CN2069411U - Soft water treatment device with saline liquid jetting device - Google Patents
Soft water treatment device with saline liquid jetting device Download PDFInfo
- Publication number
- CN2069411U CN2069411U CN89220097U CN89220097U CN2069411U CN 2069411 U CN2069411 U CN 2069411U CN 89220097 U CN89220097 U CN 89220097U CN 89220097 U CN89220097 U CN 89220097U CN 2069411 U CN2069411 U CN 2069411U
- Authority
- CN
- China
- Prior art keywords
- saline solution
- saline liquid
- soft water
- water treatment
- tower
- 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.)
- Withdrawn
Links
Images
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model provides a soft water treatment device with a saline liquid jetting device, which is characterized in that the soft water treatment device with a saline liquid jetting device adopts a saline liquid jetting device to send saline liquid continuously to a regeneration tower and cancels the arrangement type of a traditional high saline liquid box and a low saline liquid pool and the process that the dissolving salt is carried out by special people and the saline liquid is periodically pumped to the high saline liquid box. The utility model has the advantages of compact structure, small occupation land, simple operation, convenient management, entire assembly, reliable operation, continuous water output, good and stable water quality, etc. Thus, a new soft water treatment device which can match with a boiler for the entire machine output is provided.
Description
The utility model belongs to a kind of and makes the ion-exchange water treatment device of regenerator through improved with sodium-chlor (salt), can be widely used in hard water is softened the industry of handling.
In the existing water softening plant, in making oiler feed reach the technological standard of regulation, its main method is to exchange with the ion in ion exchange resin and the former water; With salt is the saturated resin regeneration that regenerator makes inefficacy.Sell the three tower thermopnore water treating equipment (872111160 patented products that Patent Office of the People's Republic of China has been authorized) of development newly as market, it has than obvious superiority than fixed bed, pulldown bed, moving-bed, does not need periodically to stop bed regeneration, cleaning, also comparatively reasonable on technology than double tower thermopnore.As everyone knows, its device comprises that jointly softening tower, resin regeneration tower, resin cleaning tower, resin circulation and saline solution carry five parts: undertaken after soft water handles by the softening tower of interior dress ion exchange resin, the resin that lost efficacy is regenerated through regenerator column, reuse through cleaning after again, and carries several parts compositions such as saline solution to regenerator column.Prior art is that solid salt and water are added low level dissolved salt pond, utilizes the dissolving that circulates of salt liquid pump, to saline solution saturated after, pump is to the high-order salt case that is disposed at high-rise position again, oneself flows into regenerator column then.When being dissolved salt, its weak point to have the special messenger to operate, periodically with pump the saturated saline solution in low level dissolved salt pond is delivered to high-order salt case, its equipment configuration discrepancy in elevation is big, and floor space is bigger, and used valve, pipeline more, can not satisfy requirement with the outlet of the supporting water softening plant complete machine of boiler.
The purpose of this utility model is to cancel the low level salt pond and the high-order salt case of existing soft water treatment unit, reaches the effect that simplifies the operation, makes things convenient for management, overall package, increases water quality.
The purpose of this utility model is achieved in that dissolved salt top of tower spray soft water, behind one section salt deposit in the dissolved salt tower, enter the saline solution inlet of saline solution ejector and the salt flowage of negative pressure chamber through saline solution variable valve, saline solution under meter under the screen cloth at the bottom of the tower, with enter the jet inlet of saline solution ejector and the soft water of jet chamber from soft water force (forcing) pump, saline solution fluid valve and sneak at mixing section, enter the regenerator column bottom from mixture export, thereby can continuously finish the preparation and the course of conveying of saline solution.
The utility model is compared with other thermopnore water treatment device, and following advantage is arranged:
1. compact construction, floor space is little.For example 2 tons/time occupation area of equipment 1.2m only
2,, use so be particularly suitable for the user that the workshop area is less, factory building is not high owing to do not need to dispose low level salt pond and high-order salt liquid box.
2. continuous effluent, water quality is good and stable.The residual harness of handling back water quality reaches below the 0.015mg-N/l.
3. simplify the operation convenient management.This equipment added salt continuously-running five days, and other thermopnores generally from saline solution of low level salt liquid pool pump high-order salt liquid box can only move 12 hours.
4. overall package, reliable operation, easy for installation.Thereby provide soft water treatment unit with the outlet of boiler integrated equipment.
Concrete principle of work of the present utility model, technical process and main technical details are further described by following embodiment and accompanying drawing.
Fig. 1: the process flow sheet of this device
Wherein: 1, former water regulating valve
2, raw water flow meter
3, softening tower
4, regenerating resin reverse flow valve
5, regenerator column rinse water under meter
6, soft water force (forcing) pump
7, regeneration rinse water variable valve
8, regenerator column
9, clean the resin reverse flow valve
10, rinse water variable valve
11, rinse water under meter
12, new green resin delivery valve
13, resin fluid valve
14, saline solution fluid valve
15, resin ejector
16, saline solution ejector
17, cleaning tower
18, saline solution under meter
19, dissolved salt tower
20, saline solution variable valve
21, dissolved salt tower cleaning valve
22, dissolved salt tower feedwater valve
23, tensimeter
Fig. 2, saline solution ejector sectional view
The utility model technical process is divided into: softening flow process, regeneration flow process, cleaning process, resin circulation process, saline solution are carried flow process five major parts:
1. softening flow process: former water footpath former water regulating valve (1) and raw water flow meter (2) enter bottom the softening tower (3), soften displacement with sodium ionomer resin in the tower.Make water softening, soft water flows out through cat head again.
2. regeneration flow process: regenerator (saline solution) was entered by regenerator column (8) end.With the displacement of regenerating of exhausted resin in the tower.The regenerator waste liquid is discharged by regenerator column (8) top.
3. cleaning process: rinse water is cleaned resin in the tower in rinse water under meter (11) enters cleaning tower (17), and the waste liquid after the cleaning is discharged by cat head.
4. resin circulation process, the exhausted resin at softening tower (3) end are under differential pressure action, flow into regenerator column (8) through regenerating resin reverse flow valve (4), through after the regeneration again under differential pressure action, flow into through cleaning resin reverse flow valve (9) that cleaning tower (17) resin cleans up after new green resin delivery valve (12) enters resin ejector (15).And, resin penetrated deliver to softening tower (3) top at soft water force (forcing) pump (6) output pressure reactive force.Like this, resin just constantly recycles.
5. saline solution is carried flow process: solid salt adds in the dissolved salt tower (19), soft water makes the salt dissolving in dissolved salt tower feedwater valve (22) enters dissolved salt tower (19), the saturated saline solution of gained enters the saline solution input aperture (24) of saline solution ejector (16) when A increases through saline solution variable valve (20) and saline solution under meter (18), pressurization soft water enters jet inlet (26) the B end of saline solution ejector (16) through saline solution fluid valve (14), enter jet chamber (27) again, in negative pressure chamber (25), produce negative pressure, saline solution be sucked into mix in the mixing section (28) after, flow out to regenerator column (8) by mixture export (29) D end and make regenerator and use.
Above-mentioned saline solution ejector (16) in use, when A end during for the saline solution input aperture, promptly its corresponding C end plug is lived (can be used as Butterworth Hatch uses): on the contrary when using C end input saline solution, the A end should clog (also can be used as Butterworth Hatch uses).
In the above-mentioned dissolved salt tower (19) solid salt that accounts for tower height degree 70-85% is housed.The salt grain is soaked in the soft water in the dissolved salt tower (19), and cat head sprays adding soft water continuously.Saturated saline solution is from the screen cloth output continuously down at dissolved salt tower (19) end.
Ejector is originally as known technology, its scantlings of the structure can be selected by handbook and test: when being used for the saline solution course of conveying of soft water processing, key is the required regenerator of regenerator column without interruption (saline solution), the results showed, the ratio of the sectional area of the sectional area (28) of saline solution ejector mixing section and jet chamber (27) is controlled between 3.5 to 2.7, all can meet the demands, wherein Zui Jia sectional area ratio is 3: 1.
The volume of saline solution ejector (16) is very little, owing to require the precision of processing higher, other materials need and can process, and are good but can adopt transparent synthetic glass processing and manufacturing.
The main technical details of this equipment:
Softening tower flow velocity: 25m/h
Former water highest hardness :≤5mg-N/l
Residual harness: 0-0.015mg-N/l
Salt loss-rate: 80g/gN
Ion exchange resin: 732#
Claims (3)
1. thermopnore water treatment device, particularly a kind of soft water treatment unit with the saline solution ejector, by several being grouped into such as softening tower (3), regenerator column (8), the circulation of cleaning tower (17) resin and saline solution conveyings, it is characterized in that the saline solution conveying finishes by dissolved salt tower (19), variable valve (20) and soft water force (forcing) pump (6).
2. device according to claim 1 is characterized in that mixing section (28) sectional area of saline solution ejector (16) and the ratio of jet chamber (27) sectional area should be controlled between 3.5 to 2.7, and its best sectional area ratio is 3: 1.
3. device according to claim 1 is characterized in that saline solution ejector (16) is advisable to adopt transparent synthetic glass processing and manufacturing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN89220097U CN2069411U (en) | 1989-11-21 | 1989-11-21 | Soft water treatment device with saline liquid jetting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN89220097U CN2069411U (en) | 1989-11-21 | 1989-11-21 | Soft water treatment device with saline liquid jetting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2069411U true CN2069411U (en) | 1991-01-16 |
Family
ID=4874837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN89220097U Withdrawn CN2069411U (en) | 1989-11-21 | 1989-11-21 | Soft water treatment device with saline liquid jetting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2069411U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019205523A1 (en) * | 2018-04-28 | 2019-10-31 | 芜湖美的厨卫电器制造有限公司 | Ejector of water softener valve, water softener valve, and water softener |
| CN112723477A (en) * | 2020-12-25 | 2021-04-30 | 珠海格力电器股份有限公司 | Diversion structure, soft water system and regeneration method |
-
1989
- 1989-11-21 CN CN89220097U patent/CN2069411U/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019205523A1 (en) * | 2018-04-28 | 2019-10-31 | 芜湖美的厨卫电器制造有限公司 | Ejector of water softener valve, water softener valve, and water softener |
| US10767777B2 (en) | 2018-04-28 | 2020-09-08 | Wuhu Midea Kitchen And Bath Appliances Mfg. Co., Ltd. | Ejector of a water softener valve and water softener valve |
| CN112723477A (en) * | 2020-12-25 | 2021-04-30 | 珠海格力电器股份有限公司 | Diversion structure, soft water system and regeneration method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1994904A (en) | Sea water nanofiltration desalination method and device | |
| CN214167701U (en) | High-efficient MBR biological treatment system of landfill leachate | |
| CN109665593A (en) | Ion exchange resin adsorbs the Processes and apparatus that DTRO produces water ammonia nitrogen | |
| CN113735294A (en) | Silt processor for river sewage treatment | |
| CN2069411U (en) | Soft water treatment device with saline liquid jetting device | |
| CN201125201Y (en) | Combined type intermediate water treating eqiupment | |
| CN205953611U (en) | Can interior electrolytic reaction jar of abluent fixed bed of double -phase cross -flow | |
| CN116785799A (en) | Waste acid recovery treatment process for lead-acid storage battery | |
| CN107746154A (en) | One kind printing and dyeing（Containing antimony）Sewage disposal system | |
| CN104056554B (en) | A kind of MBR on-line cleaning method | |
| CN214244029U (en) | Water quality treatment system for surface water recharging | |
| CN212821372U (en) | Cleaning device for constructed wetland filler | |
| CN1216812C (en) | Advanced treatment method for urban middle water as industrial recirculated cooling water | |
| CN209651941U (en) | A kind of system that ion exchange resin absorption DTRO produces water ammonia nitrogen | |
| CN208302795U (en) | A kind of flat bed as ion-exchange unit | |
| RU2817630C1 (en) | Resource-saving ionite water treatment plant | |
| CN1070168A (en) | Heavy metal containing wastewater treatment reuse method and device | |
| CN218968960U (en) | Industrial sewage treatment device | |
| CN109954299A (en) | It is a kind of efficiently to mention device for mark | |
| CN213112687U (en) | Landfill leachate aerobic tank fire fighting equipment | |
| CN209307083U (en) | A kind of high COD chemical wastewater treatment settling tank of high salt | |
| CN220283857U (en) | Industrial strong brine treatment equipment | |
| CN2223138Y (en) | Solid-liquid phase physico-chemical self-controling reactor | |
| CN220703477U (en) | Mine water treatment device for underground coal mine | |
| CN214829519U (en) | Leading filter equipment of plant odor treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |