CN201380045Y - Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water - Google Patents
Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water Download PDFInfo
- Publication number
- CN201380045Y CN201380045Y CN200920105875U CN200920105875U CN201380045Y CN 201380045 Y CN201380045 Y CN 201380045Y CN 200920105875 U CN200920105875 U CN 200920105875U CN 200920105875 U CN200920105875 U CN 200920105875U CN 201380045 Y CN201380045 Y CN 201380045Y
- Authority
- CN
- China
- Prior art keywords
- desalination
- reverse osmosis
- water
- mine water
- 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
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 71
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 37
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 28
- 238000003475 lamination Methods 0.000 claims description 22
- 238000011001 backwashing Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 7
- 238000005429 turbidity Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000001764 infiltration Methods 0.000 description 3
- 230000035621 Permeability Rate Effects 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000001186 cumulative Effects 0.000 description 2
- 238000011033 desalting Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials 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O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound 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OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 230000037250 Clearance Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000035512 clearance Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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
- Y02A20/131—Reverse-osmosis
Abstract
The utility model provides a pretreatment device and a reverse osmosis desalination apparatus for desalination of mine water. The pretreatment device comprises a water pump, a laminated filter and an ultrafilter, wherein the water pump, the laminated filter and the ultrafilter are connected sequentially via pipes. By utilizing the pretreatment device, the pretreatment process for reverse osmosis desalination is simpler, the treatment effect is better, and the volume of the device is reduced.
Description
Technical field
The utility model relates to a kind of water treatment facilities, particularly a kind of pretreatment unit of mine water desalination and reverse osmosis deaslination equipment.
Background technology
The China's coal-mine major part is in the area of lack of water, and the reclamation of mine water utilization has become the main path that solves the mine water resource shortage.At present, domestic mine water desalting processing mainly adopts the reverse osmosis deaslination treatment process.For guaranteeing counter-infiltration system long-term stability, reliability service, the preliminary treatment of counter-infiltration system is very important.The preliminary treatment of counter-infiltration system must be satisfied the water quality requirement of feed water by reverse osmosis, i.e. turbidity＜0.3NTU, pollution index FI value＜4.Pretreated main purpose is to remove suspension, turbidity, colourity, organic matter etc.If do not remove these materials, can accumulate in the film surface film is polluted, and separate out with solid form, film properties is degenerated.Finally cause the permeability rate and the salt rejection rate of film to descend, influence aquifer yield and water quality.
The pretreating process of present domestic coal mine water reverse osmosis deaslination adopts traditional more medium filter, active carbon filter, accurate filter and security personnel's filter level Four to filter.This complex treatment process, poor processing effect, and bulky, complicated operation, labour intensity is big, is difficult to adapt to the development level of present China's coal-mine.
The utility model content
The purpose of this utility model one provides a kind of pretreatment unit of mine water desalination, makes that the pretreating process of reverse osmosis deaslination is simpler, treatment effect better, the volume of reduction means.
The purpose of this utility model two provides a kind of reverse osmosis deaslination equipment, makes the desalination pretreating process more simplify, and desalting effect is better.
In order to realize purpose one, the utility model provides a kind of pretreatment unit of mine water desalination, comprising: water pump, lamination filter and ultrafilter, described water pump, lamination filter are connected by pipeline successively with ultrafilter.
By above technical scheme as can be known: the pretreatment unit of the utility model mine water desalination, water pump, lamination filter and ultrafilter are formed a single unit system, have the following advantages: simplified pretreating process, finished the work by two kinds of filters; Treatment effect is good; Dwindled the cumulative volume of device, reduced requirement installing space; Simple to operate, reduced labourer's labour intensity.
In order to realize purpose two, the utility model also provides a kind of reverse osmosis deaslination equipment, the pretreatment unit, high-pressure pump and the Reverse Osmosis Desalination Process Equipment that comprise the mine water desalination, the delivery port of the pretreatment unit of described mine water desalination, high-pressure pump and Reverse Osmosis Desalination Process Equipment are connected successively by pipeline, the pretreatment unit of described mine water desalination, comprise: water pump, lamination filter and ultrafilter, described water pump, lamination filter are connected by pipeline successively with ultrafilter.
By above technical scheme as can be known: the utility model reverse osmosis deaslination equipment, by setting up the pretreatment unit of mine water desalination, can reduce the contaminated degree of reverse osmosis membrane, prevent that film from descending because of being subjected to polluting the permeability rate and the salt rejection rate that cause film.
Also in conjunction with the accompanying drawings the utility model is described in further detail below by specific embodiment.
Description of drawings
Fig. 1 is the structural representation of the pretreatment unit of utility model mine water desalination;
Fig. 2 is the structural representation of utility model reverse osmosis deaslination equipment.
The specific embodiment
Embodiment one
As shown in Figure 1, the pretreatment unit of a kind of mine water desalination of embodiment of the present utility model comprises: water pump 1, lamination filter 2 and ultrafilter 3, described water pump 1, lamination filter 2 and ultrafilter 3 are connected successively by pipeline 5.
In concrete the application, water pump 1, lamination filter 2 and ultrafilter 3 are fixed in the same frame 4, by water pump 1 mine water is drawn in the pipeline 5.Mine water at first flows into lamination filter 2 by pipeline 5, removes suspensions such as the grains of sand, iron rust in the mine water by lamination filter 2, and reduces organic content in the mine water; Flow into ultrafilter 3 through lamination filter 2 treated waters by pipeline 5, by ultrafilter 3, materials such as bacterium, iron rust, colloid, larger molecular organics in the thorough filtering water, reservation is to the health beneficial trace elements, leading indicators such as the microorganism of purifying waste water, colourity and turbidity satisfy " GB5749-2006 drinking water sanitary standard " requirement.
By the mine water that the pretreatment unit of mine water desalination was handled, capacity of outlet water is 5～30t/h, and the water quality of water outlet can reach turbidity＜0.3NTU, pollution index FI value＜4, thus reach the preliminary treatment requirement of reverse osmosis desalinization system.
From technique scheme as can be seen, the pretreatment unit of a kind of mine water desalination of the utility model has following characteristics:
1, simplified pretreating process, treatment effect is good, has improved turbidity removal rate, pollution index FI value clearance and the water rate of recovery;
2, simple to operate, reduced labourer's labour intensity;
3, Zhuan Zhi cumulative volume is little, has reduced the requirement to installing space, and the manufacturing cost of complete equipment is descended.
Embodiment two
In described lamination filter 2, be provided with the full-automatic back washing controller.The full-automatic back washing controller under the situation of interruption of work, is not finished whole automatic backwash process in the several seconds.Automatically start backwash by the time differential pressure signal of setting, the backwash valve changes water (flow) direction in the filter element, and the impurity on the disc washes away in the lamination filter 2 with being trapped in.Reduced the workload that the staff clears up filter, reached and to reach better cleaning effect with self water consumption seldom.
Embodiment three
Set up filter 6 in water pump 1 water inlet.Can prevent that by setting up filter 6 oarse-grained impurity from entering in the package unit, avoid causing water pump 1, lamination filter 2 operating efficiencies to descend.
Embodiment four
As shown in Figure 2, a kind of reverse osmosis deaslination equipment of present embodiment, the pretreatment unit, high-pressure pump 8 and the Reverse Osmosis Desalination Process Equipment 7 that comprise the mine water desalination, the delivery port of the pretreatment unit of described mine water desalination, high-pressure pump and Reverse Osmosis Desalination Process Equipment are connected successively by pipeline 5, the pretreatment unit of described mine water desalination comprises: water pump 1, lamination filter 2 and ultrafilter 3, described water pump 1, lamination filter 2 and ultrafilter 3 are connected successively by pipeline 5.
The mine water that the pretreatment unit of process mine water desalination was handled flows into the water inlet of high-pressure pump 8 through delivery port.Mine water flows into Reverse Osmosis Desalination Process Equipment 7 through high-pressure pump 8 pressurization backs, the salinity that can remove in the water is handled in reverse osmosis deaslination through Reverse Osmosis Desalination Process Equipment 7, the entire process process does not consume chemical substances such as soda acid, has outstanding advantages such as long-term continuous operation, easy and simple to handle, water stabilization, operating cost are low, no chemical pollutant.
It should be noted that at last: above embodiment only in order to the explanation the technical solution of the utility model, is not intended to limit; Although the utility model is had been described in detail with reference to previous embodiment, those of ordinary skill in the art is to be understood that: it still can be made amendment to the technical scheme that aforementioned each embodiment put down in writing, and perhaps part technical characterictic wherein is equal to replacement; And these modifications or replacement do not make the essence of appropriate technical solution break away from the spirit and scope of each embodiment technical scheme of the utility model.
Claims (6)
1, a kind of pretreatment unit of mine water desalination is characterized in that, comprising: water pump, lamination filter and ultrafilter, described water pump, lamination filter are connected by pipeline successively with ultrafilter.
2, the pretreatment unit of mine water desalination according to claim 1 is characterized in that: be provided with the full-automatic back washing controller in the described lamination filter.
3, the pretreatment unit of mine water desalination according to claim 1 and 2 is characterized in that: the place sets up filter at described pump intake.
4, a kind of reverse osmosis deaslination equipment, the pretreatment unit, high-pressure pump and the Reverse Osmosis Desalination Process Equipment that comprise the mine water desalination, the delivery port of the pretreatment unit of described mine water desalination, high-pressure pump and Reverse Osmosis Desalination Process Equipment are connected successively by pipeline, it is characterized in that: the pretreatment unit of described mine water desalination comprises: water pump, lamination filter and ultrafilter, described water pump, lamination filter are connected by pipeline successively with ultrafilter.
5, reverse osmosis deaslination equipment according to claim 4 is characterized in that: be provided with the full-automatic back washing controller in the described lamination filter.
6, according to claim 4 or 5 described reverse osmosis deaslination equipment, it is characterized in that: the place sets up filter at described pump intake.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920105875U CN201380045Y (en) | 2009-02-24 | 2009-02-24 | Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920105875U CN201380045Y (en) | 2009-02-24 | 2009-02-24 | Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water |
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| Publication Number | Publication Date |
|---|---|
| CN201380045Y true CN201380045Y (en) | 2010-01-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920105875U Expired - Fee Related CN201380045Y (en) | 2009-02-24 | 2009-02-24 | Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water |
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| CN (1) | CN201380045Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815814A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Mine drainage water deep treatment technology |
| CN102815813A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Pretreatment process for mine drainage water |
-
2009
- 2009-02-24 CN CN200920105875U patent/CN201380045Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815814A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Mine drainage water deep treatment technology |
| CN102815813A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Pretreatment process for mine drainage water |
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Assignee: ViewSonic energy (Fukang) Coal Industry Co Ltd Assignor: National Engineering Research Center for Gas Controlling of Pingan Mine Contract record no.: 2013990000576 Denomination of utility model: Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water Granted publication date: 20100113 License type: Common License Record date: 20130911 |
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