light salt brine treatment unit; Sea water desalinating plant is provided with sea water desaltination suction culvert, the saliferous strong brine tube outlet of sea water desalinating plant connects strong brine dashpot; Dashpot connects the fresh feed pump of electrodialysis unit, and electrodialysis unit arranges the outer row pipeline of saturated brine, and the light salt brine outlet of electrodialysis unit connects light salt brine dashpot; The fresh feed pump of light salt brine dashpot connection handling device; Fresh feed pump connects the reaction unit of light salt brine treatment unit, and reacting material outlet connects sedimentation device, and the light salt brine of sedimentation device returns sea water desalinating plant through the circulation of circulating backwater pipeline.
As shown in Figure 1: all light salt brines that electrodialysis unit (2) is discharged, by electrodialysis light salt brine treatment unit (3), reclaim by the present invention, again fresh water is produced for sea water desalinating plant (1).The nearly saturated brine that electrodialysis unit (2) is discharged may be used for evaporating salt manufacturing.Adopt batch production mode to carry out zero discharge treatment to sea water desalinization strong brine, make sea water desalinization strong brine all be recovered process.
Adopt batch production mode to carry out zero discharge treatment to sea water desalinization strong brine, all sea water desalinization strong brines are all recovered utilization, do not discharge sewage with high salinity.
By electrodialysis light salt brine treatment unit (3), all light salt brines that electrodialysis unit (2) is discharged are reclaimed, again produce fresh water for sea water desalinating plant (1).The nearly saturated brine that electrodialysis unit (2) is discharged may be used for evaporating salt manufacturing.
Adopt batch production mode to carry out zero discharge treatment to sea water desalinization strong brine, all sea water desalinization strong brines are all recovered utilization, do not discharge sewage with high salinity.In seawater, the rate of recovery of fresh water can reach more than 75%.
Accompanying drawing explanation
Fig. 1: sea water desalinization strong brine zero discharge treatment setting drawing.
In figure: 1 sea water desalinating plant; 2, electrodialysis unit; 3, electrodialysis light salt brine treatment unit; 4 seawater feeding pipes; 5, sea water desalinization strong brine; 6, fresh water; 7, sea water desalinization strong brine dashpot; 8, electrodialysis unit fresh feed pump; 9, the nearly saturated bittern of electrodialysis; 10, the nearly saturated bittern discharge pipe of electrodialysis (devaporation salt manufacturing); 11, electrodialysis light salt brine; 12, light salt brine dashpot; 13, light salt brine treatment unit fresh feed pump; 14, reaction unit; 15, sedimentation device; 16, circulating backwater (pipeline).
Embodiment
Below in conjunction with accompanying drawing, the present invention is described in further detail:
As shown in Figure 1: be made up of sea water desalinating plant, electrodialysis unit and electrodialysis light salt brine treatment unit; Sea water desalinating plant (1) is provided with sea water desaltination suction culvert (4), saliferous strong brine (5) tube outlet of sea water desalinating plant connects strong brine dashpot (7); Dashpot (7) connects the fresh feed pump (8) of electrodialysis unit, electrodialysis unit (2) arranges the outer row pipeline (10) of saturated brine, and the light salt brine outlet of electrodialysis unit connects light salt brine dashpot (12); The fresh feed pump (13) of light salt brine dashpot (12) connection handling device (3); Fresh feed pump (13) connects the reaction unit (14) of light salt brine treatment unit (3), reacting material outlet connects sedimentation device (15), and the light salt brine of sedimentation device (15) returns sea water desalinating plant (1) through circulating backwater pipeline (16) circulation.
Illustrate that effect is as follows:
Certain desalimtor, reverse osmosis unit is adopted to carry out sea water desaltination, its charging concentration of seawater is 3.2 ° of Be ', after pre-treatment, seawater containing salt component is mainly: sodium ion 10g/l, calcium ion 0.5g/l, magnesium ion 1.18g/l, potassium ion 0.38g/l, chlorion 18.5g/l, sulfate ion 2.35g/l, inlet amount is 550m
3/ h, enters sea water desalinating plant 1 through seawater feeding pipe 4.After sea water desalinating plant 1 processes, discharge fresh water 216m through fresh water outlet pipeline
3/ h, discharges 5 ° of Be ' strong brine 334m through sea water desalinization strong brine discharge pipe 5
3/ h, it is sodium ion 18.1g/l containing salt component, calcium ion 0.64g/l, magnesium ion 2.06g/l, potassium ion 0.66g/l, chlorion 31.2g/l, sulfate radical 5.8g/l.
Sea water desalinization strong brine enters electrodialysis unit 2, obtains light salt brine 11 and nearly saturated bittern 9.Wherein nearly saturated bittern growing amount is 37.5m
3/ h, it is sodium ions content 79.8g/l containing salt component, calcium ion 1.3g/l, magnesium ion 1.25g/l, potassium ion 3.6g/l, chlorion 131.8g/l, sulfate ion 0.46g/l.Light salt brine growing amount is 296.5m
3/ h, it is sodium ions content 10.2g/l containing salt component, calcium ion 0.56g/l, magnesium ion 2.12g/l, potassium ion 0.28g/l, chlorion 18.4g/l, sulfate ion 6.5g/l.Nearly saturated bittern can be used for evaporating salt manufacturing through discharge tube 10, and electrodialysis light salt brine 11, after dashpot 12, enters electrodialysis light salt brine treatment unit 14 through pump 13.
In electrodialysis light salt brine treatment unit 14, through chemical Treatment, calcium magnesium, ion equal size in electrodialysis light salt brine 11 are reduced, obtains 290m
3the circulating backwater 16 of/h, its containing salt component be sodium ions content 10.1g/l, calcium ion lower than 0.01g/l, magnesium ion lower than 0.01g/l, potassium ion 0.27g/l, chlorion 17.4g/l, sulfate ion 2.5g/l.This circulating backwater is lower than seawater component containing salt component, again for seawater desalination system, can improve sea water desaltination water rate, and achieve the zero release of sea water desalinization strong brine.
Claims (1)
1. a sea water desalinization strong brine zero discharge treatment device, is characterized in that being made up of sea water desalinating plant, electrodialysis unit and electrodialysis light salt brine treatment unit; Sea water desalinating plant is provided with sea water desaltination suction culvert, the saliferous strong brine tube outlet of sea water desalinating plant connects strong brine dashpot; Dashpot connects the fresh feed pump of electrodialysis unit, and electrodialysis unit arranges the outer row pipeline of saturated brine, and the light salt brine outlet of electrodialysis unit connects light salt brine dashpot; The fresh feed pump of light salt brine dashpot connection handling device; Fresh feed pump connects the reaction unit of light salt brine treatment unit, and reacting material outlet connects sedimentation device, and the light salt brine of sedimentation device returns sea water desalinating plant through the circulation of circulating backwater pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420623193.1U CN204265576U (en) | 2014-10-26 | 2014-10-26 | A kind of sea water desalinization strong brine zero discharge treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420623193.1U CN204265576U (en) | 2014-10-26 | 2014-10-26 | A kind of sea water desalinization strong brine zero discharge treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204265576U true CN204265576U (en) | 2015-04-15 |
Family
ID=52800454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420623193.1U Expired - Fee Related CN204265576U (en) | 2014-10-26 | 2014-10-26 | A kind of sea water desalinization strong brine zero discharge treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204265576U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104370396A (en) * | 2014-10-26 | 2015-02-25 | 中盐工程技术研究院有限公司 | Zero-emission treatment method and device for desalinating strong brine by using seawater |
| CN106349123A (en) * | 2016-08-25 | 2017-01-25 | 江苏德玛膜科技有限公司 | Method for separating taurine in taurine crude product mother solution |
| CN107473342A (en) * | 2017-09-22 | 2017-12-15 | 李海铱 | Using electrical potential difference separation sodium, the electron ion such as chlorine desalinizes seawater and salt making apparatus |
-
2014
- 2014-10-26 CN CN201420623193.1U patent/CN204265576U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104370396A (en) * | 2014-10-26 | 2015-02-25 | 中盐工程技术研究院有限公司 | Zero-emission treatment method and device for desalinating strong brine by using seawater |
| CN104370396B (en) * | 2014-10-26 | 2016-05-18 | 中盐工程技术研究院有限公司 | A kind of sea water desalinization strong brine Zero discharge treatment method and device |
| CN106349123A (en) * | 2016-08-25 | 2017-01-25 | 江苏德玛膜科技有限公司 | Method for separating taurine in taurine crude product mother solution |
| CN107473342A (en) * | 2017-09-22 | 2017-12-15 | 李海铱 | Using electrical potential difference separation sodium, the electron ion such as chlorine desalinizes seawater and salt making apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107459200B (en) | High-salt-content wastewater salinity resource recovery process | |
| CN111484178B (en) | Comprehensive treatment method for seawater or strong brine | |
| EP2507515B1 (en) | Economical and sustainable disposal of zero liquid discharge salt byproduct | |
| CN104370396B (en) | A kind of sea water desalinization strong brine Zero discharge treatment method and device | |
| CN105565573A (en) | Device and method for desulfurization waste water zero discharge treatment | |
| CN101056693A (en) | Water desalination process and apparatus | |
| CN203768159U (en) | Small seawater desalination device | |
| CN107954528A (en) | A kind of method of Salt production concentrated brine | |
| CN203360035U (en) | Comprehensive concentrated-seawater utilization device with solar pool | |
| CN203878018U (en) | Desulfurization wastewater recycling and zero-discharge system | |
| CN204265576U (en) | A kind of sea water desalinization strong brine zero discharge treatment device | |
| CN107311353A (en) | A kind of haline water zero-discharge treatment system | |
| CN206538490U (en) | A kind of cleaning of sea water desalinization strong brine puies forward magnesium system | |
| CN109534568A (en) | Integrated seawater resources utilization system | |
| CN102976535B (en) | Method for processing and recycling strong brine by membrane desalination process | |
| CN109796099A (en) | A kind of reverse osmosis -- positive infiltration -- seawater desalination system and method for multi-effect distilling coupling | |
| JP2013181501A (en) | Osmotic pressure power generation system | |
| CN1850645A (en) | Combined production process technology for low-cost zero-emission sea water desalination comprehensive utilization | |
| CN106800351A (en) | Full Membrane seawater desalination and strong brine utilization system | |
| CN204509027U (en) | A kind of Halite water desalination system based on tubular membrane | |
| CN204454795U (en) | A kind ofly reclaim the system that reverse osmosis concentrated water produces de-mineralized water | |
| CN206886879U (en) | Membrane separation process concentrates the processing unit of brackish water | |
| CN202440382U (en) | Sea water desalination treatment system with ultra-high recover rate | |
| CN204981442U (en) | Seawater desalination integrated equipment | |
| CN206447713U (en) | Full Membrane seawater desalination and strong brine utilization 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 |
Granted publication date: 20150415 Termination date: 20161026 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |