CN204325030U - Surface water melded system - Google Patents
Surface water melded system Download PDFInfo
- Publication number
- CN204325030U CN204325030U CN201420745407.2U CN201420745407U CN204325030U CN 204325030 U CN204325030 U CN 204325030U CN 201420745407 U CN201420745407 U CN 201420745407U CN 204325030 U CN204325030 U CN 204325030U
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- China
- Prior art keywords
- water
- surface water
- anion
- resin
- melded system
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model relates to a kind of surface water melded system, comprise former pond, line mixer, multi-medium filtering pond, clean water basin, described surface water melded system also comprises cation seperation column and anion column, wide aperture resin cation (R.C.) is filled in described cation seperation column, wide aperture resin anion(R.A) is filled in described anion column, resin anion(R.A) and resin cation (R.C.) adopt wide-aperture resin, the suspended substance of absorption is many, the treatment capacity of former water softening is large, softening water is effective, because the suspended substance of wide-aperture resin absorption is many, the quantity of the resin cation (R.C.) that same original sub-block needs and resin anion(R.A) is few, decrease cost of investment, simultaneously, resin cation (R.C.) is combined with resin anion(R.A), not only reduce former water conductivity, also make anion-cation balance, make the surface water after process in neutral.
Description
Technical field
The utility model relates to a kind of surface water melded system, especially a kind of surface water melded system removing calcium ion in surface water, magnesium ion and reduction surface water electric conductivity.
Background technology
Industrial raw water is as contained divalent-metal ion and the dissolved oxygens such as calcium divalent-metal ion, magnesium in the surface water such as natural river water, tap water, well water, often be called hard water, residual sour calcium, Magnesium hydrogen carbonate or magnesium hydroxide and so on throw out can be produced after heating, be attached to the equipment internal surface that is heated such as boiler and form hard incrustation scale, incrustation scale greatly affects the capacity of heat transmission after generating, reduce the heat effect of boiler, greatly waste energy.Simultaneously, zwitterion in process water is too many, causes electric conductivity high, adopts cation seperation column to remove calcium divalent-metal ion, magnesium divalent-metal ion in former water in prior art, cause the zwitterion in process water uneven, thus cause process water meta-alkalescence or slant acidity.
Therefore, be necessary to provide a kind of surface water melded system, to solve the problem.
Utility model content
The purpose of this utility model provides a kind of surface water melded system removing calcium ion in surface water, magnesium ion and reduction surface water electric conductivity.
The technical scheme realizing the utility model object is, a kind of surface water melded system, comprise former pond, line mixer, multi-medium filtering pond, clean water basin, described surface water melded system also comprises some pipelines, described former pond, line mixer, multi-medium filtering pond, cation seperation column, anion column, clean water basin are connected in turn by described some pipelines, described surface water melded system also comprises cation seperation column and anion column, fill wide aperture resin cation (R.C.) in described cation seperation column, in described anion column, fill wide aperture resin anion(R.A).
As prioritization scheme of the present utility model, described surface water melded system also comprises grug feeding jar and volume pump, described grug feeding jar is connected on described line mixer by described volume pump, add flocculation agent in described grug feeding jar, in described grug feeding jar, flocculation agent is delivered in described line mixer by described volume pump.
As prioritization scheme of the present utility model, described surface water melded system also comprises the water pump be installed at the bottom of pond, described former pond, former water in described former pond is delivered in described line mixer by described water pump, surface water fully mixes in described line mixer with described flocculation agent, described surface water forms flock after fully mixing with described flocculation agent, and described flock adsorbs suspended substance in former water.
As prioritization scheme of the present utility model, described surface water melded system also comprises the filler be positioned in described more medium filter, and described flock tackled by described filler, is separated by described flock with described former water.
As prioritization scheme of the present utility model, described former pond is provided with water inlet pipe.
Compared with prior art, the utility model surface water melded system at least has the following advantages: resin anion(R.A) and resin cation (R.C.) adopt wide-aperture resin, the suspended substance of absorption is many, the treatment capacity of former water softening is large, softening water is effective, because the suspended substance of wide-aperture resin absorption is many, the quantity of the resin cation (R.C.) that same original sub-block needs and resin anion(R.A) is few, decrease cost of investment, simultaneously, resin cation (R.C.) is combined with resin anion(R.A), not only reduce former water conductivity, also make anion-cation balance, make the surface water after process in neutral.
Accompanying drawing explanation
In order to make content of the present utility model more easily be clearly understood, below according to specific embodiment also by reference to the accompanying drawings, the utility model is described in further detail:
Fig. 1 is the structural representation of surface water melded system of the present utility model.
Embodiment
The utility model is a kind of surface water melded system, is described further working mechanism of the present utility model below in conjunction with accompanying drawing.
As shown in Figure 1, it is provided with former pond 2, pipeline synthesizer 4, volume pump 5, grug feeding jar 6, more medium filter 7, cation seperation column 10, anion column 12, clean water basin 13, be positioned over the filler 8 in more medium filter 7, fill the resin cation (R.C.) 9 of cation seperation column 10, fill the resin anion(R.A) 11 of anion column 12, be installed on the water inlet pipe 1 on former pond 2, be installed on the water pump 3 at the bottom of pond, former pond 2, be installed on line mixer 4 between former pond 2 and multi-medium filtering pond 7 and by former pond 2, pipeline synthesizer 4, more medium filter 7, cation seperation column 10, anion column 12, the pipeline 14 that clean water basin 13 are connected in turn, grug feeding jar 6 is connected on line mixer 4 by volume pump 5.
Surface water inputs in former pond 2 by water inlet pipe 1, be delivered in pipeline coagulation device 4 by water pump 3 again, flocculation agent (as polymerize aluminum chloride etc.) is added in grug feeding jar 6, be delivered in pipeline coagulation device 4 by volume pump 5, flock is formed after surface water is fully mixed with flocculation agent, flock adsorbs suspended substance in former water, then flock and former water flow into more medium filter 7, filled 8 tackled, filler 8 plays the effect of filtration, flock is separated with former water, former water flow in cation seperation column 10 from more medium filter 7, calcium divalent-metal ion in former water, the positively charged ions such as divalent-metal ion such as magnesium are combined with resin cation (R.C.) 9, remove the calcium divalent-metal ion in former water, the divalent-metal ions such as magnesium, then, former water flows in anion column 12, sulfate radical in former water, hydroxide radical, the negatively charged ion such as divalent sulfur are combined with resin anion(R.A) 11, remove the sulfate radical in former water, hydroxide radical, the negatively charged ion such as divalent sulfur, finally, former water after softening flows into clean water basin 13.
Resin anion(R.A) 11 and resin cation (R.C.) 9 adopt wide-aperture resin, the suspended substance of absorption is many, and the treatment capacity of former water softening is large, and softening water is effective, because the suspended substance of wide-aperture resin absorption is many, the resin cation (R.C.) 9 that same original sub-block needs is few with the quantity of resin anion(R.A) 11, decreases cost of investment, simultaneously, resin cation (R.C.) 9 is combined with resin anion(R.A) 11, not only reduce former water conductivity, also make anion-cation balance, make the surface water after process in neutral.
Above-described specific embodiment; the purpose of this utility model, technical scheme and beneficial effect are further described; be understood that; the foregoing is only specific embodiment of the utility model; be not limited to the utility model; all within spirit of the present utility model and principle, any amendment made, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. a surface water melded system, comprise former pond, line mixer, multi-medium filtering pond, clean water basin, it is characterized in that: described surface water melded system also comprises cation seperation column and anion column, described surface water melded system also comprises some pipelines, described former pond, line mixer, multi-medium filtering pond, cation seperation column, anion column, clean water basin are connected in turn by described some pipelines, fill wide aperture resin cation (R.C.) in described cation seperation column, in described anion column, fill wide aperture resin anion(R.A).
2. surface water melded system according to claim 1, it is characterized in that: described surface water melded system also comprises grug feeding jar and volume pump, described grug feeding jar is connected on described line mixer by described volume pump, add flocculation agent in described grug feeding jar, in described grug feeding jar, flocculation agent is delivered in described line mixer by described volume pump.
3. surface water melded system according to claim 2, it is characterized in that: described surface water melded system also comprises the water pump be installed at the bottom of pond, described former pond, former water in described former pond is delivered in described line mixer by described water pump, surface water fully mixes in described line mixer with described flocculation agent, described surface water forms flock after fully mixing with described flocculation agent, and described flock adsorbs suspended substance in former water.
4. surface water melded system according to claim 3, is characterized in that: described surface water melded system also comprises the filler be positioned in described more medium filter, and described flock tackled by described filler, is separated by described flock with described former water.
5. surface water melded system according to claim 1, is characterized in that: described former pond is provided with water inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420745407.2U CN204325030U (en) | 2014-12-02 | 2014-12-02 | Surface water melded system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420745407.2U CN204325030U (en) | 2014-12-02 | 2014-12-02 | Surface water melded system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204325030U true CN204325030U (en) | 2015-05-13 |
Family
ID=53161409
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420745407.2U Expired - Fee Related CN204325030U (en) | 2014-12-02 | 2014-12-02 | Surface water melded system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204325030U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106587439A (en) * | 2016-12-30 | 2017-04-26 | 资阳海天水务有限公司 | Tap water production process based on use of metal film |
-
2014
- 2014-12-02 CN CN201420745407.2U patent/CN204325030U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106587439A (en) * | 2016-12-30 | 2017-04-26 | 资阳海天水务有限公司 | Tap water production process based on use of metal film |
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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: 20150513 Termination date: 20171202 |