CN203853091U - Ion exchanger control device with sodium ion monitor - Google Patents
Ion exchanger control device with sodium ion monitor Download PDFInfo
- Publication number
- CN203853091U CN203853091U CN201420146575.XU CN201420146575U CN203853091U CN 203853091 U CN203853091 U CN 203853091U CN 201420146575 U CN201420146575 U CN 201420146575U CN 203853091 U CN203853091 U CN 203853091U
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- Prior art keywords
- valve
- brine
- monitor
- sodion
- interchanger
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Abstract
The utility model relates to a control device and especially relates to an ion exchanger control device with a sodium ion monitor. The ion exchanger control device with the sodium ion monitor comprises a general water inlet pipe (1), a branch pipe A (2), a branch pipe B (3), an exchanger A (4), an exchanger B (5), a general water outlet pipe (6), a salt water tank (7) and a controller (8). According to the ion exchanger control device provided by the utility model, resin in the exchangers has the advantages of up-flow regeneration, low salt consumption and long regeneration period. The quality of water is monitored through various monitors, and when the quality does not accord with the standard, pumps and valves are controlled to be opened and closed through the controller, so that full-automatic operation can be realized and labor is saved. The control device has the advantages of less auxiliary equipment and investment saving. The two exchangers are used for alternatively backwashing, regenerating and front washing, so that the continuity of generation of soft water can be ensured.
Description
Technical field
The utility model relates to a kind of control device, especially includes the ion exchange controller of sodion monitor.
Background technology
Existing Na-ion exchanger will be regenerated after operation a period of time, during regeneration, will stop water correction, affected the continuous production of demineralized water, because carrying out Na-ion exchanger regeneration, need supporting auxiliary device many, operated valve is many, joint connection in site pipeline is many, if operating personnel are unfamiliar with the function of pipeline, easily to equipment and valve maloperation, do not cause water outlet up to standard or whole system loine pressure is raise and make pipe breakage, therefore, connecting pipe between each equipment, valves etc. all need scene to install, debugging, investment cost is large, floor space is large, complex operation, Gei Ge industrial and mining enterprises have brought very burden, and make resin regeneration not thorough, and salt consumption is large, operating cost is high.
Summary of the invention
The utility model is for the deficiencies in the prior art, provides a kind of counter-current regeneration, salt consumption is low, the regeneration period is long, operation full-automation, and auxiliary device is few, reduced investment, uninterruptedly produces the ion exchange controller that has sodion monitor of soft water.
For achieving the above object, the technical solution that the utility model adopts is:
The ion exchange controller that has sodion monitor, comprises water inlet manifold, A arm, B arm, A interchanger, B interchanger, total outlet pipe, brine tank, controller;
Water inlet manifold is connected with total outlet pipe by A arm, B arm;
On A arm, along water inlet direction, be provided with successively A water intaking valve, A interchanger, A sodion monitor, A outlet valve, on B arm, along water inlet direction, be provided with successively B water intaking valve, B interchanger, B sodion monitor, B outlet valve, total outlet pipe is provided with total outlet valve;
The sewage draining exit of A interchanger is provided with C sodion monitor and A blowoff valve successively;
The sewage draining exit of B interchanger is provided with D sodion monitor and B blowoff valve successively;
The water inlet of brine tank is connected with total outlet pipe by pipeline, pipeline is provided with C water intaking valve, in brine tank, be provided with liquid level sensor, the delivery port of brine tank is connected with brine pump by pipeline, brine pump is connected with A arm, B arm after A interchanger, B interchanger by pipeline, and pipeline is provided with A brine valve, B brine valve;
A water intaking valve, A sodion monitor, A outlet valve, B water intaking valve, B sodion monitor, B outlet valve, total outlet valve, C sodion monitor, A blowoff valve, D sodion monitor, B blowoff valve, C water intaking valve, liquid level sensor, brine pump, A brine valve, B brine valve are connected with controller by holding wire.
Described brine pump is measuring pump or membrane pump.
Described controller is PLC controller.
Described A water intaking valve, A outlet valve, B water intaking valve, B outlet valve, total outlet valve, A blowoff valve, B blowoff valve, C water intaking valve, A brine valve, B brine valve are motor-driven valve.
While producing soft water, controller opens A water intaking valve, A outlet valve, B water intaking valve, B outlet valve, total outlet valve, close A blowoff valve, B blowoff valve, C water intaking valve, brine pump, A brine valve, B brine valve; Hard water is from water inlet manifold after A interchanger, B interchanger exchange, and soft water enters subsequent processing from total outlet valve.
When the numerical value of A sodion monitor reaches certain value, start the anti-A of cleaning interchanger, controller cuts out A water intaking valve, opens A blowoff valve; The soft water part that B interchanger produces is back to A interchanger through A outlet valve A interchanger is carried out to backwash; After a period of time, controller cuts out A outlet valve, opens brine pump and A brine valve, and the salt solution in brine tank is squeezed in A interchanger resin is wherein regenerated; After a period of time, controller cuts out brine pump and A brine valve, opens A water intaking valve, allows hard water enter A interchanger it is just washed; When the numerical value of C sodion monitor reaches certain value, controller opens A outlet valve, closes A blowoff valve, allows A interchanger carry out normal soft water production.
When the numerical value of B sodion monitor reaches certain value, start the anti-B of cleaning interchanger, controller cuts out B water intaking valve, opens B blowoff valve; The soft water part that A interchanger produces is back to B interchanger through B outlet valve B interchanger is carried out to backwash; After a period of time, controller cuts out B outlet valve, opens brine pump and B brine valve, and the salt solution in brine tank is squeezed in B interchanger resin is wherein regenerated; After a period of time, controller cuts out brine pump and B brine valve, opens B water intaking valve, allows hard water enter B interchanger it is just washed; When the numerical value of D sodion monitor reaches certain value, controller opens B outlet valve, closes B blowoff valve, allows B interchanger carry out normal soft water production.
The numerical value of the liquid level sensor in brine tank is during lower than certain value, and controller opens C water intaking valve flows in brine tank by soft water, and when the numerical value of liquid level sensor is during higher than certain value, controller cuts out C water intaking valve, completes supplementing brine tank water liquid.
the beneficial effects of the utility model:
1, the resin in the utility model interchanger is counter-current regeneration, salt consumption is low, the regeneration period is long.
2, the utility model is by the quality of various monitoring instruments monitoring water quality, when not meeting Time Controller and control the switching of each pump and valve, realized operation full-automatic, saved manpower.
3, few, the reduced investment of the utility model auxiliary device.
4, the utility model replaces backwash, regeneration, just washes with two interchangers, has guaranteed that soft water is produced uninterrupted.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
1-water inlet manifold, 2-A arm, 3-B arm, 4-A interchanger, 5-B interchanger, the total outlet pipe of 6-, 7-brine tank, 8-controller, 9-A water intaking valve, 10-A sodion monitor, 11-A outlet valve, 12-B water intaking valve, 13-B sodion monitor, 14-B outlet valve, the total outlet valve of 15-, 16-C sodion monitor, 17-A blowoff valve, 18-D sodion monitor, 19-A blowoff valve, 20-C water intaking valve, 21-liquid level sensor, 22-brine pump, 23-A brine valve, 24-B brine valve.
Specific embodiment
embodiment 1
As shown in Figure 1, there is the ion exchange controller of sodion monitor, comprise water inlet manifold 1, A arm 2, B arm 3, A interchanger 4, B interchanger 5, total outlet pipe 6, brine tank 7, controller 8;
Water inlet manifold 1 is connected with total outlet pipe 6 by A arm 2, B arm 3;
On A arm 2, along water inlet direction, be provided with successively A water intaking valve 9, A interchanger 4, A sodion monitor 10, A outlet valve 11, on B arm, along water inlet direction, be provided with successively B water intaking valve 12, B interchanger 5, B sodion monitor 13, B outlet valve 14, total outlet pipe 6 is provided with total outlet valve 15;
The sewage draining exit of A interchanger 4 is provided with C sodion monitor 16 and A blowoff valve 17 successively;
The sewage draining exit of B interchanger 5 is provided with D sodion monitor 18 and B blowoff valve 19 successively;
The water inlet of brine tank 7 is connected with total outlet pipe by pipeline, pipeline is provided with C water intaking valve 20, in brine tank 7, be provided with liquid level sensor 21, the delivery port of brine tank 7 is connected with brine pump 22 by pipeline, brine pump 22 is connected with A arm 2, B arm 3 after A interchanger 4, B interchanger 5 by pipeline, and pipeline is provided with A brine valve 23, B brine valve 24;
A water intaking valve 9, A sodion monitor 10, A outlet valve 11, B water intaking valve 12, B sodion monitor 13, B outlet valve 14, total outlet valve 15, C sodion monitor 16, A blowoff valve 17, D sodion monitor 18, B blowoff valve 19, C water intaking valve 20, liquid level sensor 21, brine pump 22, A brine valve 23, B brine valve 24 are connected with controller 8 by holding wire.
Described brine pump 22 is measuring pump.
Described controller 8 is PLC controller.
Described A water intaking valve 9, A outlet valve 11, B water intaking valve 12, B outlet valve 14, total outlet valve 15, A blowoff valve 17, B blowoff valve 19, C water intaking valve 20, A brine valve 23, B brine valve 24 are motor-driven valve.
While producing soft water, controller 8 is opened A water intaking valve 9, A outlet valve 11, B water intaking valve 12, B outlet valve 14, total outlet valve 15, closes A blowoff valve 17, B blowoff valve 19, C water intaking valve 20, brine pump 22, A brine valve 23, B brine valve 24; Hard water is from water inlet manifold 1 after A interchanger 4, B interchanger 5 exchange, and soft water enters subsequent processing from total outlet valve 15.
When the numerical value of A sodion monitor 10 reaches certain value, start the anti-A of cleaning interchanger 4, controller 8 cuts out A water intaking valve 9, opens A blowoff valve 17; The soft water part that B interchanger 5 produces is back to 4 pairs of A interchangers of A interchanger 4 through A outlet valve 11 and carries out backwash; After a period of time, controller 8 cuts out A outlet valve 11, opens brine pump 22 and A brine valve 23, and the salt solution in brine tank 7 is squeezed in A interchanger 4 resin is wherein regenerated; After a period of time, controller 8 cuts out brine pump 22 and A brine valve 23, opens A water intaking valve 9, allows hard water enter A interchanger 4 it is just washed; When the numerical value of C sodion monitor 16 reaches certain value, controller 8 is opened A outlet valve 11, closes A blowoff valve 17, allows A interchanger 4 carry out normal soft water production.
When the numerical value of B sodion monitor 13 reaches certain value, start the anti-B of cleaning interchanger 5, controller 8 cuts out B water intaking valve 12, opens B blowoff valve 19; The soft water part that A interchanger 4 produces is back to 5 pairs of B interchangers of B interchanger 5 through B outlet valve 14 and carries out backwash; After a period of time, controller 8 cuts out B outlet valve 14, opens brine pump 22 and B brine valve 24, and the salt solution in brine tank 7 is squeezed in B interchanger 5 resin is wherein regenerated; After a period of time, controller 8 cuts out brine pump 22 and B brine valve 24, opens B water intaking valve 12, allows hard water enter B interchanger 5 it is just washed; When the numerical value of D sodion monitor 18 reaches certain value, controller 8 is opened B outlet valve 14, closes B blowoff valve 19, allows B interchanger 5 carry out normal soft water production.
The numerical value of the liquid level sensor 21 in brine tank 7 is during lower than certain value, controller 8 is opened C water intaking valve 20 allows soft water flow in brine tank 7, when the numerical value of liquid level sensor 21 is during higher than certain value, controller 8 cuts out C water intaking valve 20, completes supplementing brine tank 7 water liquid.
embodiment 2
The specific embodiment is as embodiment 1, and difference is that described brine pump is membrane pump.
Claims (5)
1. the ion exchange controller that has sodion monitor, it is characterized in that, comprise water inlet manifold (1), A arm (2), B arm (3), A interchanger (4), B interchanger (5), total outlet pipe (6), brine tank (7), controller (8);
Water inlet manifold (1) is connected with total outlet pipe (6) by A arm (2), B arm (3);
A arm (2) is upper is provided with A water intaking valve (9), A interchanger (4), A sodion monitor (10), A outlet valve (11) successively along water inlet direction, on B arm, along water inlet direction, be provided with successively B water intaking valve (12), B interchanger (5), B sodion monitor (13), B outlet valve (14), total outlet pipe (6) is provided with total outlet valve (15);
The sewage draining exit of A interchanger (4) is provided with C sodion monitor (16) and A blowoff valve (17) successively;
The sewage draining exit of B interchanger (5) is provided with D sodion monitor (18) and B blowoff valve (19) successively;
The water inlet of brine tank (7) is connected with total outlet pipe by pipeline, pipeline is provided with C water intaking valve (20), in brine tank (7), be provided with liquid level sensor (21), the delivery port of brine tank (7) is connected with brine pump (22) by pipeline, brine pump (22) is connected with A arm (2), B arm (3) after A interchanger (4), B interchanger (5) by pipeline, and pipeline is provided with A brine valve (23), B brine valve (24);
A water intaking valve (9), A sodion monitor (10), A outlet valve (11), B water intaking valve (12), B sodion monitor (13), B outlet valve (14), total outlet valve (15), C sodion monitor (16), A blowoff valve (17), D sodion monitor (18), B blowoff valve (19), C water intaking valve (20), liquid level sensor (21), brine pump (22), A brine valve (23), B brine valve (24) are connected with controller (8) by holding wire.
2. the ion exchange controller that has sodion monitor according to claim 1, is characterized in that, described brine pump (22) is measuring pump or membrane pump.
3. the ion exchange controller that has sodion monitor according to claim 1 and 2, is characterized in that, described controller (8) is PLC controller.
4. the ion exchange controller that has sodion monitor according to claim 1 and 2, it is characterized in that, described A water intaking valve (9), A outlet valve (11), B water intaking valve (12), B outlet valve (14), total outlet valve (15), A blowoff valve (17), B blowoff valve (19), C water intaking valve (20), A brine valve (23), B brine valve (24) are motor-driven valve.
5. the ion exchange controller that has sodion monitor according to claim 3, it is characterized in that, described A water intaking valve (9), A outlet valve (11), B water intaking valve (12), B outlet valve (14), total outlet valve (15), A blowoff valve (17), B blowoff valve (19), C water intaking valve (20), A brine valve (23), B brine valve (24) are motor-driven valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420146575.XU CN203853091U (en) | 2014-03-29 | 2014-03-29 | Ion exchanger control device with sodium ion monitor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420146575.XU CN203853091U (en) | 2014-03-29 | 2014-03-29 | Ion exchanger control device with sodium ion monitor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203853091U true CN203853091U (en) | 2014-10-01 |
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ID=51602971
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420146575.XU Expired - Fee Related CN203853091U (en) | 2014-03-29 | 2014-03-29 | Ion exchanger control device with sodium ion monitor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203853091U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111718012A (en) * | 2019-08-19 | 2020-09-29 | 开能健康科技集团股份有限公司 | Water softener |
| CN115676971A (en) * | 2022-11-04 | 2023-02-03 | 西安热工研究院有限公司 | Ion exchange equipment operation system and method |
-
2014
- 2014-03-29 CN CN201420146575.XU patent/CN203853091U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111718012A (en) * | 2019-08-19 | 2020-09-29 | 开能健康科技集团股份有限公司 | Water softener |
| CN115676971A (en) * | 2022-11-04 | 2023-02-03 | 西安热工研究院有限公司 | Ion exchange equipment operation system and method |
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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 |
Granted publication date: 20141001 Termination date: 20150329 |
|
| EXPY | Termination of patent right or utility model |