CN107285519B - A kind of condensed water precision processing system - Google Patents

A kind of condensed water precision processing system Download PDF

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Publication number
CN107285519B
CN107285519B CN201710613306.8A CN201710613306A CN107285519B CN 107285519 B CN107285519 B CN 107285519B CN 201710613306 A CN201710613306 A CN 201710613306A CN 107285519 B CN107285519 B CN 107285519B
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CN
China
Prior art keywords
resin particle
detection bar
flow rate
high flow
mixed bed
Prior art date
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CN201710613306.8A
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Chinese (zh)
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CN107285519A (en
Inventor
孙泽杭
李强
张贺
徐威
孙健
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhejiang Zheneng Shaoxing Binhai Cogeneration Co Ltd
Original Assignee
Zhejiang Zheneng Shaoxing Binhai Cogeneration Co Ltd
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Priority to CN201710613306.8A priority Critical patent/CN107285519B/en
Publication of CN107285519A publication Critical patent/CN107285519A/en
Application granted granted Critical
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • C02F2001/427Treatment of water, waste water, or sewage by ion-exchange using mixed beds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02Non-contaminated water, e.g. for industrial water supply
    • C02F2103/023Water 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 systems; including fore filter, high flow rate mixed bed; filter screen is provided in outlet pipe; it is provided with the testing agency for detecting resin particle accumulating amount in the outlet pipe of filter screen side, the Hui Zhi mechanism for being recovered to the resin particle of accumulation in water inlet pipe is provided on outlet pipe.The present invention has the following advantages and effects: this programme utilizes new mechanical structure, utilize filter screen filtration resin particle, resin particle after accumulation, which enters in filter bag, to be collected, detection bar can be pushed to rotate after resin particle is accumulated to a certain extent, operator is the rotation that detection bar can be observed through observation window, the resin particle of accumulation is transported in water inlet pipe by returning rouge pipe followed by liposuction pump, resin particle and water are transported in high flow rate mixed bed by water inlet pipe together again;Whole process realization eaily recycles the resin particle gone out from high flow rate mixed bed internal leakage, meets energy-saving and environment-friendly objective.

Description

A kind of condensed water precision processing system
Technical field
The present invention relates to water-treatment technology field, in particular to a kind of condensed water precision processing system.
Background technique
Ion exchange resin in modern power plants is usually required through fore filter and high flow rate mixed bed.
Currently, 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, condensate recovery tank and condensation Also it is connected with back water pump, deironing filter, level-one oil removal filter, second level oil removal filter, high flow rate mixed bed between water tank in turn And resin catcher, condensate tank successively connect backwash water tank with condensate pump and radiator and connect with backwash water pump, backwash water Pump is connect with deironing filter, level-one oil removal filter, second level oil removal filter respectively.Deironing filter, level-one oil removing filtering Device, second level oil removal filter, high flow rate mixed bed are connect with compressed air reservoir respectively.High flow rate mixed bed is also stored up with alkali liquor storage tank and acid solution Tank connection.
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 filtered resins will be rinsed away directly;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, influence the resin in high flow rate mixed bed To the desalination effect of condensed water.
Summary of the invention
The object of the present invention is to provide a kind of condensed water precision processing system, can eaily recycle mixed from high speed The resin particle that bed internal leakage is gone out.
Above-mentioned technical purpose of the invention has the technical scheme that a kind of condensate polishing treatment system It unites, including fore filter, high flow rate mixed bed, is provided on the water inlet end of the high flow rate mixed bed for being connected in the prefilter Water inlet pipe on device is connected with outlet pipe on the water outlet of the high flow rate mixed bed, filter screen is provided in the outlet pipe, described It is provided with the testing agency for detecting resin particle accumulating amount in the outlet pipe of filter screen side, is set on the outlet pipe It is equipped with the Hui Zhi mechanism for being recovered to the resin particle of accumulation in the water inlet pipe.
By using above scheme, the water after fore filter filters enters high flow rate mixed bed by water inlet pipe Interior, the water after then passing through high flow rate mixed bed desalination is transferred out by outlet pipe, wherein utilizing the filtering being arranged in outlet pipe Net, the resin particle that filter screen can will come out from high flow rate mixed bed internal leakage, when resin particle is constantly accumulated on filter screen Afterwards, using the accumulating amount of testing agency's detection resin particle, after detecting that accumulation is excessive, using Hui Zhi mechanism by the tree of accumulation Rouge particle is recovered in water inlet pipe, and resin particle and water are transported in high flow rate mixed bed by water inlet pipe together 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 are as follows: the filter screen is in coniform, the institute being open towards the high flow rate mixed bed side State the filter bag being fixed on the one end of filter screen far from the high flow rate mixed bed for collecting resin particle.
By using above scheme, work as resin particle towards the coniform of high flow rate mixed bed side in opening using filter screen After accumulating on filter screen, resin particle can be pooled to mistake of the filter screen far from high flow rate mixed bed one end with the inner wall of filter screen In filter bag, resin particle can realize accumulation in filter bag, reduce because influencing after accumulation of the resin particle on filter screen A possibility that speed that water flow passes through in filter screen.
The further setting of the present invention are as follows: the testing agency includes the institute being rotatably connected on the upside of the filter bag State the detection bar in outlet pipe, one end is fixed in the detection bar and the other end is fixed on the bullet on the inner wall of the outlet pipe Spring, the spring are formed with recessed portion after driving one end of the detection bar to contradict on the filter bag outer wall, are located at described It is provided with observation window on the outlet pipe side wall of the one end of detection bar far from the filter bag, the resin in the filter bag When particle packing is excessive, resin particle pushes the detection bar that the detection bar is rotated.
By using above scheme, after at the position that the resin particle in filter bag is stacked into recessed portion, the tree of accumulation Rouge particle can generate thrust to detection bar one end in recessed portion, so that detection bar rotates, operator is 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 mechanism recycles resin particle, spring pushes detection bar rotation, so that detection bar continues to contradict the shape on filter bag At recessed portion.
The further setting of the present invention are as follows: offer rotation hole in the detection bar, fixed on the inner wall of the outlet pipe There is the shaft for passing through the rotation hole, between described detection bar one end of the filter bag side and the rotation hole Away from be greater than positioned at the observation window side described detection bar one end at a distance from the rotation hole.
By using above scheme, it is greater than using the spacing of detection bar one end and rotation hole for being located at filter bag side and is located at Detection bar one end of observation window side is at a distance from rotation hole, when the resin particle of accumulation pushes detection bar to rotate, benefit With lever principle, detection bar can be more easier to rotate, so that the sensitivity of detection bar is more preferable.
The further setting of the present invention are as follows: the detection bar is contradicted far from one end of the filter bag in the observation window On inner wall, it is greater than positioned at described detection bar one end of the filter bag side and the spacing of the high flow rate mixed bed and is located at the observation Described detection bar one end of window side is at a distance from the high flow rate mixed bed.
By using above scheme, it is greater than position using the spacing of detection bar one end and high flow rate mixed bed for being located at filter bag side In observation window side detection bar one end at a distance from high flow rate mixed bed, detection bar can be at inclined state at this time, and tilt Direction along the direction of water flow, detection bar can be more easier to rotate at this time, so that the sensitivity of detection bar is more preferable;Together When detection bar far from filter bag one end contradict on the inner wall of observation window, detection bar can cannot invert at this time.
The further setting of the present invention are as follows: the detection bar is fixed with for contradicting on one end far from the filter bag Detection block on the observation window is provided with noctilucent powder layer in the detection block.
It is often more dim when night time operation by using above scheme, the luminescent powder in detection block is utilized at this time Layer, noctilucent powder layer can issue light at night itself, operator can be facilitated to see the rotation of detection bar clearly in time at this time, convenient Operator clears up the resin particle of accumulation in time.
The further setting of the present invention are as follows: the Hui Zhi mechanism includes that one end is connected in the filter bag far from the filtering On net one end and the other end is connected to returning rouge pipe, being connected to the rouge pipe that returns close to the outlet pipe side on the water inlet pipe Cut rouge valve, be connected to the liposuction pump returned on rouge pipe.
By using above scheme, returns on rouge pipe and cut rouge valve due to preventing the water entered back in rouge pipe from flowing back into high speed It in mixed bed, after operator observes detection bar rotation, opens and cuts rouge 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 are as follows: the Hui Zhi mechanism further include be located at the high flow rate mixed bed and the filter screen it Between the outlet pipe on the first valve, on the water inlet pipe between the fore filter and described time rouge pipe Second valve.
It closes the first valve after operator observes detection bar rotation by using above scheme and closes second Valve, high flow rate mixed bed is in the state not also being discharged of not intaking at this time, opens cut rouge valve at this time, and 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;The pump of liposuction at this time will not be by excessive water It is fed together in water inlet pipe together with resin particle, high flow rate mixed bed is conducive to increase resin without reprocessing excessive water The service life of grain.
In conclusion the invention has the following advantages: using filter screen filtration from high flow rate mixed bed internal leakage come out Resin particle, the resin particle after accumulation, which enters in filter bag, to be collected, and is after resin particle is accumulated to a certain extent Detection bar can be pushed to rotate, operator is the rotation that detection bar can be observed through observation window, is pumped followed by liposuction by heap Long-pending resin particle is transported in water inlet pipe by returning rouge pipe, and resin particle and water are transported to high flow rate mixed bed again by water inlet pipe together It is interior;Whole process realization eaily recycles the resin particle gone out from high flow rate mixed bed internal leakage, and high speed is effectively ensured The desalination effect of resin in mixed bed to condensed water.
Detailed description of the invention
Fig. 1 is schematic structural view of the invention;
Fig. 2 is the enlarged drawing in the portion A in Fig. 1, is mainly used for embodying filter screen, filter bag, the connection between testing agency is closed System.
In figure: 1, fore filter;2, high flow rate mixed bed;3, water inlet pipe;4, outlet pipe;41, filter screen;42, filter bag; 43, observation window;44, shaft;5, testing agency;51, detection bar;511, rotation hole;512, detection block;513, noctilucent powder layer;52, Spring;521, recessed portion;6, Hui Zhi mechanism;61, rouge pipe is returned;62, rouge valve is cut;63, liposuction pumps;64, the first valve;65, second Valve.
Specific embodiment
Below in conjunction with attached drawing, invention is further described in detail.
A kind of condensed water precision processing system, referring to Fig.1, this kind of condensed water precision processing system include fore filter 1 and height Fast mixed bed 2, this kind of fore filter 1 are 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 the water inlet pipe 3 for being connected on fore filter 1 on end, the second valve 65 is installed on water inlet pipe 3;And high speed is mixed It is connected with the outlet pipe 4 for water water delivery to be gone out on the water outlet of 2 lower ends of bed, first valve 64 is installed on outlet pipe 4.
Referring to Fig.1, Fig. 2, in outlet pipe 4 of first valve 64 far from 2 side of high flow rate mixed bed (in figure not by bolt Show) it is fixed with filter screen 41, and filter screen 41, in being open towards the coniform of 2 side of high flow rate mixed bed, wherein filter screen 41 is remote Filter bag 42 is fixedly installed with by bolt (not shown) on one end from high flow rate mixed bed 2, under filtering from filter screen 41 The resin particle come, which will be pooled in filter bag 42, to be collected.
Shaft 44, extending direction and the filter bag 42 of shaft 44 are welded in the outlet pipe 4 of 42 upside of filter bag Extending direction is perpendicular;It wherein is connected with detection bar 51 in shaft 44, is installed on 4 side wall of outlet pipe of 51 upper end of detection bar There is observation window 43;The rotation hole 511 passed through for shaft 44 is offered in detection bar 51, and is located at the detection bar of 42 side of filter bag 51 one end and the spacing of rotation hole 511 are greater than at a distance from 51 one end of detection bar of 43 side of observation window and rotation hole 511.
One end of detection bar 51 contradicts on the outer wall of filter bag 42, and wherein detection bar 51 is supported far from one end of filter bag 42 Touching is located at 51 one end of detection bar of 42 side of filter bag and the spacing of high flow rate mixed bed 2 greater than position on the inner wall of observation window 43 In 43 side of observation window 51 one end of detection bar at a distance from high flow rate mixed bed 2;Simultaneously close to the detection bar 51 of 42 side of filter bag On be welded with spring 52, spring 52 is welded on the inner wall of outlet pipe 4 far from one end of detection bar 51, spring 52 drive detection bar 51 one end far from observation window 43 contradict on filter bag 42 and are formed with recessed portion 521.
Detection bar 51 is welded with detection block 512 on one end far from filter bag 42, be bonded with noctilucent powder layer in detection block 512 513, and noctilucent powder layer 513 is wrapped in detection block 512 by glass plate, when night, operator still can use noctilucence The light that bisque 513 issues observes the rotation of detection bar 51.
Referring to Fig.1, be connected with back rouge pipe 61 on outlet pipe 4, return rouge pipe 61 one end be passed into outlet pipe 4 inside and with Filter bag 42 is communicated far from one end of filter screen 41, and is returned rouge pipe 61 and be connected to far from one end of outlet pipe 4 positioned at the second valve On 65 water inlet pipes 3 far from 1 side of fore filter;It wherein returns rouge pipe 61 and a section rouge valve is installed on the side of outlet pipe 4 62, after the resin particle in filter bag 42 is stacked into back in rouge pipe 61, resin particle and water are prevented together using rouge valve 62 is cut It passes back into water inlet pipe 3;It is located to cut on time rouge pipe 61 between rouge valve 62 and water inlet pipe 3 simultaneously and liposuction pump 63, liposuction is installed Pump 63 is for resin particle to be withdrawn into water inlet pipe 3.
Principle: referring to Fig.1, Fig. 2, the resin particle come out using the filtering of filter screen 41 from 2 internal leakage of high flow rate mixed bed, accumulation Resin particle afterwards is entered in filter bag 42 and is collected, and can push detection bar after resin particle is accumulated to a certain extent 51, so that detection pipe rotates;Operator can observe turning for detection bar 51 through observation window 43 by detection block 512 Dynamic, detection bar 51, spring 52 are the testing agency 5 that can be configurable for detection resin particle accumulating amount at this time;It is then turned off first Valve 64 and the second valve 65 of closing, high flow rate mixed bed 2 is in the state not also being discharged of not intaking at this time, opens cut a rouge valve at this time 62, resin can be withdrawn into water inlet pipe 3 by starting liposuction pump 63, and resin particle is sent to high flow rate mixed bed 2 by water inlet pipe 3 Interior, returning rouge pipe 61, section rouge valve 62, the 63, first valve 64 of liposuction pump, the second valve 65 at this time can be configurable for the tree that will be accumulated Rouge particle is recovered to the Hui Zhi mechanism 6 in water inlet pipe 3;Whole process realization is eaily recycled out of high flow rate mixed bed 2 The resin particle to let out meets energy-saving and environment-friendly principle.
This specific embodiment is only explanation of the invention, is not limitation of the present invention, those skilled in the art Member can according to need the modification that not creative contribution is made to the present embodiment after reading this specification, but as long as at this All by the protection of Patent Law in the scope of the claims of invention.

Claims (5)

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) into It is provided on water end (W.E.) for being connected to the water inlet pipe (3) on the fore filter (1), the water outlet of the high flow rate mixed bed (2) On be connected with outlet pipe (4), it is characterised in that: is provided with filter screen (41) in the outlet pipe (4), the filter screen (41) one The testing agency (5) for detecting resin particle accumulating amount is provided in the outlet pipe (4) of side, on the outlet pipe (4) It is provided with the Hui Zhi mechanism (6) for being recovered to the resin particle of accumulation in the water inlet pipe (3);
The filter screen (41) is in opening towards the coniform of the high flow rate mixed bed (2) side, and the filter screen (41) is far from institute State the filter bag (42) being fixed on one end of high flow rate mixed bed (2) for collecting resin particle;
The testing agency (5) includes the inspection being rotatably connected in the outlet pipe (4) on the upside of the filter bag (42) Measuring staff (51), one end are fixed on the detection bar (51) and the other end is fixed on the spring on the inner wall of the outlet pipe (4) (52), the spring (52) is formed with recessed after driving one end of the detection bar (51) to contradict on the filter bag (42) outer wall Concave portion (521) is located on the outlet pipe (4) side wall of the detection bar (51) far from the one end of the filter bag (42) and is arranged There are observation window (43), when the resin particle accumulation in the filter bag (42) is excessive, resin particle pushes the detection bar (51) detection bar (51) is made to rotate;
The Hui Zhi mechanism (6) includes that one end connection is on the filter bag (42) the separate filter screen (41) one end and another End connection going back to rouge pipe (61), being connected to go back to rouge pipe (61) close to the outlet pipe (4) side on the water inlet pipe (3) Cut rouge valve (62), be connected to the liposuction pump (63) returned on rouge pipe (61).
2. a kind of condensed water precision processing system according to claim 1, it is characterised in that: opened up on the detection bar (51) Have rotation hole (511), is fixed on the inner wall of the outlet pipe (4) for the shaft (44) across the rotation hole (511), position It is greater than in the detection bar (51) one end of the filter bag (42) side and the spacing of the rotation hole (511) and is located at the sight The detection bar (51) one end of window (43) side is examined at a distance from the rotation hole (511).
3. a kind of condensed water precision processing system according to claim 2, it is characterised in that: the detection bar (51) is far from institute The one end for stating filter bag (42) contradicts on the inner wall of the observation window (43), is located at the inspection of the filter bag (42) side The spacing of measuring staff (51) one end and the high flow rate mixed bed (2) is greater than the detection bar (51) positioned at the observation window (43) side One end is at a distance from the high flow rate mixed bed (2).
4. a kind of condensed water precision processing system according to claim 3, it is characterised in that: the detection bar (51) is far from institute It states and is fixed on one end of filter bag (42) for contradicting the detection block (512) on the observation window (43), the detection block (512) noctilucent powder layer (513) are provided on.
5. a kind of condensed water precision processing system according to claim 1, it is characterised in that: the Hui Zhi mechanism (6) is also wrapped It includes the first valve (64) on the outlet pipe (4) between the high flow rate mixed bed (2) and the filter screen (41), be located at The second valve (65) on the water inlet pipe (3) between the fore filter (1) and described time rouge pipe (61).
CN201710613306.8A 2017-07-25 2017-07-25 A kind of condensed water precision processing system Active CN107285519B (en)

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

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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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CN107285519A CN107285519A (en) 2017-10-24
CN107285519B true CN107285519B (en) 2019-11-26

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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112834139A (en) * 2021-03-11 2021-05-25 西安热工研究院有限公司 Condensate fine treatment filler leakage online detection device and leakage judgment method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
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

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