CN202201737U - Sodium ion exchange full-automatic controller - Google Patents
Sodium ion exchange full-automatic controller Download PDFInfo
- Publication number
- CN202201737U CN202201737U CN2011203559264U CN201120355926U CN202201737U CN 202201737 U CN202201737 U CN 202201737U CN 2011203559264 U CN2011203559264 U CN 2011203559264U CN 201120355926 U CN201120355926 U CN 201120355926U CN 202201737 U CN202201737 U CN 202201737U
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- water
- pipe
- threeway
- interchanger
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- Expired - Fee Related
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- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model relates to a sodium ion exchange full-automatic controller for water treatment, which aims at softening hardness of raw water, improving stability of water quality after treatment and reducing labor intensity and production cost of operating workers simultaneously. A second tee joint is installed on a water outlet pipe of the controller, magnetic valves are respectively arranged on two sides of the second tee joint, and softened water outlets are respectively connected onto the magnetic valves. The other end of the second tee joint is connected with an inlet of a salt tank through a pipeline, a first side pipe is further connected onto the water outlet pipe in parallel, a ball valve is arranged on the side pipe, magnetic valves are arranged on two sides of the ball valve, and a first magnetic valve is further connected with a salt water outlet of the salt tank through a pipeline respectively. A third tee joint is arranged on a water inlet pipe, magnetic valves are arranged on two sides of the third tee joint, a second side pipe is further connected onto the water inlet pipe in parallel, a fourth tee joint is arranged on the second side pipe, and magnetic valves are arranged on two sides of the fourth tee joint. A tenth magnetic valve is further arranged at the position of an inlet of the water inlet pipe. The controller adopts the magnetic valves to perform controlling, thereby achieving automatic softening, recycling and cleaning process of the water, improving production efficiency and stability of water outlet quality and reducing the production cost and the labor intensity.
Description
Technical field
The utility model relates to sodium ion exchange full automatic controller used in a kind of water treatment.
Background technology
At present water is softened in the prior art of handling, treating processes adopts solenoid control sodium ion switching equipment more, adopts the manual rotary valve door at former water admission passage more; Its weak point is that labour intensity is big, and manual rotary valve family of power and influence complex structure, because machinery control; In use; Stuck phenomenon often appears in the control moving rod, causes the valve body wearing and tearing, influences the stability of water quality; Because the error of manual operation can not in time be supplied water when anhydrous, the resin in the interchanger can not get due protection sometimes, and the rotten and inefficacy of resin causes the increase of production cost.
Summary of the invention
In order to improve the stability of handling back water quality, reduce operator's labour intensity and production cost simultaneously, the utility model provides a kind of sodium ion exchange full automatic controller.This unit adopts solenoid control, realizes softening automatically, the autoregeneration of water, cleaning process automatically, and the stability with effluent quality of enhancing productivity reduces production costs and labour intensity.
。The technical scheme of the utility model is: a kind of sodium ion exchange full automatic controller, comprise interchanger one, interchanger two and salt case, and in the upper end of interchanger one and interchanger two rising pipe that communicates is housed; The water inlet pipe that communicates is equipped with in the lower end; Wherein, threeway two is housed on above-mentioned rising pipe, adorns SV three and SV four respectively in the both sides of threeway two; SV three and SV four connect the softening water outlet again respectively; Threeway two the other ends are connected with the inlet of salt case through pipeline, and on rising pipe, also are parallel with side pipe one, adorn ball valve on the side pipe one; At the both sides of ball valve dress SV one and SV two, SV one and SV two are connected with the brine outlet of salt case through pipeline respectively again; And threeway three is housed on the described water inlet pipe, at the both sides of threeway three dress SV five and SV six, and on water inlet pipe also parallelly connected side pipe two, threeway four is housed on the side pipe two, SV seven and SV eight are adorned in the both sides of threeway four; SV ten also is equipped with in ingress at water inlet pipe.
For the needs that adapt to filtration yield and improve filtering stability, described interchanger one and interchanger two are UPVC plastics pot or metal tin; Filtering layers in described interchanger one, the interchanger two are to press silica sand on water cap device or the nylon wire.
The beneficial effect of the utility model is: this full automatic controller gets into interchanger from former water and all adopts SV whole-process automatic operation under the control of rly. to getting rid of softening water and waste water; Realize softening automatically, the autoregeneration of water; Automatically cleaning process, thus enhance productivity stability with effluent quality, safe and reliable in the operational process; Time saving and energy saving, easy to maintenance.
Description of drawings
Fig. 1 is the structural representation of the utility model.
1-rising pipe among the figure, 2-SV one, 3-ball valve, 4-SV two, 5-SV three, 6-threeway two, 7-SV four; 8-SV five, 9-threeway three, 10-SV 66,11-SV seven, 12-threeway four, 13-SV eight, 14-SV nine; The 15-water inlet pipe, 16-interchanger one, 17-interchanger two, 18-brine outlet, 19-salt case, 20-electric pump; 21-SV ten, 22-salt water inlet, the outlet of 23-softening water, 24-Sewage outlet, 25-side pipe one, 26-side pipe two.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further:
By shown in Figure 1, this sodium ion exchange full automatic controller comprises interchanger 1, interchanger 2 17 and salt case 19; In the upper end of interchanger 1 and interchanger 2 17 rising pipe 1 that communicates is housed, the water inlet pipe 15 that communicates is equipped with in interchanger 1 and interchanger 2 17 lower ends, wherein; Threeway 26 is housed on above-mentioned rising pipe 1; Adorn SV 35 and SV 47 respectively in the both sides of threeway 26, SV 35 and SV 47 connect softening water outlet 23 again respectively, and threeway 26 the other ends are connected with the inlet 22 of salt case 19 through pipeline; And on rising pipe 1, also be parallel with side pipe 1; Dress ball valve 3 on the side pipe 1, at the both sides of ball valve 3 dress SV 1 and SV 24, SV 1 and SV 24 are connected with the brine outlet 18 of salt case 19 through pipeline respectively again; And threeway 39 is housed on the described water inlet pipe 15; At the both sides of threeway 39 dress SV 58 and SV 6 10; And also parallelly connected side pipe 2 26 is equipped with threeway 4 12 on the side pipe 2 26 on water inlet pipe 15, the both sides dress SV 7 11 and the SV 8 13 of threeway 4 12; SV 10 also is equipped with in ingress at water inlet pipe 15.
In addition, for the needs that adapt to filtration yield and improve filtering stability, described interchanger 1 and interchanger 2 17 are UPVC plastics pot or metal tin, when filtration yield per hour more than 10 tons the time, adopt metal tin; And the filtering layer in described interchanger 1 and the interchanger 2 17 is to press silica sand on water cap device or the nylon wire, and it is simple in structure pressing the advantage of silica sand on the nylon wire, practices thrift cost, and duration of service is long.
The working process of this sodium ion exchange full automatic controller is following:
1, softening process: former water gets into interchanger 1 through SV 10 and SV 58 successively through pipeline, behind the resin substitution in interchanger 1, discharges softening water through SV 35 and softening water outlet 23 again;
2, regenerative process: salt solution passes through the SV 24 on pump 20 and the side pipe 25 successively through the brine outlet 18 of supersalt case 19; Get into interchanger 17; Filtering layer in interchanger 17 filters, pass through the SV 8 13 and threeway 4 12 on the side pipe 2 26 again after, discharge through Sewage outlet 24.
3, cleaning process: former water is through pipeline process SV 10 and SV 58; Get into interchanger 1; Get into interchanger 2 17 through the SV 1 on the side pipe 25, ball valve 3 and SV 24 successively again, discharge by Sewage outlet 24 through SV 8 13 on the side pipe 2 26 and threeway 4 12 backs from the lower end of interchanger 2 17.
Above-mentioned three processes are carried out simultaneously, SV 6 10 in service,, SV 47 cuts out, and other SVs are opened.Said process is provided with the set time by the time relay, by intermediate relay period rly., and two swap tank crossing operations; Wait until and accomplish working time; The time relay is controlled electromagnetic valve closed automatically and is opened, and originally opens solenoid valve is closed, and this process exchanges operation repeatedly.
This unit adopts solenoid control, can realize softening automatically, the autoregeneration of water, cleaning process automatically, and the stability with effluent quality of enhancing productivity reduces production costs and labour intensity.
Claims (3)
1. a sodium ion exchanges full automatic controller; Comprise interchanger one (16), interchanger two (17) and salt case (19); In the upper end of two interchangers (16,17) rising pipe (1) that communicates is housed, the water inlet pipe (15) that communicates is equipped with in the lower end; It is characterized in that: threeway two (6) is housed on above-mentioned rising pipe (1); Adorn SV three (5) and SV four (7) respectively in the both sides of threeway two (6), SV three (5) and SV four (7) connect softening water outlet (23) again respectively, and threeway two (6) the other ends are connected with the inlet (22) of salt case (19) through pipeline; And on rising pipe (1), also be parallel with side pipe one (25); Side pipe one (25) is gone up dress ball valve (3), and at the both sides of ball valve (3) dress SV one (2) and SV two (4), SV one (2) and SV two (4) are connected with the brine outlet (18) of salt case (19) through pipeline respectively again; And threeway three (9) is housed on the above-mentioned water inlet pipe (15); At the both sides of threeway three (9) dress SV five (8) and SV six (10); And go up also parallelly connected side pipe two (26) at water inlet pipe (15); Threeway four (12) is housed, the both sides dress SV seven (11) and the SV eight (13) of threeway four (12) on the side pipe two (26); In the ingress of water inlet pipe (15) SV ten (21) is housed also.
2. sodium ion exchange full automatic controller according to claim 1, it is characterized in that: described interchanger one (16) and interchanger two (17) are UPVC plastics pot or metal tin.
3. sodium ion exchange full automatic controller according to claim 1, it is characterized in that: the filtering layer in described interchanger one (16) and the interchanger two (17) is to press silica sand on water cap device or the nylon wire.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203559264U CN202201737U (en) | 2011-09-22 | 2011-09-22 | Sodium ion exchange full-automatic controller |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203559264U CN202201737U (en) | 2011-09-22 | 2011-09-22 | Sodium ion exchange full-automatic controller |
Publications (1)
Publication Number | Publication Date |
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CN202201737U true CN202201737U (en) | 2012-04-25 |
Family
ID=45965870
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011203559264U Expired - Fee Related CN202201737U (en) | 2011-09-22 | 2011-09-22 | Sodium ion exchange full-automatic controller |
Country Status (1)
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CN (1) | CN202201737U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103043820A (en) * | 2012-12-27 | 2013-04-17 | 攀钢集团攀枝花钢钒有限公司 | Method for controlling chemical water treatment process of boiler |
-
2011
- 2011-09-22 CN CN2011203559264U patent/CN202201737U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103043820A (en) * | 2012-12-27 | 2013-04-17 | 攀钢集团攀枝花钢钒有限公司 | Method for controlling chemical water treatment process of boiler |
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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: 20120425 Termination date: 20180922 |
|
CF01 | Termination of patent right due to non-payment of annual fee |