CN204873941U - Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system - Google Patents
Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system Download PDFInfo
- Publication number
- CN204873941U CN204873941U CN201520494487.3U CN201520494487U CN204873941U CN 204873941 U CN204873941 U CN 204873941U CN 201520494487 U CN201520494487 U CN 201520494487U CN 204873941 U CN204873941 U CN 204873941U
- Authority
- CN
- China
- Prior art keywords
- diaphragm valve
- water
- pipeline
- resin container
- water treatment
- 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.)
- Active
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system, including first to the 5th diaphragm valve, a first diaphragm valve port be connected with resin tank deck mouth and another port in proper order through the fourth diaphragm valve, the sprayer is connected with resin tank bottoms mouth, pipe connection between the first and fourth diaphragm valve has the inlet tube, pipeline between sprayer and the resin tank bottoms mouth is through second diaphragm valve and play water piping connection, pipeline between first diaphragm valve and the resin tank deck mouth is through third diaphragm valve and sewage pipe connection, pipeline between sprayer and the resin tank bottoms mouth is through the 5th diaphragm valve and sewage pipe connection. The utility model discloses the full room bed counter current regeneration demineralized water treatment process who realizes has avoided protective layer, operational layer, the inefficacy layer of sodium type ion resin to take place indiscriminate layer, and regeneration effect is good, the demineralized water high quality, and salt consumes for a short time, and secondary pollution is minimum.
Description
Technical field
The utility model relates to a kind of many valves for full chamber bed counter-current regeneration soften water treatment process and controls water treatment system, belongs to water treatment field.
Background technology
Nowadays, softening water treatment facility is applied by popularity in every profession and trades such as industrial and mining enterprises, Urban water supply, field irrigation, pharmacy, boiler, air conditioning and heatings.Mainly contain co-current regeneration technique and this two large soften water treatment process of counter-current regeneration technique on the market at present.
Although traditional co-current regeneration technique has the simple feature of device structure, but it can produce a large amount of waste water in regenerative process, and regenerator---the utilization ratio of salt is not high, salt consumption is very large, therefore, the result not making full use of salt makes salt discharge with waste water, causes serious secondary pollution to environment.
Traditional counter-current regeneration technique needs top to press in regenerative process, and (air pressure or hydraulic pressure) prevents the protective layer of resin in resin container, working lining, random layer occurs inefficacy layer; this just makes the device structure of counter-current regeneration technique become complicated; not easily realize Automated condtrol, cannot big area popularity.
Utility model content
The purpose of this utility model is to provide the many valves of a kind of full chamber bed counter-current regeneration soften water treatment process to control water treatment system; this many valve controls that full chamber bed counter-current regeneration soften water treatment process that water treatment system realizes avoids the protective layer of sodium form ion exchange resin, random layer phenomenon occurs for working lining, inefficacy layer; sodium form ion exchange resin favorable regeneration effect; softening water quality is high; salt consumption is little, substantially reduces secondary pollution.
To achieve these goals, the utility model have employed following technical scheme:
A kind of many valves control water treatment system, it is characterized in that: it comprises the first to the 5th diaphragm valve, one water transport port of the first diaphragm valve is connected with the top mouth of the resin container being filled with the sodium form ion exchange resin accounting for resin container volume 90% ~ 95%, another water transport port of first diaphragm valve is successively via the 4th diaphragm valve, injector is connected with the end mouth of resin container, the pipeline be connected between first diaphragm valve with the 4th diaphragm valve is connected with water inlet pipe, the suction salt entrance of injector is connected with the delivery port of saturated salt water pot, the pipeline be connected between injector and the end mouth of resin container is connected with rising pipe via the second diaphragm valve, the pipeline be connected between first diaphragm valve and the top mouth of resin container is connected with blow-off pipe via the 3rd diaphragm valve, the pipeline be connected between injector and the end mouth of resin container is connected with blow-off pipe via the 5th diaphragm valve, the control port of the first to the 5th diaphragm valve is connected with the corresponding controling end mouth of pressure source divider respectively, the control signal transmission ends of pressure source divider is connected with the control signal transmission ends of controller.
The utility model has the advantages that:
1, the utility model system achieves full chamber bed counter-current regeneration soften water treatment process by multi-valve control means; avoid the protective layer of sodium form ion exchange resin in regenerative process, random layer phenomenon occurs working lining, inefficacy layer; and take full advantage of regenerator---salt; salt consumption is little; the salt of discharging with waste water is few, substantially reduces the secondary pollution caused environment.
2, the utility model system architecture is simple, and operation understands, without the need to the programdesign of complexity, can realize Automated condtrol, the water yield is adjustable, and maintenance cost is low, is suitable for popularity.
3, the utility model system both can realize large discharge water treatment, can realize low discharge water treatment again.When the water yield requiring to process is different, the diaphragm valve of appropriate size only need be changed.
Accompanying drawing explanation
Fig. 1 is the composition schematic diagram that the many valves of the utility model control water treatment system.
Fig. 2 A is the explanatory view of softening water treatment process.
Fig. 2 B is the explanatory view of sodium form ion exchange resin step for regeneration.
Fig. 2 C is the explanatory view that calcium ions and magnesium ions replaces operation again.
Fig. 2 D is the explanatory view of matting.
Embodiment
As shown in Figure 1, the many valves of the utility model control water treatment system and comprise the first diaphragm valve 10, second diaphragm valve 20, 3rd diaphragm valve 30, 4th diaphragm valve 40, 5th diaphragm valve 50, one water transport port of the first diaphragm valve 10 is connected with the top mouth 71 of the resin container 70 being filled with the sodium form ion exchange resin 110 accounting for resin container 70 volume 90% ~ 95%, another water transport port of first diaphragm valve 10 is successively via the 4th diaphragm valve 40, injector 200 is connected with the end mouth 72 of resin container 70, the pipeline be connected between first diaphragm valve 10 with the 4th diaphragm valve 40 is connected with water inlet pipe 101, namely one end of water inlet pipe 101 and the pipeline that is connected between the first diaphragm valve 10 with the 4th diaphragm valve 40 are connected and the other end is connected with the water outlet of water equipment (not shown), as Fig. 1, the water-in 201 of injector 200 is connected with the 4th diaphragm valve 40 by pipeline, the water outlet 203 of injector 200 is connected with the end mouth 72 of resin container 70 by pipeline, the suction salt entrance 202 of injector 200 is connected by the outlet of flexible pipe with the saturated salt water pot (not shown) being loaded with saturated brine, the pipeline be connected between injector 200 and the end mouth 72 of resin container 70 is connected with rising pipe 102 via the second diaphragm valve 20, namely one end of rising pipe 102 is connected with a water transport port of the second diaphragm valve 20 and the other end is connected with the water inlet of watering equipment (not shown), the pipeline be connected between first diaphragm valve 10 and the top mouth 71 of resin container 70 is connected with blow-off pipe 103 via the 3rd diaphragm valve 30, namely one end of blow-off pipe 103 is connected with a water transport port of the 3rd diaphragm valve 30 and the other end is connected with the entrance of waste removal equipment (not shown), the pipeline be connected between injector 200 and the end mouth 72 of resin container 70 is also connected with blow-off pipe 103 via the 5th diaphragm valve 50, first diaphragm valve 10, second diaphragm valve 20, 3rd diaphragm valve 30, 4th diaphragm valve 40, the control port of the 5th diaphragm valve 50 is connected with the corresponding controling end mouth of pressure source divider 80 via flexible pipe respectively, the control signal transmission ends of pressure source divider 80 and the control signal transmission ends of controller 90 are electrically connected.
In the utility model, the first to the 5th diaphragm valve 10,20,30,40,50 is diaphragm valve, and be the universal valve of standard, it can be pneumatic diaphragm valve or hydraulic diaphragm valve.Connection between corresponding each diaphragm valve, between the top mouth 71 of respective diaphragm valve and resin container 70, end mouth 72 all adopts pipeline to connect and realizes, and the connection between each diaphragm valve and pressure source divider 80 all adopts hose connection realization.The effect of pressure source divider 80 is under the instruction transmitted at controller 90, to the unlatching of each diaphragm valve, closes and controls, and pressure source divider 80 is using water or gas as pressure source.The effect of controller 90 is that control pressure source divider 80 works, to start water technology under the instruction of input.
In the utility model, controller 90, pressure source divider 80, diaphragm valve, injector 200, water equipment, watering equipment, waste removal equipment etc. are existing device, the parts of this area or know technology, therefore its concrete formation does not here describe in detail.In practice, sodium form ion exchange resin 110 is for knowing filtrate, and resin container 70 can be glass fiber reinforced plastic tank, lining moulds carbon steel tank or stainless cylinder of steel.
The flow process controlling the full chamber bed counter-current regeneration soften water treatment process that water treatment system realizes based on the many valves of the utility model is:
1) under a control of the controller 90, pressure source divider 80 controls the first diaphragm valve 10, second diaphragm valve 20 and opens, all the other diaphragm valves are closed, as shown in Figure 2 A, the former water that water equipment exports enters from water inlet pipe 101, after the first diaphragm valve 10, enter the top mouth 71 of resin container 70, in resin container 70, pass through sodium form ion exchange resin 110 by the calcium ions and magnesium ions (Ca in former water
2+, Mg
2+) absorption fall after, flow out softening water from the end mouth 72 of resin container 70, softening water exports watering equipment to through the second diaphragm valve 20, rising pipe 102, completes softening water treatment process.
2) after sodium form ion exchange resin 110 absorbing calcium ions and magnesium ions lost efficacy (inefficacy refers to that sodium form ion exchange resin 110 fully cannot adsorb calcium ions and magnesium ions and makes the softening water made not reach industry standard), under a control of the controller 90, pressure source divider 80 controls the 3rd diaphragm valve 30, 4th diaphragm valve 40 is opened, all the other diaphragm valves are closed, as shown in Figure 2 B, the former water exported from water equipment to enter and through the 4th diaphragm valve 40 from water inlet pipe 101, when the water-in 201 of current from injector 200 enters, when flowing through and flow out from water outlet 203 at a high speed, negative pressure is formed in injector 200 inside, so under the effect of ambient pressure, saturated brine in saturated salt water pot is sucked in injector 200 cavity from suction salt entrance 202, thus former water and saturated brine are mixed to form dilution salt solution, dilution salt solution enters the end mouth 72 of resin container 70, the calcium ions and magnesium ions generation replacement(metathesis)reaction on the sodium form ion exchange resin 110 of salt solution and inefficacy is diluted in resin container 70, most of calcium ions and magnesium ions on sodium form ion exchange resin 110 is displaced, push up mouth 71 from resin container 70 and discharge the waste water containing the calcium ions and magnesium ions of replacing, now can be considered that sodium form ion exchange resin 110 has recovered the ability of absorbing calcium ions and magnesium ions and realized regeneration, waste water is through the 3rd diaphragm valve 30, blow-off pipe 103 is expelled to waste removal equipment, complete sodium form ion exchange resin step for regeneration.
3) after sodium form ion exchange resin step for regeneration terminates, under a control of the controller 90, pressure source divider 80 continues control the 3rd diaphragm valve 30, 4th diaphragm valve 40 is opened, all the other diaphragm valves are closed, as shown in Figure 2 C, the former water exported from water equipment to enter and through the 4th diaphragm valve 40 from water inlet pipe 101, but now injector 200 cuts out and inhales salt entrance 202, so former water directly passes through from injector 200 and enters the end mouth 72 of resin container 70, forms with salt remaining in resin container 70 and dilute salt solution and continue the calcium ions and magnesium ions generation replacement(metathesis)reaction with remnants on sodium form ion exchange resin 110, further the calcium ions and magnesium ions on sodium form ion exchange resin 110 is replaced, achieve making full use of of salt, salt consumption is very little, greatly reduce salt and discharge the secondary pollution caused with waste water, push up mouth 71 from resin container 70 to continue to discharge waste water, waste water is through the 3rd diaphragm valve 30, blow-off pipe 103 is expelled to waste removal equipment, complete calcium ions and magnesium ions and replace operation again.
4) after sodium form ion exchange resin 110 recovers industry and traffic ability (industry and traffic ability refers to that sodium form ion exchange resin 110 can carry out the ability of fully absorption to calcium ions and magnesium ions), under a control of the controller 90, pressure source divider 80 controls the first diaphragm valve 10, 5th diaphragm valve 50 is opened, all the other diaphragm valves are closed, as shown in Figure 2 D, the former water exported from water equipment enters from water inlet pipe 101, the top mouth 71 of resin container 70 is entered after the first diaphragm valve 10, residual brine on sodium form ion exchange resin 110 in resin container 70 is cleaned up, waste water (rinse water) is discharged from resin container 70 end mouth 72, waste water is through the 5th diaphragm valve 50, blow-off pipe 103 is expelled to waste removal equipment, complete matting.
5) step 1 is returned).
It should be noted that, in above-mentioned full chamber bed counter-current regeneration soften water treatment process, in resin container 70, the volume of the sodium form ion exchange resin 110 of filling should account for 90% ~ 95% of resin container 70 splendid attire volume.Thus replace again in operation at the above-mentioned sodium form ion exchange resin step for regeneration and calcium ions and magnesium ions that sodium form ion exchange resin 110 are realized to fully regeneration; sodium form ion exchange resin 110 is at flow action float downward; because sodium form ion exchange resin 110 volume accounts for 90% ~ 95% of resin container 70 volume; therefore; sodium form ion exchange resin 110 only and there is very little space between the bottom of resin container 70; the space that sodium form ion exchange resin 110 does not stir up and down, just can avoid the protective layer of sodium form ion exchange resin, working lining thus, random layer phenomenon occurs inefficacy layer.
If the volume ratio of resin container 70 is less than 90% shared by sodium form ion exchange resin 110, then still can there is random layer problem, if the volume ratio of resin container 70 is greater than 95% shared by sodium form ion exchange resin 110, then sodium form ion exchange resin its volumetric expansion after regeneration ending, can cause damage to resin container, and sodium form ion exchange resin volumetric expansion simultaneously extrudes the phenomenon that fragmentation can occur mutually.In reality is implemented, such as, the volume ratio of resin container 70 shared by sodium form ion exchange resin 110 can be set to 90%, 92%, 95% etc.
In reality is implemented, step 2) the dilution salt solution that uses and step 3) in the saltiness of dilution salt solution that formed generally be set between 5% ~ 15%, if be less than 5%, then effectively cannot reach sodium form ion exchange resin regeneration object, if be greater than 15%, then can cause the waste of salt resource to a certain extent, in reality is implemented, the saltiness of such as diluting salt solution can be set to 5%, 10%, 15% etc.
In the utility model, other resin cation (R.C.) available or resin anion(R.A) substitute the sodium form ion exchange resin in resin container, correspondingly use other to substitute dilution salt solution with water (all example hydrochloric acids, sodium hydroxide etc.), thus realize the treatment process such as full chamber bed counter-current regeneration pure water.
The utility model has the advantages that:
1, the utility model system achieves full chamber bed counter-current regeneration soften water treatment process by multi-valve control means; avoid the protective layer of sodium form ion exchange resin in regenerative process, random layer phenomenon occurs working lining, inefficacy layer; and take full advantage of regenerator---salt; salt consumption is little; the salt of discharging with waste water is few, substantially reduces the secondary pollution caused environment.
2, the utility model system architecture is simple, and operation understands, without the need to the programdesign of complexity, can realize Automated condtrol, the water yield is adjustable, and maintenance cost is low, is suitable for popularity.
3, the utility model system both can realize large discharge water treatment, can realize low discharge water treatment again.When the water yield requiring to process is different, the diaphragm valve of appropriate size only need be changed.
The know-why being more than preferred embodiment of the present utility model and using; for a person skilled in the art; when not deviating from spirit and scope of the present utility model; any based on apparent changes such as the equivalent transformation on technical solutions of the utility model basis, simple replacements, all belong within the utility model protection domain.
Claims (2)
1. the many valves of full chamber bed counter-current regeneration soften water treatment process control water treatment system, it is characterized in that: it comprises the first to the 5th diaphragm valve, one water transport port of the first diaphragm valve is connected with the top mouth of the resin container being filled with the sodium form ion exchange resin accounting for resin container volume 90% ~ 95%, another water transport port of first diaphragm valve is successively via the 4th diaphragm valve, injector is connected with the end mouth of resin container, the pipeline be connected between first diaphragm valve with the 4th diaphragm valve is connected with water inlet pipe, the suction salt entrance of injector is connected with the delivery port of saturated salt water pot, the pipeline be connected between injector and the end mouth of resin container is connected with rising pipe via the second diaphragm valve, the pipeline be connected between first diaphragm valve and the top mouth of resin container is connected with blow-off pipe via the 3rd diaphragm valve, the pipeline be connected between injector and the end mouth of resin container is connected with blow-off pipe via the 5th diaphragm valve, the control port of the first to the 5th diaphragm valve is connected with the corresponding controling end mouth of pressure source divider respectively, the control signal transmission ends of pressure source divider is connected with the control signal transmission ends of controller.
2. many valves as claimed in claim 1 control water treatment system, it is characterized in that:
Described first to the 5th diaphragm valve is pneumatic diaphragm valve or hydraulic diaphragm valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520494487.3U CN204873941U (en) | 2015-07-09 | 2015-07-09 | Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520494487.3U CN204873941U (en) | 2015-07-09 | 2015-07-09 | Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204873941U true CN204873941U (en) | 2015-12-16 |
Family
ID=54818340
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520494487.3U Active CN204873941U (en) | 2015-07-09 | 2015-07-09 | Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204873941U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944522A (en) * | 2015-07-09 | 2015-09-30 | 北京康洁之晨水处理技术有限公司 | Multi-valve control water treatment system and full-chamber bed up-flow regeneration softened water treatment process |
| CN115072832A (en) * | 2021-03-13 | 2022-09-20 | 北京康洁之晨水处理技术有限公司 | Full-chamber bed ion exchange control system and control method |
-
2015
- 2015-07-09 CN CN201520494487.3U patent/CN204873941U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104944522A (en) * | 2015-07-09 | 2015-09-30 | 北京康洁之晨水处理技术有限公司 | Multi-valve control water treatment system and full-chamber bed up-flow regeneration softened water treatment process |
| CN104944522B (en) * | 2015-07-09 | 2017-01-11 | 北京康洁之晨水处理技术有限公司 | Multi-valve control water treatment system and full-chamber bed up-flow regeneration softened water treatment process |
| CN115072832A (en) * | 2021-03-13 | 2022-09-20 | 北京康洁之晨水处理技术有限公司 | Full-chamber bed ion exchange control system and control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104944522A (en) | Multi-valve control water treatment system and full-chamber bed up-flow regeneration softened water treatment process | |
| CN201161191Y (en) | Acid-alkali regenerative agent conserving mix bed regenerating unit | |
| CN207153718U (en) | A kind of strong acid, strong base ion exchange bed program control automatic regenerating unit | |
| CN204873941U (en) | Full room bed counter current regeneration demineralized water treatment process is with many valve controls water processing system | |
| CN204848355U (en) | Demineralized water equipment | |
| CN212655517U (en) | Dual-mode switching operation metallurgical wastewater softening device | |
| CN204897489U (en) | Float bed counter current regeneration demineralized water treatment process with many valve controls water processing system | |
| CN207760087U (en) | Wet method soft water dosing system | |
| CN104944521A (en) | Multi-valve control system and one-work one-standby full-chamber bed up-flow regeneration softened water treatment process | |
| CN207091116U (en) | A kind of full-automatic removal water hardness device | |
| CN204873942U (en) | It be equipped with to expire room bed counter current regeneration demineralized water treatment process and uses many valve control system to use one | |
| CN204625258U (en) | A kind ofly parallel-series can to switch and use and utilize the Di of regenerator | |
| CN104528877B (en) | Water-cooling circulating system | |
| CN204456270U (en) | A kind of workshop pure water water system | |
| CN217756961U (en) | Circulation system is washed to second grade desalination ion exchanger cluster | |
| CN109650620A (en) | A kind of water body restoration device | |
| CN206437905U (en) | A kind of water-softening plant of centrifugal water resource heat pump | |
| CN204447439U (en) | Many valves control water treatment system | |
| CN203976489U (en) | Recirculated water is softening treatment unit continuously | |
| CN204710352U (en) | Macroporous absorbent resin regenerative system | |
| CN206818056U (en) | A kind of denitration heat exchanger rinses optimization device | |
| CN206570062U (en) | The equipment that external cleaning full chamber bed counter-current regeneration softens water treatment technology can be achieved | |
| CN204778944U (en) | Mix bed regenerating unit | |
| CN205199527U (en) | Automatic throw demineralized water processing system who adds sodium chloride solution | |
| CN202754831U (en) | Softened water device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |