CN101337708A - Water purifier controlled by electrovalve - Google Patents
Water purifier controlled by electrovalve Download PDFInfo
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- CN101337708A CN101337708A CNA2008101182393A CN200810118239A CN101337708A CN 101337708 A CN101337708 A CN 101337708A CN A2008101182393 A CNA2008101182393 A CN A2008101182393A CN 200810118239 A CN200810118239 A CN 200810118239A CN 101337708 A CN101337708 A CN 101337708A
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- water
- vacuum breaker
- ion exchange
- exchange column
- regenerated liquid
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- Treatment Of Water By Ion Exchange (AREA)
Abstract
The invention discloses a water purifying device controlled by an electromagnetic valve. The water purifying device comprises at least an ion exchange column A, at least an ion exchange column B, and a regenerated liquid tank; the upper outlet of the ion exchange column A is connected with a check valve A and a check valve B respectively; the upper outlet of the ion exchange column B is connected with a check valve C and a check valve D respectively; a water outlet is arranged at the middle part of a connecting pipeline; the upper outlet of the regenerated liquid tank is connected with a major cleaning electromagnetic valve through a cross joint; one of the other two ports of the cross joint is connected with the connecting pipelines of the water outlet and the check valves; the other one of the other two ports of the cross joint is connected with a regenerated liquid absorbing device and a bouffant bed electromagnetic valve; the other end of the bouffant bed electromagnetic valve is connected with the connecting pipeline between the check valve C and the check valve D; the other end of the major cleaning electromagnetic valve is connected with the lower outlets of the regenerated liquid absorbing device and the regenerated liquid tank; and a regenerating electromagnetic valve is arranged on the connecting pipeline between the upper outlet and the lower outlet of the regenerated liquid tank. The water purifying device can effectively avoid wasting the regenerated liquid, further stabilize the discharge of wastewater, eliminate water crossing, ensure flexible installation and suit popularized application.
Description
Technical field
The present invention relates to the water-purification plant of a kind of water-purification plant, particularly a kind of solenoid control.
Background technology
The water-purification plant of existing employing rotary valve control, because the preparation technology of rotary valve own is numerous and diverse, in operational process, easily make valve body wear and tear, pull, and then quality is produced in influence owing to the influence of impurities sand grains in the former water, and this maintenance of equipment difficulty is big, is difficult to promote the use of.And other water-purification plants also exist the discharge of wastewater instability, easily go here and there water, produce problems such as water quality instability, so demand developing a kind of operating temperature, easy-maintaining simple in structure, widely used novel water-purification plant urgently.
Summary of the invention
The water-purification plant that the purpose of this invention is to provide a kind of solenoid control.
The water-purification plant of solenoid control provided by the invention as shown in Figure 1, comprises at least one ion exchange column A1 and at least one ion exchange column B2 and regeneration flow container 16;
In the water-purification plant that provides in the present invention, the upper outlet of one of them of ion exchange column A1 and B2 is connected with B8 with vacuum breaker A7 respectively by Y-tube, and vacuum breaker A is positioned on the vacuum breaker B; The upper outlet of another ion exchange column is connected with vacuum breaker D10 with vacuum breaker C9 respectively by Y-tube, and vacuum breaker C is positioned on the vacuum breaker D; Vacuum breaker A links to each other with vacuum breaker C, and the middle part of connecting pipeline is provided with water outlet 26; Vacuum breaker B links to each other with vacuum breaker D;
Link to each other by two parallel pipelines between above-mentioned two ion exchange columns 1 and 2 the following outlet, one of them connecting pipeline is provided with two outage closed type entering water electromagnetic valves 3 and 4; Water-in 28 is between two outage closed type entering water electromagnetic valves; Another connecting pipeline is provided with the waste discharge mouth of a river 27, and the waste discharge mouth of a river is provided with effluent electric three-way valve 5;
The upper outlet of regeneration flow container 16 links to each other with outage closed type great purge magnetic valve 6 by four-way; Two other port of four-way, one links to each other with connecting pipeline between water outlet 26 and the vacuum breaker C9, another port successively with inhale regenerated liquid device 11 and an outage normal open type pine magnetic valve 12 links to each other; The other end of this outage normal open type pine bed magnetic valve 12 links to each other with the pipeline between vacuum breaker B and the vacuum breaker D;
The other end of above-mentioned outage closed type great purge magnetic valve 6 links to each other with the following outlet of inhaling regenerated liquid device 11 and regeneration flow container 16 respectively, and wherein, and the connecting pipeline between the following outlet of regeneration flow container is provided with outage closed type regeneration magnetic valve 14.
In the above-mentioned solenoid control water-purification plant, select single-column or multicolumn series connection for use according to the size of handling ionic weight, promptly ion exchange column A can be 2-6 ion exchange column series connection, and ion exchange column B can be 2-6 ion exchange column series connection.Can carry out serial or parallel connection according to conventional method of attachment between the adjacent ions exchange column.
For reaching better water purifying effect, can on the connecting pipeline between outage closed type regeneration magnetic valve and the regeneration flow container, be provided with to filter and irritate 19.Used vacuum breaker ABCD can select lift check valve or horizontal vacuum breaker for use; Wherein, lift check valve should vertically be installed and used in pipeline, and the horizontal vacuum breaker should level be installed and used in pipeline; In actual use, sealing, the boiling water that lift check valve can be more stable than the horizontal vacuum breaker.When selecting lift check valve for use, all vacuum breaker are straight up to opening, and downwards for closing, as shown in Figure 1, the arrow direction is the pass in the other direction for opening.When selecting the horizontal vacuum breaker for use, all vacuum breaker are level and install, and liquid flows to water outlet 26 directions for opening by vacuum breaker A7, otherwise is the pass; Liquid flows on the exchange column 1 the threeway direction for opening by vacuum breaker B8, otherwise for closing; Liquid flows on the exchange column 2 the threeway direction for opening by vacuum breaker D10, otherwise for closing.
On the connecting pipeline of inhaling between regenerated liquid device and the outage closed type regeneration magnetic valve, regenerated liquid under meter 13 is set; On water-in and two connecting pipelines that cut off the power supply between the closed type entering water electromagnetic valve, inlet gage 25 is set; At the top of filtering filling automatic exhaust steam valve 20 is set, the bottom is provided with wash water valve 22; Top at the regeneration flow container is provided with regenerated liquid cover 23, and the bottom is provided with wash water valve 21, and the side is provided with regeneration flow container visor 17; Inside at the regeneration flow container is provided with orifice plate and filter screen 18; Resin is set in the side of two cationic exchange coloums observes visor 24.
Each ion-exchange unit comprises two ion exchange columns among the present invention, can fill various Zeo-karbs (as sodium ion exchange resin) or anionite-exchange resin as required in each ion exchange column, thereby uses as sun bed or cloudy bed.Filling and the corresponding regenerator of ion exchange resin in the regeneration flow container 16.When using as the sun bed, regenerator is Industrial Salt or hydrochloric acid.When using as cloudy bed, regenerator is an alkali.
In the water-purification plant of solenoid control provided by the invention, water outlet 26 need be higher than cationic exchange coloum 1 and more than the 2 top elbow 1.7m; The waste discharge mouth of a river 27 need be higher than the resin layer of filling in cationic exchange coloum 1 and 2, and is working properly to guarantee vacuum breaker and to inhale the regenerated liquid device.
Utilize the water-purification plant of solenoid control provided by the invention, can realize producing the water purification process of water, pine bed, regeneration, little cleaning, great purge; When promptly a cationic exchange coloum produced water therein, another cationic exchange coloum was finished the technology of pine bed, regeneration, little cleaning, great purge successively.
Solenoid control water-purification plant provided by the invention, regenerated liquid irritate or filter irritate with the regenerated liquid under meter between the regeneration magnetic valve is installed, can effectively avoid inhaling regenerated liquid device (water sprayer) and cross regenerated liquid waste and the deterioration of water outlet quality that suction phenomenon causes; Vacuum breaker can be vertically or level be installed in this device pipeline, improved Installation Flexibility, when using lift check valve vertically to install, realization sealing, boiling water function that the vacuum breaker of installing than existing level can be more stable, and do not have string water phenomenon and take place; Select effluent electric three-way valve for use, more interactive stopping valve effluent is more stable, and does not have the generation of string water phenomenon.In addition, this device can be realized the pine bed step of exchange column, helps resin regeneration; This device also can be realized the great purge step, compares with the cleaning step of existing apparatus, regenerator residual in the ion exchange resin thoroughly can be cleaned up, thereby puies forward the high yield water quality.This device can be used as the sun bed or cloudy bed uses.Through the production practice of production in 3 years, the solenoid control water-purification plant that this invention provides is stable, and the purification efficiency height produces the water stay in grade, reaches the relevant national standard regulation; Utilize this device can automatically disposable all technologies of finishing the water purifying treatment, easy to operate, and this device current consumption is low, and regenerating agent consumption is low, and production cost reduces, and apparatus structure is simple, for ease of maintenaince, is suitable for very much large-scale promotion and uses.
Description of drawings
Fig. 1 is the structural representation of solenoid control water-purification plant provided by the invention.
Embodiment
The invention will be further described below in conjunction with specific embodiment, but the present invention is not limited to following examples.
Select for use 001 * 7 strongly acidic styrene type cation exchange resin to fill the exchange column of solenoid control water-purification plant provided by the invention, adorn Industrial Salt in the regeneration flow container 16.Various technical qualification are all assembled according to the relevant regulations in the national standard of " controlling the Na-ion exchanger technical qualification automatically " of being numbered GB/T18300-2001 in this device.
As shown in Figure 1, when cationic exchange coloum A1 produced water, cationic exchange coloum B2 finished the technology of pine bed, regeneration, little cleaning, great purge successively.The concrete technical process of this water-purification plant is as follows:
When cationic exchange coloum 1 produces water, below four valves remain following state: left entering water electromagnetic valve 3 is opened, vacuum breaker 7 is opened, vacuum breaker 8 cuts out, vacuum breaker 9 cuts out;
When 1) cationic exchange coloum 1 produced water, the former water water of purifying treatment (promptly without) entered exchange column 1 through water-in 28, left entering water electromagnetic valve 3, purified to finish after vacuum breaker 7 is flowed out by water outlet 26, was purified water;
In this step, used former water hardness is 8mmol/L, and purifying the back water hardness is 0.005mmol/L, reaches the national standard that is numbered GB/T1576-2001.
2) during cationic exchange coloum 2 pine bed, a pine bed magnetic valve 12 cuts out, vacuum breaker 10 cuts out, and effluent electric three-way valve 5 reaches cationic exchange coloum 2 and communicates with the waste discharge mouth of a river 27, and Zeo-karb promptly begins loose in the right post;
3) during cationic exchange coloum 2 regeneration, the magnetic valve 14 of will regenerating is opened, and manually-operated gate 15 is opened (this valve is only just being closed during with salt) in the salt flow container, effluent electric three-way valve 5 reaches cationic exchange coloum 2 and communicates with the waste discharge mouth of a river 27.
Regenerator in the regeneration flow container is a saturated nacl aqueous solution, this solution flows to hay tank 19, regeneration magnetic valve 14, regenerated liquid under meter 13 successively, inhales regenerated liquid device 11, a pine magnetic valve 12 from regeneration flow container 16, enter cationic exchange coloum 2 through vacuum breaker 10, regeneration of resin in the cationic exchange coloum 2 is finished in 27 discharges from the waste discharge mouth of a river at last;
4) during the little cleaning of cationic exchange coloum 2, softening water flows to pine bed magnetic valve 12 from top to bottom by the top aperture of inhaling regenerated liquid device 11, enter cationic exchange coloum 2 through vacuum breaker 10, the little cleaning of resin in the cationic exchange coloum 2 is finished in 27 discharges from the waste discharge mouth of a river at last;
5) during cationic exchange coloum 2 great purge, great purge magnetic valve 6 is opened, softening water enters cationic exchange coloum 2 by the suction regenerated liquid mouth of inhaling regenerated liquid device 11, pine bed magnetic valve 12, vacuum breaker 10, and the great purge of resin in the cationic exchange coloum 2 is finished in 27 discharges from the waste discharge mouth of a river at last; Cationic exchange coloum 2 great purge steps are finished simultaneously, cationic exchange coloum 1 produces water and finishes, thereby enter cationic exchange coloum 2 and produce water, exchange column 1 is meanwhile finished the technology of pine bed, regeneration, little cleaning, great purge, a cycle of operation of promptly finishing this water-purification plant successively.
When in the ion exchange column during filling male ion-exchange resin, original water hardness is when 1-20mmol/L, and only with two exchange columns, promptly a side one radical ion exchange column carries out the water purifying treatment, as mentioned above; When original water hardness during greater than 20mmol/L, can use four or above (as the six roots of sensation) and the used identical ion exchange column of present embodiment, be that cationic exchange coloum A or B use two or more (as three) exchange column respectively, cationic exchange coloum B uses two or more (as three) exchange column, connects according to the pipeline connecting method of routine between the adjacent ion exchange column of every side.
Claims (10)
1, a kind of water-purification plant of solenoid control is characterized in that: comprise at least one ion exchange column A (1) and at least one ion exchange column B (2) and regeneration flow container (16); The upper outlet of one of them of described ion exchange column A and B is connected with B (8) with vacuum breaker A (7) respectively by Y-tube, and vacuum breaker A is positioned on the vacuum breaker B; The upper outlet of described another ion exchange column is connected with vacuum breaker D (10) with vacuum breaker C (9) respectively by Y-tube, and vacuum breaker C is positioned on the vacuum breaker D; Described vacuum breaker A links to each other with vacuum breaker C, and the middle part of connecting pipeline is provided with water outlet (26); Described vacuum breaker B links to each other with vacuum breaker D;
Link to each other by two parallel pipelines between the following outlet of described two ion exchange columns (1) and (2), one of them described connecting pipeline is provided with two outage closed type entering water electromagnetic valves (3) and (4); Water-in (28) is between two described outage closed type entering water electromagnetic valves; Described another connecting pipeline is provided with the waste discharge mouth of a river (27), and the described waste discharge mouth of a river is provided with effluent electric three-way valve (5);
The last water-in of described regeneration flow container (16) links to each other with outage closed type great purge magnetic valve (6) by four-way; Two other port of described four-way, one links to each other with connecting pipeline between described vacuum breaker A (7) and the described vacuum breaker C (9), another port successively with inhale regenerated liquid device (11) and an outage normal open type pine magnetic valve (12) links to each other; The other end of described outage normal open type pine bed magnetic valve (12) links to each other with the pipeline between described vacuum breaker B and the vacuum breaker D;
The other end of described outage closed type great purge magnetic valve (6) links to each other with the following outlet of inhaling regenerated liquid device (11) and regeneration flow container (16) respectively, and the connecting pipeline between the following outlet of described and regeneration flow container is provided with the closed type of the cutting off the power supply magnetic valve (14) of regenerating.
2, solenoid control water-purification plant according to claim 1 is characterized in that: described ion exchange column A is 2-6; Described ion exchange column B is 2-6.
3, solenoid control water-purification plant according to claim 2 is characterized in that: described ion exchange column A is that serial or parallel connection connects; Described ion exchange column B is that serial or parallel connection connects.
4, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: on the connecting pipeline between described outage closed type regeneration magnetic valve and the regeneration flow container, be provided with to filter and irritate (19).
5, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: described vacuum breaker A-D is lift check valve or horizontal vacuum breaker.
6, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: on the connecting pipeline between described suction regenerated liquid device and the outage closed type regeneration magnetic valve, regenerated liquid under meter (13) is set; On the connecting pipeline between described water-in and two the described outage closed type entering water electromagnetic valves, inlet gage (25) is set.
7, solenoid control water-purification plant according to claim 4 is characterized in that: the top of irritating in described filtration is provided with automatic exhaust steam valve (20), and the bottom is provided with wash water valve (22).
8, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: regenerated liquid cover (23) is set at the top of described regeneration flow container, and the bottom is provided with wash water valve (21); Orifice plate and filter screen (18) are set in the inside of described regeneration flow container.
9, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: resin is set in the side of described two cationic exchange coloums observes visor (24); Regeneration flow container visor (17) is set in the side of described regeneration flow container.
10, according to the arbitrary described solenoid control water-purification plant of claim 1-3, it is characterized in that: described ion exchange column is cationic exchange coloum or anion-exchange column.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008101182393A CN101337708A (en) | 2008-08-11 | 2008-08-11 | Water purifier controlled by electrovalve |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2008101182393A CN101337708A (en) | 2008-08-11 | 2008-08-11 | Water purifier controlled by electrovalve |
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| Publication Number | Publication Date |
|---|---|
| CN101337708A true CN101337708A (en) | 2009-01-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2008101182393A Pending CN101337708A (en) | 2008-08-11 | 2008-08-11 | Water purifier controlled by electrovalve |
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| Country | Link |
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| CN (1) | CN101337708A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103991929A (en) * | 2014-06-06 | 2014-08-20 | 四川恒达环境技术有限公司 | Electrolytic manganese wastewater ion exchange treatment system |
| CN111153468A (en) * | 2020-03-13 | 2020-05-15 | 中国工程物理研究院动力部 | Heavy metal wastewater treatment device |
| CN116440885A (en) * | 2023-06-15 | 2023-07-18 | 徐州华睿炭材料科技有限公司 | Activated carbon recovery device |
-
2008
- 2008-08-11 CN CNA2008101182393A patent/CN101337708A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103991929A (en) * | 2014-06-06 | 2014-08-20 | 四川恒达环境技术有限公司 | Electrolytic manganese wastewater ion exchange treatment system |
| CN111153468A (en) * | 2020-03-13 | 2020-05-15 | 中国工程物理研究院动力部 | Heavy metal wastewater treatment device |
| CN116440885A (en) * | 2023-06-15 | 2023-07-18 | 徐州华睿炭材料科技有限公司 | Activated carbon recovery device |
| CN116440885B (en) * | 2023-06-15 | 2023-08-25 | 徐州华睿炭材料科技有限公司 | Activated carbon recovery device |
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Open date: 20090107 |