CN107285519A - A kind of condensed water precision processing system - Google Patents
A kind of condensed water precision processing system Download PDFInfo
- Publication number
- CN107285519A CN107285519A CN201710613306.8A CN201710613306A CN107285519A CN 107285519 A CN107285519 A CN 107285519A CN 201710613306 A CN201710613306 A CN 201710613306A CN 107285519 A CN107285519 A CN 107285519A
- Authority
- CN
- China
- Prior art keywords
- detection bar
- resin particle
- flow rate
- high flow
- mixed bed
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
- C02F2001/427—Treatment of water, waste water, or sewage by ion-exchange using mixed beds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/023—Water in cooling circuits
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a kind of condensed water precision processing system; including fore filter, high flow rate mixed bed; screen pack is provided with outlet pipe; be provided with the Hui Zhi mechanisms being provided with the testing agency for detecting resin particle accumulating amount, outlet pipe for the resin particle of accumulation being recovered in water inlet pipe in the outlet pipe of screen pack side.The present invention has advantages below and effect：This programme utilizes new mechanical structure, utilize filter screen filtration resin particle, resin particle after accumulation, which is entered in filter bag, to be collected, detection bar can be promoted to rotate after resin particle is accumulated to a certain extent, operating personnel are the rotation that detection bar can be observed through observation window, the resin particle of accumulation is transported in water inlet pipe by returning fat pipe followed by liposuction pump, resin particle and water are together transported in high flow rate mixed bed by water inlet pipe again；Whole process realizes the resin particle for eaily recycling and being gone out from high flow rate mixed bed internal leakage, meets the objective of energy-conserving and environment-protective.
Description
Technical field
The present invention relates to water-treatment technology field, more particularly to a kind of condensed water precision processing system.
Background technology
Ion exchange resin in modern power plants is usually required by fore filter and high flow rate mixed bed.
At present, Publication No. CN203781955U, the day for announcing is that the Chinese patent on the 20th of August in 2014 discloses a kind of steam
Generating set precision processing device of condensation water, including coagulation hydroenergy backwater case, condensate tank and backwash water tank, coagulate water recovery tank and condensation
Also it is connected with back water pump, deironing filter, one-level oil removal filter, two grades of oil removal filters, high flow rate mixed beds between water tank in turn
And resin catcher, condensate tank is connected backwash water tank with condensate pump and radiator successively and is connected with backwash water pump, backwash water
Pump is connected with deironing filter, one-level oil removal filter, two grades of oil removal filters respectively.Deironing filter, one-level oil removing filtering
Device, two grades of oil removal filters, high flow rate mixed beds are connected with compressed air reservoir respectively.High flow rate mixed bed is also stored up with alkali liquor storage tank and acid solution
Tank is connected.
This kind of steam-electric power unit precision processing device of condensation water will be come out using resin catcher from high flow rate mixed bed internal leakage
Resin particle filter out, these filtering after resin will directly rinse away；But if go out from high flow rate mixed bed internal leakage
When the resin particle come is excessive, the resin in high flow rate mixed bed will be reduced more significantly, the resin having influence in high flow rate mixed bed
To the desalination effect of condensate.
The content of the invention
It is an object of the invention to provide a kind of condensed water precision processing system, can eaily it recycle mixed from high speed
The resin particle that bed internal leakage is gone out.
The present invention above-mentioned technical purpose technical scheme is that：A kind of condensate polishing treatment system
It is provided with system, including fore filter, high flow rate mixed bed, the water inlet end of the high flow rate mixed bed for connecting in the prefilter
It is connected with water inlet pipe on device, the water side of the high flow rate mixed bed in outlet pipe, the outlet pipe and is provided with screen pack, it is described
It is provided with the testing agency for detecting resin particle accumulating amount, the outlet pipe and sets in the outlet pipe of screen pack side
Be equipped with the Hui Zhi mechanisms for the resin particle of accumulation being recovered in the water inlet pipe.
By using such scheme, the water after fore filter filtering enters high flow rate mixed bed by water inlet pipe
It is interior, then pass through the water after high flow rate mixed bed desalination and transferred out by outlet pipe, wherein utilizing the filtering being arranged in outlet pipe
Net, the resin particle that screen pack will can come out from high flow rate mixed bed internal leakage, when resin particle is constantly accumulated on screen pack
Afterwards, the accumulating amount of resin particle is detected using testing agency, when detect accumulation it is excessive after, using Hui Zhi mechanisms by the tree of accumulation
Fat particle is recovered in water inlet pipe, and resin particle and water are together transported in high flow rate mixed bed by water inlet pipe again；Whole process is realized
The resin particle gone out from high flow rate mixed bed internal leakage is eaily recycled, the resin in high flow rate mixed bed is effectively ensured to solidifying
The desalination effect born water.
The further setting of the present invention is：The screen pack is in coniform, institute of the opening towards the high flow rate mixed bed side
State the filter bag being fixed with the one end of screen pack away from the high flow rate mixed bed for collecting resin particle.
By using such scheme, work as resin particle towards the coniform of high flow rate mixed bed side in opening using screen pack
After being accumulated on screen pack, resin particle can be pooled to mistake of the screen pack away from high flow rate mixed bed one end with the inwall of screen pack
In filter bag, resin particle can realize accumulation in filter bag, reduce because being influenceed after accumulation of the resin particle on screen pack
The possibility for the speed that current pass through in screen pack.
The further setting of the present invention is：The testing agency includes being rotatably connected on the institute on the upside of the filter bag
State that the detection bar in outlet pipe, one end are fixed in the detection bar and the other end is fixed on the bullet on the inwall of the outlet pipe
Spring, one end of detection bar described in the Spring driving is formed with depressed part after contradicting on the filter bag outer wall, positioned at described
Observation window is provided with the rising pipe side wall of the one end of detection bar away from the filter bag, the resin in the filter bag
When particle packing is excessive, resin particle promotes the detection bar that the detection bar is rotated.
By using such scheme, after the resin particle in filter bag is stacked at the position of depressed part, the tree of accumulation
Fat particle can produce thrust to detection bar one end in depressed part so that detection bar rotates, and operating personnel are through observation
Window is the rotation that detection bar can be observed, and the detection to resin particle accumulating amount can be finally realized by the rotation of detection bar；
After Hui Zhi mechanisms reclaim resin particle, spring promotes detection bar to rotate so that detection bar continues to contradict the shape on filter bag
Be in depression portion.
The further setting of the present invention is：Offered in the detection bar fixed on rotation hole, the inwall of the outlet pipe
Have for the rotating shaft through the rotation hole, between described detection bar one end of the filter bag side and the rotation hole
Distance away from more than described detection bar one end positioned at the observation window side and the rotation hole.
By using such scheme, it is more than using detection bar one end positioned at filter bag side and the spacing of rotation hole and is located at
Detection bar one end of observation window side and the distance of rotation hole, when the resin particle of accumulation promotes detection bar to rotate, profit
With lever principle, detection bar can be more prone to rotate, so that the sensitivity of detection bar is more preferable.
The further setting of the present invention is：The one end of the detection bar away from the filter bag is contradicted in the observation window
On inwall, it is more than positioned at described detection bar one end of the filter bag side with the spacing of the high flow rate mixed bed and is located at the observation
Described detection bar one end of window side and the distance of the high flow rate mixed bed.
By using such scheme, it is more than position using detection bar one end positioned at filter bag side and the spacing of high flow rate mixed bed
Detection bar one end and the distance of high flow rate mixed bed in observation window side, now detection bar is that can be at inclined state, and is tilted
Direction along the direction of current, now detection bar can be more prone to rotate, so that the sensitivity of detection bar is more preferable；Together
When one end away from filter bag of detection bar contradict on the inwall of observation window, now detection bar can not can be inverted.
The further setting of the present invention is：The detection bar is fixed with one end away from the filter bag for contradicting
Noctilucent powder layer is provided with detection block on the observation window, the detection block.
It is often more dim when night time operation by using such scheme, now utilize the luminescent powder in detection block
Layer, noctilucent powder layer can send light at night, can now facilitate operating personnel to see the rotation of detection bar clearly in time in itself, convenient
Operating personnel clear up the resin particle of accumulation in time.
The further setting of the present invention is：The Hui Zhi mechanisms include one end and connected in the filter bag away from the filtering
Net on one end and other end connection returning fat pipe, being connected to the fat pipe that returns close to the outlet pipe side on the water inlet pipe
Cut fat valve, be connected to the liposuction pump returned on fat pipe.
By using such scheme, return on fat pipe and cut fat valve because the water for preventing from entering back in fat pipe is back at a high speed
In mixed bed, as operating personnel it was observed that after detection bar is rotated, opening and cutting a fat valve, resin can be withdrawn into water by starting liposuction pump
In pipe, resin particle is sent in high flow rate mixed bed by water inlet pipe.
The further setting of the present invention is：The Hui Zhi mechanisms also include being located at the high flow rate mixed bed and the screen pack it
Between the outlet pipe on the first valve, on the water inlet pipe between the fore filter and described time fat pipe
Second valve.
By using such scheme, as operating personnel it was observed that after detection bar is rotated, closing the first valve and closing second
Valve, now state of the high flow rate mixed bed in also not water outlet of not intaking, now opens and cuts a fat valve, starting liposuction pump can be by resin
It is withdrawn into water inlet pipe, resin particle is sent in high flow rate mixed bed by water inlet pipe；Now liposuction pump will not be by excessive water
Together it is sent to together with resin particle in water inlet pipe, high flow rate mixed bed need not reprocess excessive water, is conducive to increasing resin
The service life of grain.
In summary, the invention has the advantages that：Come out using filter screen filtration from high flow rate mixed bed internal leakage
Resin particle, the resin particle after accumulation, which is entered in filter bag, to be collected, and is after resin particle is accumulated to a certain extent
Detection bar can be promoted to rotate, operating personnel are the rotation that detection bar can be observed through observation window, followed by liposuction pump by heap
Long-pending resin particle is transported in water inlet pipe by returning fat pipe, and resin particle and water are together transported to high flow rate mixed bed by water inlet pipe again
It is interior；Whole process realizes the resin particle for eaily recycling and being gone out from high flow rate mixed bed internal leakage, is effectively ensured at a high speed
The desalination effect of resin in mixed bed to condensate.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is the enlarged drawing in A portions in Fig. 1, is mainly used in embodying the annexation between screen pack, filter bag, testing agency.
In figure：1st, fore filter；2nd, high flow rate mixed bed；3rd, water inlet pipe；4th, outlet pipe；41st, screen pack；42nd, filter bag；
43rd, observation window；44th, rotating shaft；5th, testing agency；51st, detection bar；511st, rotation hole；512nd, detection block；513rd, noctilucent powder layer；52、
Spring；521st, depressed part；6th, Hui Zhi mechanisms；61st, fat pipe is returned；62nd, fat valve is cut；63rd, liposuction pump；64th, the first valve；65th, second
Valve.
Embodiment
The present invention is described in further detail below in conjunction with accompanying drawing.
A kind of condensed water precision processing system, reference picture 1, this kind of condensed water precision processing system includes fore filter 1 and height
Fast mixed bed 2, this kind of fore filter 1 is introduced from the great emerging Environmental Protection Technology Co., Ltd in Shenzhen；The wherein water inlet of high flow rate mixed bed 2
It is connected with end and for connecting the second valve 65 is installed on the water inlet pipe 3 on fore filter 1, water inlet pipe 3；And it is mixed at a high speed
It is connected with the water side of 2 lower ends of bed on the outlet pipe 4 for water water delivery to be gone out, outlet pipe 4 and first valve 64 is installed.
Reference picture 1, Fig. 2, bolt is passed through in outlet pipe 4 of first valve 64 away from the side of high flow rate mixed bed 2（In figure not
Show）Be fixed with screen pack 41, and screen pack 41 in opening towards the coniform of the side of high flow rate mixed bed 2, wherein screen pack 41 is remote
Pass through bolt on one end from high flow rate mixed bed 2（Not shown in figure）Filter bag 42 is installed with, under being filtered from screen pack 41
The resin particle come, which will be pooled in filter bag 42, to be collected.
Rotating shaft 44, bearing of trend and the filter bag 42 of rotating shaft 44 are welded with the outlet pipe 4 of the upside of filter bag 42
Bearing of trend is perpendicular；Detection bar 51 wherein is connected with rotating shaft 44, is installed on the side wall of outlet pipe 4 of the upper end of detection bar 51
There is observation window 43；The rotation hole 511 passed through for rotating shaft 44 is offered in detection bar 51, and positioned at the detection bar of the side of filter bag 42
51 one end and the spacing of rotation hole 511 are more than one end of detection bar 51 positioned at the side of observation window 43 and the distance of rotation hole 511.
One end of detection bar 51 is contradicted on the outer wall of filter bag 42, and the wherein one end of detection bar 51 away from filter bag 42 is supported
Touch on the inwall of observation window 43, and one end of detection bar 51 positioned at the side of filter bag 42 and the spacing of high flow rate mixed bed 2 are more than position
The one end of detection bar 51 and the distance of high flow rate mixed bed 2 in the side of observation window 43；Simultaneously close to the detection bar 51 of the side of filter bag 42
On be welded with spring 52, the one end of spring 52 away from detection bar 51 is welded on the inwall of outlet pipe 4, spring 52 driving detection bar
51 one end away from observation window 43 contradict on filter bag 42 and are formed with depressed part 521.
Detection bar 51 is welded with detection block 512, detection block 512 on one end away from filter bag 42 and is bonded with noctilucent powder layer
513, and noctilucent powder layer 513 is wrapped in detection block 512 by glass plate, when night operating personnel still can utilize noctilucence
The light that bisque 513 is sent is it was observed that the rotation of detection bar 51.
Be connected with back fat pipe 61 on reference picture 1, outlet pipe 4, return fat pipe 61 one end be passed into outlet pipe 4 inside and with
The one end of filter bag 42 away from screen pack 41 is communicated, and time one end of fat pipe 61 away from outlet pipe 4 is connected to positioned at the second valve
On 65 water inlet pipes 3 away from the side of fore filter 1；Wherein return fat pipe 61 and a section fat valve is installed on the side of outlet pipe 4
62, after the resin particle in filter bag 42 is stacked into back in fat pipe 61, resin particle and water are prevented together using fat valve 62 is cut
Pass back into water inlet pipe 3；Liposuction pump 63, liposuction are installed positioned at section returning on fat pipe 61 between fat valve 62 and water inlet pipe 3 simultaneously
Pump 63 is used to resin particle being withdrawn into water inlet pipe 3.
Principle：Reference picture 1, Fig. 2, the resin particle come out from the internal leakage of high flow rate mixed bed 2 is filtered using screen pack 41, accumulation
Resin particle afterwards is entered to be collected in filter bag 42, and detection bar can be promoted after resin particle is accumulated to a certain extent
51 so that detection pipe rotates；Operating personnel can observe turning for detection bar 51 through observation window 43 by detection block 512
Dynamic, now detection bar 51, spring 52 are the testing agency 5 configurable for detection resin particle accumulating amount；It is then turned off first
Valve 64 and the second valve 65 of closing, now state of the high flow rate mixed bed 2 in also not water outlet of not intaking, now opens and cuts a fat valve
62, resin can be withdrawn into water inlet pipe 3 by starting liposuction pump 63, and resin particle is sent into high flow rate mixed bed 2 by water inlet pipe 3
It is interior, now return fat pipe 61, cut fat valve 62, liposuction pump 63, the first valve 64, the second valve 65 i.e. configurable for by the tree of accumulation
Fat particle is recovered to the Hui Zhi mechanisms 6 in water inlet pipe 3；Whole process is realized and eaily recycled out of high flow rate mixed bed 2
The resin particle let out, meets the principle of energy-conserving and environment-protective.
This specific embodiment is only explanation of the invention, and it is not limitation of the present invention, people in the art
Member can make the modification without creative contribution to the present embodiment as needed after this specification is read, but as long as at this
All protected in the right of invention by Patent Law.
Claims (8)
1. a kind of condensed water precision processing system, including fore filter（1）, high flow rate mixed bed（2）, the high flow rate mixed bed（2）Enter
It is provided with water end (W.E.) for connecting in the fore filter（1）On water inlet pipe（3）, the high flow rate mixed bed（2）Water side
On be connected with outlet pipe（4）, it is characterised in that：The outlet pipe（4）Inside it is provided with screen pack（41）, the screen pack（41）One
The outlet pipe of side（4）Inside it is provided with the testing agency for detecting resin particle accumulating amount（5）, the outlet pipe（4）On
It is provided with for the resin particle of accumulation to be recovered into the water inlet pipe（3）Interior Hui Zhi mechanisms（6）.
2. a kind of condensed water precision processing system according to claim 1, it is characterised in that：The screen pack（41）In opening
Towards the high flow rate mixed bed（2）Coniform, the screen pack of side（41）Away from the high flow rate mixed bed（2）One end on it is fixed
There is the filter bag for collecting resin particle（42）.
3. a kind of condensed water precision processing system according to claim 2, it is characterised in that：The testing agency（5）Including
It is rotatably connected on positioned at the filter bag（42）The outlet pipe of upside（4）Interior detection bar（51）, one end be fixed on it is described
Detection bar（51）Go up and the other end is fixed on the outlet pipe（4）Inwall on spring（52）, the spring（52）Driving institute
State detection bar（51）One end contradict in the filter bag（42）Depressed part is formed with after on outer wall（521）, positioned at the detection
Bar（51）Away from the filter bag（42）One end the outlet pipe（4）Observation window is provided with the wall of side（43）, when the mistake
Filter bag（42）When interior resin particle accumulation is excessive, resin particle promotes the detection bar（51）So that the detection bar（51）Hair
It is raw to rotate.
4. a kind of condensed water precision processing system according to claim 3, it is characterised in that：The detection bar（51）On open up
There is rotation hole（511）, the outlet pipe（4）Inwall on be fixed with for through the rotation hole（511）Rotating shaft（44）, position
In the filter bag（42）The detection bar of side（51）One end and the rotation hole（511）Spacing be more than be located at it is described see
Examine window（43）The detection bar of side（51）One end and the rotation hole（511）Distance.
5. a kind of condensed water precision processing system according to claim 4, it is characterised in that：The detection bar（51）Away from institute
State filter bag（42）One end contradict in the observation window（43）Inwall on, positioned at the filter bag（42）The inspection of side
Measuring staff（51）One end and the high flow rate mixed bed（2）Spacing be more than be located at the observation window（43）The detection bar of side（51）
One end and the high flow rate mixed bed（2）Distance.
6. a kind of condensed water precision processing system according to claim 5, it is characterised in that：The detection bar（51）Away from institute
State filter bag（42）One end on be fixed with for contradict in the observation window（43）On detection block（512）, the detection block
（512）On be provided with noctilucent powder layer（513）.
7. a kind of condensed water precision processing system according to claim 2, it is characterised in that：The Hui Zhi mechanisms（6）Including
One end is connected in the filter bag（42）Away from the screen pack（41）On one end and the other end connection in the water inlet pipe（3）On
Return fat pipe（61）, be connected to and described return fat pipe（61）Close to the outlet pipe（4）Section fat valve of side（62）, be connected to it is described
Return fat pipe（61）On liposuction pump（63）.
8. a kind of condensed water precision processing system according to claim 7, it is characterised in that：The Hui Zhi mechanisms（6）Also wrap
Include positioned at the high flow rate mixed bed（2）With the screen pack（41）Between the outlet pipe（4）On the first valve（64）, be located at
The fore filter（1）With described time fat pipe（61）Between the water inlet pipe（3）On the second valve（65）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710613306.8A CN107285519B (en) | 2017-07-25 | 2017-07-25 | A kind of condensed water precision processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710613306.8A CN107285519B (en) | 2017-07-25 | 2017-07-25 | A kind of condensed water precision processing system |
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| Publication Number | Publication Date |
|---|---|
| CN107285519A true CN107285519A (en) | 2017-10-24 |
| CN107285519B CN107285519B (en) | 2019-11-26 |
Family
ID=60103511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710613306.8A Active CN107285519B (en) | 2017-07-25 | 2017-07-25 | A kind of condensed water precision processing system |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63315189A (en) * | 1988-06-03 | 1988-12-22 | Ebara Infilco Co Ltd | Condensate treatment method |
| CN2172155Y (en) * | 1993-10-05 | 1994-07-20 | 于益民 | High effect resin trap |
| CN203155235U (en) * | 2013-03-18 | 2013-08-28 | 玉锋实业集团有限公司 | Leakage prevention and collection device in resin tank |
| CN203577407U (en) * | 2013-10-14 | 2014-05-07 | 鞍钢股份有限公司 | Resin trapper |
| CN104511199A (en) * | 2013-09-30 | 2015-04-15 | 何光辉 | Vertical-type resin trapper |
| CN105562125A (en) * | 2014-11-10 | 2016-05-11 | 何光辉 | Novel metal resin trapper |
-
2017
- 2017-07-25 CN CN201710613306.8A patent/CN107285519B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63315189A (en) * | 1988-06-03 | 1988-12-22 | Ebara Infilco Co Ltd | Condensate treatment method |
| CN2172155Y (en) * | 1993-10-05 | 1994-07-20 | 于益民 | High effect resin trap |
| CN203155235U (en) * | 2013-03-18 | 2013-08-28 | 玉锋实业集团有限公司 | Leakage prevention and collection device in resin tank |
| CN104511199A (en) * | 2013-09-30 | 2015-04-15 | 何光辉 | Vertical-type resin trapper |
| CN203577407U (en) * | 2013-10-14 | 2014-05-07 | 鞍钢股份有限公司 | Resin trapper |
| CN105562125A (en) * | 2014-11-10 | 2016-05-11 | 何光辉 | Novel metal resin trapper |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107285519B (en) | 2019-11-26 |
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