CN204981453U - Small -size integrated seawater desalination equipment - Google Patents
Small -size integrated seawater desalination equipment Download PDFInfo
- Publication number
- CN204981453U CN204981453U CN201520740208.7U CN201520740208U CN204981453U CN 204981453 U CN204981453 U CN 204981453U CN 201520740208 U CN201520740208 U CN 201520740208U CN 204981453 U CN204981453 U CN 204981453U
- Authority
- CN
- China
- Prior art keywords
- storage tank
- water
- water storage
- electric drive
- membrane stack
- 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
- 239000013535 sea water Substances 0.000 title claims abstract description 43
- 238000010612 desalination reaction Methods 0.000 title abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- 239000012528 membrane Substances 0.000 claims abstract description 25
- 238000001471 micro-filtration Methods 0.000 claims abstract description 17
- 239000003651 drinking water Substances 0.000 claims abstract description 5
- 235000020188 drinking water Nutrition 0.000 claims abstract description 5
- 239000013505 freshwater Substances 0.000 claims description 18
- 239000003610 charcoal Substances 0.000 claims description 14
- 230000002745 absorbent Effects 0.000 claims description 13
- 239000002250 absorbent Substances 0.000 claims description 13
- 238000011033 desalting Methods 0.000 claims description 13
- 230000010354 integration Effects 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 2
- 229910052799 carbon Inorganic materials 0.000 abstract 2
- 238000001179 sorption measurement Methods 0.000 abstract 2
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 13
- 244000005700 microbiome Species 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 239000000084 colloidal system Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 230000003612 virological effect Effects 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- KACAUYDQOUENGF-UHFFFAOYSA-N [Ta].[Ru].[Ir] Chemical compound [Ta].[Ru].[Ir] KACAUYDQOUENGF-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005286 illumination Methods 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a small -size integrated seawater desalination equipment, including sea water storage tank, micro -filtration device, the sea water storage tank is connected with the micro -filtration device through being equipped with the sea water intake pump, aqua storage tank, electrically -driven membrane system in the middle of being equipped with behind the micro -filtration device, be equipped with the active carbon adsorption device after the electrically -driven membrane system, the active carbon adsorption device is connected with the drinking water ultraviolet disinfector who is equipped with through the pipeline, drinking water ultraviolet disinfector is connected with the water storage tank that is equipped with, the water storage tank is equipped with water faucet, the utility model discloses make compact structure between each device, the integrated design production of being convenient for, it is little to have the quality, and the energy consumption is low, the advantages such as transportation installation of being convenient for.
Description
Technical field
The utility model belongs to sea water desaltination process field, discloses a kind of small-sized integrated sea water desalting equipment.
Background technology
China is the country that Freshwater resources lack, and in the proportion of wherein China's water resources, Freshwater resources are only 2.5%, and seawater resources then account for 97.5%, and sea water desaltination, as the increment technique of Freshwater resources, has become the strategic selection solving shortage of water resources; Containing a large amount of microorganism in the seawater surface seawater that particularly water temperature is higher, not only can increase sea water desalting equipment intake pressure, cause various accident, also can impact effluent quality; And in traditional sea water desalting equipment, remove the measure mainly killing microorganisms in pretreatment process of microorganism, comprise interruption chloridization process, " shock " chloridization process, use the methods such as polymer antisludging agent, although most of microorganism can be removed, thoroughly remove very difficult, and there is complex process in traditional sea water desalting equipment, floor space is large, and the large but problems such as poor processing effect of chemical consumption, are not suitable for the use of small-sized sea water desalting equipment.
Current sea water desaltination utilisation technology mainly contains: multistage flash vaporization, low-temperature multiple-effect distillation, reverse osmosis method and electroosmose process, wherein due to electrodialytic technique have that power consumption is low, low operating pressure, electric drive film stain resistance are strong, system applying flexible, operating maintenance convenience, long service life, former Water Sproading rate high, more and more extensive in the application of field of seawater desalination.
Utility model content
In order to solve traditional sea water desalting equipment complex process, floor space is large, chemical consumption is large and the problems such as poor processing effect, realizes being applicable to small-sized sea water desaltination processing demands, proposes a kind of small-sized integrated sea water desalting equipment.
The utility model is achieved through the following technical solutions:
A kind of small-sized integrated sea water desalting equipment, comprise seawater storage tank, micro-filtration, seawater storage tank is connected with micro-filtration by being provided with seawater intake pump, intermediate water storage groove, electric drive membranous system is provided with after micro-filtration, absorbent charcoal adsorber is provided with after described electric drive membranous system, described absorbent charcoal adsorber is connected with the ultraviolet disinfector be provided with by pipeline, and described ultraviolet disinfector is connected with the water tank be provided with, and described water tank is provided with drinking water faucet.
Further, described electric drive membranous system comprises dense water storage tank, fresh water storage tank, pole water storage tank, electric drive membrane stack, rectifier, one end of described dense water storage tank and fresh water storage tank is respectively equipped with middle water pump A, middle water pump B is connected with intermediate water storage groove, the other end is respectively equipped with dense water-circulating pump, fresh water circulating pump is connected with electric drive membrane stack, described pole water storage tank is connected with electric drive membrane stack by pole water-circulating pump, described dense water storage tank, fresh water storage tank, pole water storage tank and electric drive membrane stack are connected to form the complete recycle system, described electric drive membrane stack is connected with the positive and negative electrode of rectifier respectively by wire, described absorbent charcoal adsorber, is connected with electric drive membrane stack with the middle water pump C be provided with by pipeline.
Further, described equipment realizes Integration Design, PLC centralized Control, realizes automatically running.
The beneficial effect that the utility model has is as follows:
The utility model is by carrying out desalination process by technique coupling couplings such as micro-filtration, charcoal absorption, electrodialytic technique, uv sterilisations to seawater, effective removal of suspended substance in seawater, microorganism, bacterium etc. can be realized, not only achieve the raising of sea-water-desalination water producing water quality, also improve the processing efficiency of microorganism in water, reach control bacterium breeding, increase water quality and the object of mouthfeel; The utility model makes compact construction between each device simultaneously, and be convenient to integrated design and produce, have quality little, energy consumption is low, is convenient to the advantages such as transport installation.
Accompanying drawing explanation
Fig. 1 is appliance arrangement schematic diagram of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described further:
As Fig. 1, a kind of small-sized integrated sea water desalting equipment, comprise seawater storage tank 1, micro-filtration 3, seawater storage tank 1 is connected with micro-filtration 3 by being provided with seawater intake pump 2, intermediate water storage groove 4, electric drive membranous system is provided with after micro-filtration 3, absorbent charcoal adsorber 16 is provided with after described electric drive membranous system, described absorbent charcoal adsorber 16 is connected with the ultraviolet disinfector 17 be provided with by pipeline, described ultraviolet disinfector 17 is connected with the water tank 18 be provided with, and described water tank 18 is provided with drinking water faucet 19.
Described electric drive membranous system comprises dense water storage tank 7, fresh water storage tank 8, pole water storage tank 9, electric drive membrane stack 13, rectifier 14, described dense water storage tank 7 is respectively equipped with middle water pump A5 with one end of fresh water storage tank 8, middle water pump B6 is connected with intermediate water storage groove 4, the other end is respectively equipped with dense water-circulating pump 10, fresh water circulating pump 11 is connected with electric drive membrane stack 13, described pole water storage tank 9 is connected with electric drive membrane stack 13 by pole water-circulating pump 12, described dense water storage tank 7, fresh water storage tank 8, pole water storage tank 9 and electric drive membrane stack 13 are connected to form the complete recycle system, described electric drive membrane stack 13 is connected with the positive and negative electrode of rectifier 14 respectively by wire, described absorbent charcoal adsorber 16, is connected with electric drive membrane stack 13 with the middle water pump C15 be provided with by pipeline.
Describedly only remove the fluidized-bed reactor of microorganism in water by precipitation replace to micro-filtration 3 by existing, tentatively retain the microorganisms such as water suspension, bacterium, fractionated viral and large size colloid, seawater is delivered to intermediate water storage groove 4 after micro-filtration, exports electric drive membranous system to by above-mentioned intermediate water storage groove 4.
Describedly set up ultraviolet disinfector 17, the water outlet of described absorbent charcoal adsorber 16 enters ultraviolet disinfector 17 and removes Inactivation of Enteric Viruses In Water, chlamydozoan etc.
The small-sized integrated sea water desalinating plant of described one realizes Integration Design, adopts PLC centralized Control, thus realizes automatically running.
When using the utility model to carry out desalination process to seawater, seawater in seawater storage tank 1 is joined in micro-filtration 3 by seawater intake pump 2, suspended substance, bacterium, fractionated viral and large size colloid in micro-filtration 3 trap water, pass into the dense water storage tank 7 of electric drive film and fresh water storage tank 8 by the water outlet of intermediate water storage groove 5.Electric drive membrane stack median septum size 270mm*110mm used, useful area is 200cm
2, electric drive membrane stack adopts ion-exchange membrane, and both sides are respectively a pair painting ruthenium-iridium-tantalum anodic-cathodic, and internal anionic exchange membrane and cationic exchange membrane are alternately placed, and forms concentrated storage tank and fresh water storage tank, totally 6 repeating units respectively; Dense water storage tank, fresh water storage tank and pole water storage tank flow is maintained by rectifier, the water outlet of electric drive membrane stack enters absorbent charcoal adsorber 16 through middle water pump C15, absorbent charcoal material granularity used is at 4 ~ 30 orders, material adopts bamboo material, tamped density is about 0.50 ~ 0.65g/mL, absorbent charcoal adsorber water outlet enters ultraviolet disinfector, ultraviolet disinfector used can effectively produce a large amount of ultraviolet illumination, wherein 90% is the ultraviolet of the 253.7nm most with sterilization effect, enters water tank and store after sterilization.
Claims (3)
1. a small-sized integrated sea water desalting equipment, comprise seawater storage tank (1), micro-filtration (3), it is characterized in that: seawater storage tank (1) is connected with micro-filtration (3) by being provided with seawater intake pump (2), intermediate water storage groove (4) is provided with after micro-filtration (3), electric drive membranous system, absorbent charcoal adsorber (16) is provided with after described electric drive membranous system, described absorbent charcoal adsorber (16) is connected with the ultraviolet disinfector be provided with (17) by pipeline, described ultraviolet disinfector (17) is connected with the water tank be provided with (18), described water tank (18) is provided with drinking water faucet (19).
2. the small-sized integrated sea water desalting equipment of one according to claim 1, it is characterized in that: described electric drive membranous system comprises dense water storage tank (7), fresh water storage tank (8), pole water storage tank (9), electric drive membrane stack (13), rectifier (14), described dense water storage tank (7) is respectively equipped with middle water pump A(5 with one end of fresh water storage tank (8)), middle water pump B(6) be connected with intermediate water storage groove (4), the other end is respectively equipped with dense water-circulating pump (10), fresh water circulating pump (11) is connected with electric drive membrane stack (13), described pole water storage tank (9) is connected with electric drive membrane stack (13) by pole water-circulating pump (12), described dense water storage tank (7), fresh water storage tank (8), pole water storage tank (9) and electric drive membrane stack (13) are connected to form the complete recycle system, described electric drive membrane stack (13) is connected with the positive and negative electrode of rectifier (14) respectively by wire, described absorbent charcoal adsorber (16), by pipeline and the middle water pump C(15 be provided with) be connected with electric drive membrane stack (13).
3. the small-sized integrated sea water desalting equipment of one according to claim 1, is characterized in that: described equipment realizes Integration Design, PLC centralized Control, realizes automatically running.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520740208.7U CN204981453U (en) | 2015-09-23 | 2015-09-23 | Small -size integrated seawater desalination equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520740208.7U CN204981453U (en) | 2015-09-23 | 2015-09-23 | Small -size integrated seawater desalination equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204981453U true CN204981453U (en) | 2016-01-20 |
Family
ID=55115840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520740208.7U Expired - Fee Related CN204981453U (en) | 2015-09-23 | 2015-09-23 | Small -size integrated seawater desalination equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204981453U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105217854A (en) * | 2015-09-23 | 2016-01-06 | 江苏省科建成套设备有限公司 | A kind of small-sized integrated sea water desalting equipment |
-
2015
- 2015-09-23 CN CN201520740208.7U patent/CN204981453U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105217854A (en) * | 2015-09-23 | 2016-01-06 | 江苏省科建成套设备有限公司 | A kind of small-sized integrated sea water desalting equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100581640C (en) | Electro-deionization method and device for synchronously concentrating and purifying heavy metal wastewater | |
| CN205088043U (en) | Integrated seawater desalination equipment of solar drive | |
| CN102838227A (en) | System and method for treating industrial park recycled water to form power plant boiler supplemental water | |
| CN107381923A (en) | Desalinization processing unit and its method based on membrane capacitance deionization and membrane distillation | |
| CN202492891U (en) | Purified water treatment pure water conveying system | |
| CN204981453U (en) | Small -size integrated seawater desalination equipment | |
| CN211972026U (en) | Ultrapure water preparation system for laboratory | |
| CN105347583B (en) | A kind of electric drive film desalination process and its equipment | |
| CN204211580U (en) | A kind of Demineralized Water Production equipment | |
| CN204265572U (en) | A kind of hotel's softening water and direct drinking water treatment system | |
| CN205473110U (en) | Electrically -driven membrane preparation is equipment of drinking water directly | |
| CN203429000U (en) | Centralized drinking water treatment device employing ultra-filtration and partial nanofiltration in parallel connection | |
| CN202046959U (en) | Reclaimed water reusing equipment | |
| CN204981278U (en) | Dense water recycle's of reverse osmosis integrated equipment | |
| CN201762203U (en) | Emergency type movable water purification and split-charging device | |
| CN204874155U (en) | Experimental animals drinking water treatment equipment | |
| CN105060575B (en) | A kind of anti-electrodialysis of coupling and electrodialytic method for desalting seawater | |
| CN105217854A (en) | A kind of small-sized integrated sea water desalting equipment | |
| CN209974374U (en) | Sea water desalination treatment device for islands | |
| CN103224307A (en) | Continuous electro-adsorption process-based sea water desalination apparatus | |
| CN205382049U (en) | Polycrystalline silicon is with super pure water treatment system | |
| CN207659238U (en) | A kind of film electricity combination water treatment facilities | |
| CN102219321B (en) | Recycled water recycling equipment and process | |
| CN204848382U (en) | Sea water desalination device | |
| CN108793536A (en) | A method of carrying out sea water desalination using trough-electricity |
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: 20160120 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |