CN207002332U - A kind of ion exchange water processor for flower cultivation - Google Patents
A kind of ion exchange water processor for flower cultivation Download PDFInfo
- Publication number
- CN207002332U CN207002332U CN201720802046.4U CN201720802046U CN207002332U CN 207002332 U CN207002332 U CN 207002332U CN 201720802046 U CN201720802046 U CN 201720802046U CN 207002332 U CN207002332 U CN 207002332U
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- water
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- exchanger
- raw water
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Abstract
The utility model discloses a kind of ion exchange water processor for flower cultivation, including raw water pump and ion exchange booster pump, the raw water flow meter, the pre-filtrating equipment, the ion-exchanger, the de-ionized water flow rate meter that is connected on ion-exchanger that are connected with pre-filtrating equipment that are connected with ion exchange booster pump that are connected with raw water pump being connected respectively with raw water；It is provided with raw water regulating valve between raw water pump and raw water flow meter, the raw water in raw water pump is discharged by raw water flow meter；Ion exchange booster pump is connected with pre-filtrating equipment, deionized water regulating valve, water intaking valve are connected between pre-filtrating equipment and ion-exchanger, cationic ion-exchange resin is provided with ion-exchanger, deionized water is through producing water valve, the discharge of de-ionized water flow rate meter after ion-exchanger processing.Calcium, magnesium ion salt content without reduce raw water of the utility model in water removal is gone, while pH value is changed into acid from alkalescence, easy to use, high treating effect.
Description
Technical field
A kind of ion exchange water processor for flower cultivation is the utility model is related to, belongs to ion exchange water treatment
Technical applications.
Background technology
In recent years because the needs beautified the environment, flower cultivation turn into new industry.Northern area is largely introduced cultivation and permitted
Originate in southern flower plants and nursery stock more, but due to the difference of southern and northern water quality, cause flower plants and nursery stock yellow leaf occur, fall leaf phenomenon.
Calcium, magnesium ion content are higher in northern area underground water, and pH value is alkalescence, and southern most area underground water
Middle calcium, magnesium ion content are relatively low, and pH value is acidity, thus cultivated in the north southern flowers be critical that calcium in water, magnesium from
Sub- content reduces, and pH value is changed into acid from alkalescence.
Existing flower cultivation method for treating water is that calcium, the magnesium ion in water are removed with reverse osmosis membrane, while produces water by alkali
Property be changed into acid, be that reverse osmosis membrane is also stripped of other ions such as sulphur while calcium, magnesium ion is removed the shortcomings that this method
Hydrochlorate, heavy carbonate etc., cause total salinity in production water and decline, eliminate many necessary elements needed for plant growth.Make
With such flower cultivation water, it is necessary to which flowers normal growth could be maintained by adding substantial amounts of nutriment.
The content of the invention
In view of the above-mentioned problems of the prior art, the utility model provides a kind of ion exchange water for flower cultivation
Processing unit, the salt content of calcium, magnesium ion without reducing raw water in water is can remove, while pH value is changed into acid from alkalescence,
Effectively meet flower growth demand.
To achieve these goals, a kind of ion exchange water treatment for flower cultivation that the utility model uses fills
Put, including raw water pump and ion exchange booster pump, the raw water flow meter and ion that are connected with raw water pump being connected respectively with raw water
Exchange the connected pre-filtrating equipment of booster pump, the ion-exchanger being connected with pre-filtrating equipment and be connected on ion-exchanger
De-ionized water flow rate meter；
It is provided with raw water regulating valve between raw water pump and the raw water flow meter, the raw water in raw water pump is arranged by raw water flow meter
Go out；
The ion exchange booster pump is connected with pre-filtrating equipment, and deionization is connected between pre-filtrating equipment and ion-exchanger
Water regulating valve, water intaking valve, the ion-exchanger is interior to be provided with cationic ion-exchange resin, and deionized water passes through after ion-exchanger processing
Produce water valve, the discharge of de-ionized water flow rate meter.
As an improvement, also including regeneration liquid case, regeneration liquid case is connected by regeneration pump, acid inlet valve with ion-exchanger；
The tank body top connection of the water intaking valve and ion-exchanger, the tank body bottom of exchanger are connected with production water valve.
As an improvement, the acid inlet valve is connected on the pipeline between deionized water regulating valve and water intaking valve；
Backwash water intaking valve is further connected between the deionized water regulating valve and water intaking valve, the another of backwash water intaking valve terminates at tank
Between body bottom and production water valve, positive wash-off water valve is connected on the pipeline between the backwash water intaking valve and production water valve, just washes out water valve
The other end be in communication with the outside, be connected to backwash outlet valve on the pipeline between water intaking valve and the tank body top, backwash outlet valve with
External world's connection.
As an improvement, the regenerated liquid box installed has the hydrochloric acid solution that concentration is 4%.
As an improvement, it is connected to air bleeding valve at the top of the ion-exchanger.
As an improvement, the bottom of the ion-exchanger is connected to blowoff valve.
Relative to existing reverse osmosis membrane technology, the utility model does not reduce raw water while deliming, magnesium ion is gone
Salt content, while pH value is changed into acid from alkalescence, easy to use, high treating effect.This method is than hyperfiltration operating pressure
Low, processing water is big, and water use efficiency is high, energy saving in running significant effect.
Brief description of the drawings
Fig. 1 is principle schematic diagram of the present utility model；
In figure：1st, raw water pump, 2, raw water regulating valve, 3, raw water flow meter, 4, ion exchange booster pump, 5, pre-filtering dress
Put, 6, deionized water regulating valve, 7, ion-exchanger, 8, de-ionized water flow rate meter, 9, regeneration liquid case, 10, regeneration pump, 11, enter
Water valve, 12, just wash out water valve, 13, backwash water intaking valve, 14, backwash outlet valve, 15, production water valve, 16, air bleeding valve, 17, blowoff valve,
18th, acid inlet valve.
Embodiment
To make the purpose of this utility model, technical scheme and advantage of greater clarity, below by drawings and Examples,
The utility model is further elaborated.However, it should be understood that specific embodiment described herein is only solving
The utility model is released, is not limited to the scope of the utility model.
As shown in figure 1, a kind of ion exchange water processor for flower cultivation, including the original being connected respectively with raw water
Water pump 1 and ion exchange booster pump 4, the raw water flow meter 3 being connected with raw water pump 1, the pre- mistake being connected with ion exchange booster pump 4
Filter device 5, the ion-exchanger 7 being connected with pre-filtrating equipment 5 and the de-ionized water flow rate meter being connected on ion-exchanger 7
8；
It is provided with raw water regulating valve 2 between the raw water pump 1 and raw water flow meter 3, the raw water in raw water pump 1 passes through raw water flow
The discharge of meter 3；
The ion exchange booster pump 4 is connected with pre-filtrating equipment 5, is connected between pre-filtrating equipment 5 and ion-exchanger 7
Ion water regulating valve 6, water intaking valve 11, the ion-exchanger 7 is interior to be provided with cationic ion-exchange resin, after the processing of ion-exchanger 7
Deionized water is through producing water valve 15, de-ionized water flow rate meter 8 is discharged.Raw water pump 1 is in parallel with ion exchange booster pump 4, using regulation
The ratio of raw water and deionized water carrys out water production control water quality.
As the improvement of embodiment, in addition to regeneration liquid case 9, regeneration liquid case 9 passes through regeneration pump 10, acid inlet valve 18 and ion
Exchanger 7 is connected；The water intaking valve 11 is connected with the tank body top of ion-exchanger 7, tank body bottom and the production water valve of exchanger
15 are connected.When equipment produces water, water intaking valve 11 and production water valve 15 are opened, tank body top import of the water by water intaking valve 11 from exchanger
Into export out from tank base by the filtering of exchanger resin filtering layer out turns into product water through producing water valve 15 again.
As the improvement of embodiment, the acid inlet valve 18 is connected on the pipeline between deionized water regulating valve 6 and water intaking valve 11；
Be further connected with backwash water intaking valve 13 between the deionized water regulating valve 6 and water intaking valve 11, backwash water intaking valve 13 it is another
Terminate between tank body bottom and production water valve 15, positive wash-off water is connected on the pipeline between the backwash water intaking valve 13 and production water valve 15
Valve 12, the positive other end for washing out water valve 12 are in communication with the outside, and backwash is connected on the pipeline between the water intaking valve 11 and tank body top
Outlet valve 14, backwash outlet valve 14 are in communication with the outside.Water intaking valve 11 and production water valve 15 are opened during equipment normal operation.Equipment is rinsed
When be divided into recoil and square impact, backwash water intaking valve 13 is opened with backwash outlet valve 14 during recoil, the directly outer row of water outlet；Intake during square impact
Valve 11 and the positive water valve 12 that washes out are opened, and water outlet is directly outer to be arranged, and each valve is not opened simultaneously.
As the improvement of embodiment, the regeneration liquid case 9 is equipped with the hydrochloric acid solution that concentration is 4%.
As the improvement of embodiment, the top of the ion-exchanger 7 is connected to air bleeding valve 16, when exchanger tank body pressure compared with
When big, air bleeding valve 16 carries out pressure release exhaust.
As the improvement of embodiment, the bottom of the ion-exchanger 7 is connected to blowoff valve 17, for discharging exchanger tank body
Interior sludge.
Using the method for the utility model production deionized water：
Because cation exchange hydrotreater produces water pH in 2-4, so certain proportion need to be mixed as flower cultivation water
Raw water.Raw water is calculated according to raw water quality first and ion-exchanger produces the mixed proportion of water, according to this proportion adjustment
Raw water regulating valve 2 and deionized water regulating valve 6, the flow-rate ratio for making raw water flow meter 3 and de-ionized water flow rate meter 8 is design load,
So that mixed production water pH is between 5-6.5.Then deionized water regulating valve 6, water intaking valve 11, production water valve 15, water are opened
Entered by water intaking valve 11 from the import on the tank body top of exchanger, filtered by exchanger resin filtering layer from pot bottom and export out
Out turn into product water through producing water valve 15 again；Open raw water pump 1 and ion exchange booster pump 4, raw water can pass through original all the way
Water pump 1 is pressurized, raw water regulating valve 2, raw water flow meter 3 are discharged, and another way is pressurized, through pre-filtering by ion exchange booster pump 4
Enter after the processing of device 5 in ion-exchanger 7, the deionized water after the processing of ion-exchanger 7 and the raw water of first via discharge are converged
Output is qualified after conjunction uses water.
Renovation process after ion exchange water processor ion exchange resin failure of the present utility model：
Ion exchange resin is after prolonged work in the utility model ion exchange water treatment device, because its chemistry is handed over
It is limited to change capacity, so ion exchange resin will fail.To recover its exchange capacity, it is necessary to use regeneration of hydrochloric acid.Regeneration
Method is the hydrochloric acid solution that elder generation prepares 4% in liquid case 9 is regenerated, and first closes all valves, then opens deionized water regulating valve
6th, backwash water intaking valve 13, backwash outlet valve 14, ion exchange booster pump 4 is started, raw water flows through deionized water regulating valve 6, passes through
Backwash water intaking valve 13 enters from tank base, after ion exchange resin punching is loosened, then through the outflow of exchanger tank body top, flows through
Discharged after backwash outlet valve 14, now turn off all valves and start acid regeneration.During acid regeneration, acid inlet valve 18, water intaking valve are opened
11st, blowoff valve 17, regeneration pump 10 is started, regulation acid inlet valve 18 makes hydrochloric acid solution slowly flow across ion-exchanger in 15 minutes,
Regeneration pump 10, acid inlet valve 18, blowoff valve 17 are closed after 15 minutes, starts ion exchange booster pump 4, opens deionized water regulating valve
6th, water valve 12 is just washed out, raw water enters at the top of the tank body of exchanger through deionized water regulating valve 6, water intaking valve 11, and big yield rinses
After ion exchange resin, discharged from the tank base outflow of exchanger through the positive water valve 12 that washes out, until water outlet pH value is 2.Regeneration
Ion exchange water treatment device can be put back into afterwards.
The utility model does not reduce the salt content of raw water while deliming, magnesium ion is gone, while pH value is become by alkalescence
It is easy to use for acidity, high treating effect.This method is lower than hyperfiltration operating pressure, and processing water is big, and water use efficiency is high,
Energy saving in running significant effect.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Any modification, equivalent substitution or improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (6)
1. a kind of ion exchange water processor for flower cultivation, it is characterised in that including the original being connected respectively with raw water
Water pump（1）With ion exchange booster pump（4）With raw water pump（1）Connected raw water flow meter（3）And ion exchange booster pump（4）
Connected pre-filtrating equipment（5）With pre-filtrating equipment（5）Connected ion-exchanger（7）And it is connected to ion-exchanger（7）
On de-ionized water flow rate meter（8）；
The raw water pump（1）With raw water flow meter（3）Between be provided with raw water regulating valve（2）, raw water pump（1）In raw water pass through raw water
Flowmeter（3）Discharge；
The ion exchange booster pump（4）With pre-filtrating equipment（5）Connection, pre-filtrating equipment（5）With ion-exchanger（7）Indirectly
There is deionized water regulating valve（6）, water intaking valve（11）, the ion-exchanger（7）It is interior to be provided with cationic ion-exchange resin, ion exchange
Device（7）Deionized water is through producing water valve after processing（15）, de-ionized water flow rate meter（8）Discharge.
2. a kind of ion exchange water processor for flower cultivation according to claim 1, it is characterised in that also wrap
Include regeneration liquid case（9）, regenerate liquid case（9）Pass through regeneration pump（10）, acid inlet valve（18）With ion-exchanger（7）It is connected；
The water intaking valve（11）With ion-exchanger（7）The connection of tank body top, the tank body bottom of exchanger and production water valve（15）
It is connected.
3. a kind of ion exchange water processor for flower cultivation according to claim 2, it is characterised in that described
Acid inlet valve（18）It is connected on deionized water regulating valve（6）With water intaking valve（11）Between pipeline on；
The deionized water regulating valve（6）With water intaking valve（11）Between be further connected with backwash water intaking valve（13）, backwash water intaking valve（13）'s
It is another to terminate at tank body bottom and production water valve（15）Between, the backwash water intaking valve（13）With producing water valve（15）Between pipeline on connect
There is positive wash-off water valve（12）, just wash out water valve（12）The other end be in communication with the outside, the water intaking valve（11）Between tank body top
Pipeline on be connected to backwash outlet valve（14）, backwash outlet valve（14）It is in communication with the outside.
4. a kind of ion exchange water processor for flower cultivation according to claim 2, it is characterised in that described
Regenerate liquid case（9）Equipped with the hydrochloric acid solution that concentration is 4%.
A kind of 5. ion exchange water processor for flower cultivation according to claim 1 or 2, it is characterised in that
The ion-exchanger（7）Top be connected to air bleeding valve（16）.
A kind of 6. ion exchange water processor for flower cultivation according to claim 1 or 2, it is characterised in that
The ion-exchanger（7）Bottom be connected to blowoff valve（17）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720802046.4U CN207002332U (en) | 2017-07-05 | 2017-07-05 | A kind of ion exchange water processor for flower cultivation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720802046.4U CN207002332U (en) | 2017-07-05 | 2017-07-05 | A kind of ion exchange water processor for flower cultivation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207002332U true CN207002332U (en) | 2018-02-13 |
Family
ID=61452270
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720802046.4U Expired - Fee Related CN207002332U (en) | 2017-07-05 | 2017-07-05 | A kind of ion exchange water processor for flower cultivation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207002332U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111704204A (en) * | 2020-06-23 | 2020-09-25 | 广州拓普特轻工机械有限公司 | Water purification system for removing bromate and water purification method thereof |
-
2017
- 2017-07-05 CN CN201720802046.4U patent/CN207002332U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111704204A (en) * | 2020-06-23 | 2020-09-25 | 广州拓普特轻工机械有限公司 | Water purification system for removing bromate and water purification method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180213 Termination date: 20200705 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |