CN205803137U - A kind of burning power plant cooling water treatment system - Google Patents
A kind of burning power plant cooling water treatment system Download PDFInfo
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- CN205803137U CN205803137U CN201620505956.1U CN201620505956U CN205803137U CN 205803137 U CN205803137 U CN 205803137U CN 201620505956 U CN201620505956 U CN 201620505956U CN 205803137 U CN205803137 U CN 205803137U
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- water
- filter
- ultrafiltration
- water tank
- reverse osmosis
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Abstract
The utility model discloses a kind of processing system for garbage burning factory cooling water, belong to industrial circulating cooling water and process process regime.This dedicated processes system contains more medium filter, softening plant, clear water tanks, video disc filter, ultrafiltration apparatus, ultrafiltration water tank, reverse osmosis unit, reverse osmosis water tank.This utility model solves corrosion and scaling and the problem of foundry loam that recirculated water is in use brought, and chemistry method for dosing medicine, the drawback of conventional film facture, this system is while solving above-mentioned drawback, achieve " zero-emission " truly, improve the service life of nucleus equipment, respond the policy of national green production, energy-saving and emission-reduction.
Description
Technical field
This utility model relates to a kind for the treatment of process of circulating cooling water, is specifically related at a kind of burning power plant cooling water
Reason system.
Background technology
In many chemical enterprises, the biggest for this part water yield of cooling system, usually account for enterprise and use
The 90%~about 95% of water inventory.At present, in the process of industrial colling, most enterprises are all by reclaiming circulation
Using, the amount of makeup water wherein cooling down water is about the 3%-4% of quantity of circulating water, and the 30% of amount of makeup water will be used for evaporative cooling,
Remainder will be recycled.
The make-up water of cooling water typically directly takes from river, river, lake water, or i.e. comes into operation after carrying out simple sand filtration, cold
But water is constantly concentrated during recycling and causes salinity to increase, and electrical conductivity rises, and also exacerbates corrosion and scaling
Tendency.Meanwhile, cooling water in use constantly contacts with surrounding, absorbs the dust in air and impurity, with
Time cooling tower in illumination, suitable temperature all antibacterial and algae will be grown generation facilitation.Corrosion will be led with fouling
Causing heat exchanger leakage quickly occurs and scraps, the glutinous mud formed that grows of antibacterial and algae makes resistance to water-flow increase, heat exchange
The heat transfer efficiency of device reduces, and equipment energy consumption increases.
For corrosion and scaling and the problem of glutinous mud, conventional processing method is to carry out by the way of adding chemical drugs
Prevention and delaying, reduces the salinity of recirculated water in the way of periodically draining the dense water of part simultaneously, dense by circulation
Demagnification rate maintains proper level.The drawback brought of chemical treatment method of cooling water is: fail essence by recirculated water
Contained salinity is removed, want to maintain suitable concentration rate and will not in water salinity too high, can only be by discharging the side of dense water
Formula, this mode not only causes the waste of water resource, causes the waste of chemical agent and the pollution to environment simultaneously.
At present, for corrosion and scaling and the problem of glutinous mud, have also appeared a kind of deeper circulating water treatment process,
I.e. remove the salinity in recirculated water by reverse osmosis process.The drawback of this method is the producing water ratio that the scale-forming ion in water is easily caused film
Decline, shorten service life and the waste of water resource of film.
Utility model content
In order to solve corrosion and scaling and the problem of foundry loam that recirculated water is in use brought, and chemistry dosing
Method, the drawback of conventional film facture, this utility model devises a kind of special system for burning power plant cold water process
System, this system is while solving above-mentioned drawback, it is achieved that " zero-emission " truly, improves the use of nucleus equipment
In the life-span, respond the policy of national green production, energy-saving and emission-reduction.
The dedicated system that this utility model is used contains with lower unit: more medium filter, softening plant, water purification
Case, video disc filter, ultrafiltration apparatus, ultrafiltration water tank, security personnel filter, reverse osmosis unit, reverse osmosis water tank, cleaning filter.This is specially
More medium filter the first inlet channel 1, water intaking valve 2 and delivery pump is passed through with more medium filter in system and cooling tower water tank
3 are connected;In this dedicated system, demineralizer is connected by demineralizer the first inlet channel 4 with more medium filter;This is special
In system, clear water tanks is connected by clear water tanks the first inlet channel 5 with demineralizer;In this dedicated system, video disc filter is with clean
Water tank is connected with clarified water pump 7 by video disc filter the first inlet channel 6;In this dedicated system, ultrafiltration apparatus and video disc filter
Device is connected by ultrafiltration the first inlet channel 8;In this dedicated system, ultrafiltration water tank and ultrafiltration apparatus are by ultrafiltration water tank first
Inlet channel 9 is connected;In this dedicated system, security personnel's filter and ultrafiltration water tank are by security personnel filter the first water inlet pipe 10, UF water pump
11 are connected;In this dedicated system, reverse osmosis unit and security personnel's filter are by reverse osmosis the first inlet channel 12 and high-pressure pump 13 phase
Connect;In this dedicated system, RO product water tank is connected by RO water tank the first water inlet pipe 14 with RO device;This dedicated system produces water
Via looping back Jellyfish pipe 15 and reverse osmosis produced water pump 16 is delivered to after heat exchanger carries out heat exchange, be recycled to cooling tower water tank.
RO device water for cleaning in this dedicated system, by RO water tank by RO water tank the first outlet pipe 17, RO flushing water pump
18, after cleaning filter filtration delivered to by cleaning filter the first water inlet pipe 19, enter RO device via RO the second water inlet pipe 20 and carry out clearly
Wash;Ultrafiltration apparatus in this dedicated system, demineralizer, more medium filter water for cleaning by ultrafiltration water tank by ultrafiltration water tank the
One outlet pipe 21 and rinse water delivery pump 22, ultrafiltration the second water inlet pipe 23, demineralizer the second water inlet pipe 24, more medium filter
Two water inlet pipes 25 are supplied to that ultrafiltration apparatus, demineralizer and more medium filter are counter to be cleaned.
In this dedicated system, the dense water of each device passes through more medium filter drain pipe 26, demineralizer drain pipe 27, video disc mistake
Filter drain pipe 28, ultrafiltration drain pipe 29, reverse osmosis drain pipe 30 collect, and wherein 17% stir for dry ash, and 21% uses
In place water, 23% is used for slag remover cooling water, and 39% enters clean Waste Water Treatment.Meanwhile, after place is rinsed
The dense water of draining and clean Waste Water Treatment converges into garden dope centralized processing system.
Profitable fruit of the present utility model is:
One, while this dedicated system solves system corrosion, fouling and the foundry loam problem that recirculated water easily causes, in fortune
Chemical agent need not be added during row, reduce the operating cost of circulating water treatment, also avoid the ring caused because of medicament
Environment pollution;
Two, the water yield that the amount of makeup water of this dedicated system is only walked by wind in cooling procedure and evaporator strip, and system
Backwash institute water requirement composition, amount of makeup water is about the 1.5-2.0% of recirculated water total amount.Because system need not be circulated outside dense water
Row, the dense water that the most each device collects will stir as dry ash, place water, slag remover cooling water use, and remain dense water and enter
Enter plant area's cleaning Waste Water Treatment.The clean dense water of Waste Water Treatment and plant area's flush discharge will enter at garden dope concentration
Reason system, therefore this dedicated system achieves " zero-emission " in the water yield and decreases the consumption of the municipal public use water yield.
Three, this dedicated system can fundamentally remove the salinity in recirculated water rather than by the way of outer draining desalination,
Ca in water2+、Mg2+、Cl-Plasma can make the concentration rate of system reach 8-12 on the premise of not producing corrosion and scaling tendency.
Four, for circulating water quality feature, this dedicated system is better than conventional embrane method and processes, and shows that its response rate can reach
75%, improve water-saving result, in system, the service life of reverse osmosis membrane can reach 3-5.
Accompanying drawing illustrates:
With embodiment, this utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is the novel schematic diagram of this use;
1. more medium filter the first inlet channel in figure, 2. water intaking valve, 3. delivery pump, 4. demineralizer the first water inlet pipe
Road, 5. clear water tanks the first inlet channel, 6. video disc filter the first inlet channel, 7. clarified water pump, 8. ultrafiltration the first inlet channel,
9. ultrafiltration water tank the first inlet channel, 10. security personnel's filter the first water inlet pipe, 11. ultrafiltration water pumps, 12. reverse osmosis the first water inlet pipes
Road, 13. high-pressure pumps, 14.RO water tank the first water inlet pipe, 15. loop back Jellyfish pipe, 16. reverse osmosis produced water pumps, 17.RO water tank
One outlet pipe, 18.RO flushing water pump, 19. cleaning filter the first water inlet pipes, 20. reverse osmosis the second water inlet pipes, 21.UF water tank
One outlet pipe, 22. rinse water delivery pumps, 23. ultrafiltration the second water inlet pipes, 24. demineralizer the second water inlet pipes, 25. multi-medium filterings
Device the second water inlet pipe, 26. more medium filter drain pipies, 27. demineralizer drain pipies, 28. video disc filter drain pipies, 29. surpass
Filter drain pipe, 30. reverse osmosis drain pipies.
Detailed description of the invention
In certain embodiment, this dedicated system include more medium filter, softening plant, clear water tanks, video disc filter,
Ultrafiltration apparatus, ultrafiltration water tank, security personnel filter, reverse osmosis unit, reverse osmosis water tank, cleaning filter.Recirculated water is through multi-medium filtering
Device the first water inlet pipe 1, water intaking valve 2, delivery pump 3 enter more medium filter thus by float, granule and colloid in recirculated water
Remove.More medium filter produces water and enters demineralizer via demineralizer the first water inlet pipe 4, and demineralizer is big portion in removing recirculated water
The scale problems that subsequent ultrafiltration film and reverse osmosis membrane produce can also be prevented because of calcium, magnesium plasma while dividing scale-forming ion.Soften
Device produces water and is entered clear water tanks cached by clear water tanks the first water inlet pipe 5, then via video disc filter the first water inlet pipe 6, clean
Water pump 7 enters video disc filter and filters, and video disc filter can prevent the medium and small quartz sand fine particle thing in 100 μ of water from blocking up
Plug subsequent ultrafiltration film.Video disc filter product water enters ultrafiltration apparatus via ultrafiltration the first water inlet pipe 8 and filters, and ultrafiltration is being filtered
Fall the service life that can extend follow-up reverse osmosis membrane in water while macromolecular substances.Ultrafiltration is produced water and is entered via ultrafiltration water tank first
Water pipe 9 is cached in ultrafiltration water tank, and ultrafiltration water tank water outlet enters security personnel's filter via security personnel's filter the first water inlet pipe 10, ultrafiltration water pump 11
Device filters, and security personnel's filter produces water and enters reverse osmosis through row filtration, RO product via reverse osmosis the first water inlet pipe 12, high-pressure pump 13
Water is cached in RO water tank via RO water tank the first water inlet pipe 14.RO water tank water outlet is via looping back Jellyfish pipe 15 and reverse osmosis produced water
Pump 16 is being back to cooling tower after heat exchanger heat exchange.
In certain embodiment, the cleaning of RO device is supplied by RO water tank, and rinse water is clear from RO water tank the first outlet pipe 17, RO
After wash water pump 18, cleaning filter the first water inlet pipe 19 enter cleaning filter filtration, reverse osmosis the second water inlet pipe 20 enter reverse osmosis
Device filters thoroughly.More medium filter, demineralizer, the rinse water of ultrafiltration are supplied by ultrafiltration water tank, and rinse water is from ultrafiltration water
Case the first outlet pipe 21 and rinse water delivery pump 22 flow out, and flow through ultrafiltration the second water inlet pipe 23 and supply ultrafiltration apparatus and carry out instead in way
Clean, way flows through demineralizer the second water inlet pipe 24 and supplies that demineralizer is counter to be cleaned, way flows through more medium filter second
Water inlet pipe 25 supplies that more medium filter is counter to be cleaned.
In certain embodiment, more medium filter backwash water, demineralizer backwash water, video disc filter backwash water, ultrafiltration are dense
Water and backwash water, reverse osmosis concentrated water and backwash water are respectively through more medium filter drain pipe 26, demineralizer drain pipe 27, video disc
Filter drain pipe 28, ultrafiltration drain pipe 29, reverse osmosis drain pipe 30 collects, and wherein 17% stirs for dry ash, 21%
For place water, 23% is used for slag remover cooling water, and 39% enters clean Waste Water Treatment.Meanwhile, after place is rinsed
Draining and the dense water of clean Waste Water Treatment converge into garden dope centralized processing system.
Claims (1)
1. a burning power plant cooling water treatment system, including more medium filter, softening plant, clear water tanks, video disc mistake
Filter, ultrafiltration apparatus, ultrafiltration water tank, security personnel filter, reverse osmosis unit, reverse osmosis water tank, cleaning filter, it is characterised in that: many
Medium filter and cooling tower water tank are by more medium filter the first inlet channel (1), water intaking valve (2) and delivery pump (3) phase
Even, demineralizer is connected by demineralizer the first inlet channel (4) with more medium filter, and clear water tanks and demineralizer pass through clear water tanks
First inlet channel (5) is connected, and video disc filter and clear water tanks are by video disc filter the first inlet channel (6) and clarified water pump
(7) being connected, ultrafiltration apparatus is connected by ultrafiltration the first inlet channel (8) with video disc filter, and ultrafiltration water tank and ultrafiltration apparatus lead to
Crossing ultrafiltration water tank the first inlet channel (9) to be connected, security personnel's filter and ultrafiltration water tank are by security personnel's filter the first water inlet pipe (10), UF
Water pump (11) is connected, and reverse osmosis unit is connected with high-pressure pump (13) by reverse osmosis the first inlet channel (12) with security personnel's filter,
RO is produced water tank and is connected by RO water tank the first water inlet pipe (14) with RO device, produces water via looping back Jellyfish pipe (15) and reverse osmosis
Thoroughly produce water pump (16) to deliver to after heat exchanger carries out heat exchange, be recycled to cooling tower water tank;RO device water for cleaning in described system
Delivered to clearly by RO water tank the first outlet pipe (17), RO flushing water pump (18), cleaning filter the first water inlet pipe (19) by RO water tank
After filter washer filters, enter RO device via RO the second water inlet pipe (20) and be carried out;Ultrafiltration apparatus, softening in described system
Device, the water for cleaning of more medium filter are passed through ultrafiltration water tank the first outlet pipe (21) and rinse water delivery pump by ultrafiltration water tank
(22), ultrafiltration the second water inlet pipe (23), demineralizer the second water inlet pipe (24), more medium filter the second water inlet pipe (25) are supplied to surpass
Filter device, demineralizer and more medium filter is counter cleans;In described system, the dense water of each device is arranged by more medium filter
Water pipe (26), demineralizer drain pipe (27), video disc filter drain pipe (28), ultrafiltration drain pipe (29), reverse osmosis drain pipe
(30) collecting, wherein 17% stir for dry ash, 21% is used for place water, and 23% is used for slag remover cooling water, and 39% enters
Entering clean Waste Water Treatment, draining and the dense water of clean Waste Water Treatment after the flushing of place converge into garden dope and concentrate
Processing system.
Priority Applications (1)
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CN201620505956.1U CN205803137U (en) | 2016-05-27 | 2016-05-27 | A kind of burning power plant cooling water treatment system |
Applications Claiming Priority (1)
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CN201620505956.1U CN205803137U (en) | 2016-05-27 | 2016-05-27 | A kind of burning power plant cooling water treatment system |
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CN205803137U true CN205803137U (en) | 2016-12-14 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108558125A (en) * | 2018-02-14 | 2018-09-21 | 中国国际贸易中心股份有限公司 | It is suitable for the stain disease processing method and system of public building comprehensive utilization |
-
2016
- 2016-05-27 CN CN201620505956.1U patent/CN205803137U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108558125A (en) * | 2018-02-14 | 2018-09-21 | 中国国际贸易中心股份有限公司 | It is suitable for the stain disease processing method and system of public building comprehensive utilization |
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