CN208916852U - The Zero emission device that concentration is evaporated waste water is evaporated using boiler smoke waste heat - Google Patents
The Zero emission device that concentration is evaporated waste water is evaporated using boiler smoke waste heat Download PDFInfo
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- CN208916852U CN208916852U CN201821276731.9U CN201821276731U CN208916852U CN 208916852 U CN208916852 U CN 208916852U CN 201821276731 U CN201821276731 U CN 201821276731U CN 208916852 U CN208916852 U CN 208916852U
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- waste water
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- 239000002351 wastewater Substances 0.000 title claims abstract description 55
- 239000000779 smoke Substances 0.000 title claims abstract description 10
- 239000002918 waste heat Substances 0.000 title claims abstract description 10
- 238000001035 drying Methods 0.000 claims abstract description 37
- 238000001704 evaporation Methods 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 230000003139 buffering Effects 0.000 claims abstract description 11
- 239000007921 spray Substances 0.000 claims abstract description 11
- 230000003009 desulfurizing Effects 0.000 claims description 14
- 239000000945 filler Substances 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 15
- 239000003546 flue gas Substances 0.000 abstract description 15
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000010842 industrial wastewater Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000012267 brine Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Chemical compound 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- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000005712 crystallization Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000001187 sodium carbonate Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The Zero emission device that concentration is evaporated waste water is evaporated using boiler smoke waste heat, part is evaporated including being concentrated by evaporation part and concentrated water, part is concentrated by evaporation to draw a part of 90~160 DEG C of low-temperature flue gas from electric precipitator rear pass, enter after the first bypass blower pressurization and is concentrated by evaporation tower, waste water is forced into through waste water circulating pump and is concentrated by evaporation tower top spray, concentrated water is evaporated part to draw a part of 100~170 DEG C of low-temperature flue gas from air preheater rear pass, drying tower is led to after bypass blower pressurization, concentrated waste water leads to drying tower top through concentrated water pump pressurization and is sprayed, drying tower is connected with electric precipitator, buffering ash can is set below drying tower；Flue draws a part of 300~360 DEG C of high-temperature flue gas from before air preheater simultaneously, auxiliary is evaporated drying in the insufficient situation of low-temperature flue gas thermic load, the utility model has the advantages that low energy consumption, investment is low, operating cost is low, can promote the use of wastewater zero discharge field.
Description
Technical field
The utility model belongs to industrial waste water disposal device or equipment technical field, and in particular to utilizes boiler smoke to a kind of
Gas waste heat is evaporated the Zero emission device that concentration is evaporated waste water.
Background technique
Current so-called zero-emission is the near-zero release of waste water, is difficult to realize real zero-emission.Softened using lime
Or after the processing of the chemical precipitation methods such as sodium carbonate is up to standard, still containing the soluble solid of high concentration in waste water, it is difficult to recycle.
If brine waste directly to be sprayed to coal yard secondary pollution easy to form, and equipment can be corroded；Using UF membrane
Technology, such as the disadvantages of reverse osmosis, positive infiltration, nanofiltration exist that investment is high, energy consumption is high, operating cost is high, film easy blocking pollution, most
Whole strong brine also needs the processing such as crystallization.
Although being directly evaporated technology simple process using high-temperature flue gas, equipment is reliable for operation, invests lower, energy consumption
Height, boiler efficiency decline.
In conclusion the prior art also needs inherently to improve, invent it is a kind of energy-efficient, securely and reliably, invest it is low,
The low waste water zero-discharge technology of operating cost.
Summary of the invention
The technical problem to be solved by the utility model is to overcome above-mentioned the deficiencies in the prior art, a kind of design conjunction is provided
Reason, structure are simple, low energy consumption, investment is low, operating cost is low is evaporated concentration using boiler smoke waste heat and is evaporated waste water
Zero emission device.
Solve above-mentioned technical problem the technical solution adopted is that: the outlet of boiler passes through the entrance of pipeline and air preheater
It is connected and the lower inlet of drying tower is connected, the outlet of air preheater is connected by flue with the entrance of electric precipitator
Logical, setting outlet is connected with the entrance of the first bypass blower on the flue between air preheater and electric precipitator, by the of first
The outlet of transportation work style machine is connected with the lower inlet of drying tower, and the upper outlet of drying tower is connected by pipeline with the entrance of electric precipitator
Logical, the lower outlet of drying tower is connected with the entrance of buffering ash can, and the outlet of electric precipitator is connected with the entrance of air-introduced machine, draws
The outlet of blower is connected by flue with the entrance of desulfurizing tower, and the outlet of desulfurizing tower is connected with chimney, air-introduced machine and desulfurization
Setting outlet is connected with the entrance of the second bypass air-introduced machine on flue between tower, the outlet and evaporation of the second bypass air-introduced machine
The lower inlet of inspissator is connected, and the upper outlet of evaporation concentrator is connected with the entrance of desulfurizing tower, lower outlet and waste water tank
One entrance is connected, and waste water is entered by another entrance of waste water tank, and an outlet of waste water tank is dense by waste water circulating pump and evaporation
The upper inlet of contracting device is connected, another outlet is pumped by concentrated water and is connected with the upper inlet of drying tower.
The evaporation concentrator of the utility model are as follows: middle part is provided with filler in concentrator tank body, internal upper part is provided with spray
The entrance of device, spray thrower is connected by the waste water circulating pump being mounted on pipeline with waste water tank, inspissator tank body lower part and useless
Water tank is connected.
The drying tower of the utility model are as follows: drying tower tank body internal upper part is provided with sprayer, and sprayer entrance passes through installation
Concentrated water pump on pipeline is connected with waste water tank, and drying tower tank body lower part is provided with buffering ash can.
The utility model has the advantage that compared with the prior art
The utility model carries out heating evaporation concentration to industrial wastewater using boiler of power plant fume waste heat and is evaporated waste water, in tower
Interior waste water water mist and flue gas come into full contact with heat exchange, are all evaporated, and ash content returns to flue collector with flue gas and removes through electric precipitator, separate
Solid out is discharged to buffering ash can, periodically pumps out the ash content fallen into buffering ash can 14.Solves the highly concentrated Industry Waste of thermal power plant
Water process reduces environmental pollution, reduces the highly concentrated Industrial Wastewater Treatment expense of power plant.The utility model have design rationally,
The advantages that low energy consumption, remarkable in economical benefits, can promote the use of in thermal power plant.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model one embodiment.
Fig. 2 is the structural schematic diagram of evaporation concentrator 9 in Fig. 1.
Fig. 3 is the structural schematic diagram of drying tower 13 in Fig. 1.
In figure: 1, boiler；2, air preheater；3, the first bypass blower；4, electric precipitator；5, air-introduced machine；6, by the of second
Transportation work style machine；7, desulfurizing tower；8, chimney；9, evaporation concentrator；10, waste water tank；11, concentrated water pumps；12, waste water circulating pump；13, dry
Tower；14, ash can is buffered；9-1, inspissator tank body；9-2, filler；9-3, spray thrower；13-1, drying tower tank body；13-2, it is sprayed
Device.
Specific embodiment
The utility model is described in further details with reference to the accompanying drawings and examples, but the utility model is not limited to this
A little embodiments.
Embodiment 1
In Fig. 1, the utility model is evaporated the Zero emission device that concentration is evaporated waste water, pot using boiler smoke waste heat
The outlet of furnace 1 is connected by pipeline with the entrance of air preheater 2 and the lower inlet of drying tower 13 is connected, air preheat
The outlet of device 2 is connected by flue with the entrance of electric precipitator 4, is set on the flue between air preheater 2 and electric precipitator 4
It sets outlet to be connected with the entrance of the first bypass blower 3, draws 100~170 DEG C of low-temperature flue gas, pressurize through the first bypass blower 3
After lead to drying tower 13, the outlet of the first bypass blower 3 is connected with the lower inlet of drying tower 13, and the upper outlet of drying tower 13 leads to
Piping is connected with the entrance of electric precipitator 4, and the lower outlet of drying tower 13 is connected with the entrance of buffering ash can 14, in Fig. 3
In, drying tower 13 described in the present embodiment is by drying tower tank body 13-1, sprayer 13-2, concentrated water pump 11, waste water tank 10, buffering ash
Tank 14 connects and composes, and drying tower tank body 13-1 internal upper part is equipped with sprayer 13-2, and sprayer 13-2 entrance is by being mounted on pipe
Concentrated water pump 11 on road is connected with waste water tank 10, and the lower part drying tower tank body 13-1 is provided with buffering ash can 14, concentrated
Waste water is forced into 13 middle and upper part of drying tower through concentrated water pump 11 and is evaporated by spraying, and waste water water mist comes into full contact with flue gas in drying tower 13
Heat exchange, is all evaporated, and ash content returns to flue collector with flue gas and removes by electric precipitator 4, and buffering ash can 14 is collected and periodically pumped out
Fall into the ash content of 13 lower part of drying tower；A part of 300~350 DEG C of high-temperature flue gas are drawn from flue before air preheater 2 simultaneously,
Auxiliary is evaporated drying in the insufficient situation of low-temperature flue gas thermic load.
The outlet of electric precipitator 4 is connected with the entrance of air-introduced machine 5, and the outlet of air-introduced machine 5 passes through flue and desulfurizing tower 7
Entrance is connected, and the outlet of desulfurizing tower 7 is connected with chimney 8, on the flue between air-introduced machine 5 and desulfurizing tower 7 setting outlet with
The entrance of second bypass air-introduced machine 6 is connected, and the outlet of the second bypass air-introduced machine 6 is connected with the lower inlet of evaporation concentrator 9,
The upper outlet of evaporation concentrator 9 is connected with the entrance of desulfurizing tower 7, lower outlet is connected with an entrance of waste water tank 10, waste water
Entered by another entrance of waste water tank 10, an outlet of waste water tank 10 on waste water circulating pump 12 and evaporation concentrator 9 by entering
Mouth is connected, another outlet is connected by concentrated water pump 11 with the upper inlet of drying tower 13, in Fig. 2, described in the present embodiment
Evaporation concentrator 9 is connected and composed by inspissator tank body 9-1, filler 9-2, spray thrower 9-3, waste water tank 10, waste water circulating pump 12, dense
Middle part is provided with filler in contracting device tank body 9-1, internal upper part is equipped with spray thrower 9-3, and the entrance of spray thrower 9-3 is by being mounted on pipe
Waste water circulating pump 12 on road is connected with waste water tank 10, and the inspissator lower part tank body 9-1 is connected with waste water tank 10, and waste water is through useless
Water-circulating pump 12, which is forced into, is concentrated by evaporation 9 middle and upper part spray of tower, and waste water is sprayed onto filler 9-2 by spray thrower 9-3 to be steamed
Hair concentration heat exchange, the flue gas for flowing through the surface filler 9-2 are quickly cooled down heat dissipation, and flue gas reaches moisture saturation, and smoke temperature drops to 50
~60 DEG C, the flue gas after cooling down returns to desulfurizing tower 7 through bypass flue, and unevaporated waste water flows into waste water tank 10, continues to follow
Ring is concentrated by evaporation.
Claims (3)
1. a kind of be evaporated the Zero emission device that concentration is evaporated waste water using boiler smoke waste heat, it is characterised in that: boiler
Outlet is connected by pipeline with the entrance of air preheater and the lower inlet of drying tower is connected, the outlet of air preheater
It is connected by flue with the entrance of electric precipitator, setting outlet and first on the flue between air preheater and electric precipitator
The entrance of bypass blower is connected, and the outlet of the first bypass blower is connected with the lower inlet of drying tower, the upper outlet of drying tower
It is connected by pipeline with the entrance of electric precipitator, the lower outlet of drying tower is connected with the entrance of buffering ash can, electric precipitator
Outlet be connected with the entrance of air-introduced machine, the outlet of air-introduced machine is connected by flue with the entrance of desulfurizing tower, desulfurizing tower
Outlet is connected with chimney, and setting outlet is connected with the entrance of the second bypass air-introduced machine on the flue between air-introduced machine and desulfurizing tower
Logical, the outlet of the second bypass air-introduced machine is connected with the lower inlet of evaporation concentrator, the upper outlet and desulfurizing tower of evaporation concentrator
Entrance be connected, it is lower outlet be connected with an entrance of waste water tank, waste water by waste water tank another entrance entrance, waste water tank
One outlet is connected by waste water circulating pump with the upper inlet of evaporation concentrator, another outlet pumped by concentrated water it is upper with drying tower
Entrance is connected.
2. according to claim 1 be evaporated the Zero emission device that concentration is evaporated waste water using boiler smoke waste heat,
It is characterized in that the evaporation concentrator are as follows: middle part is provided with filler in concentrator tank body, internal upper part is provided with spray thrower, spray
The entrance of device is connected by the waste water circulating pump being mounted on pipeline with waste water tank, and inspissator tank body lower part is connected with waste water tank
It is logical.
3. according to claim 1 be evaporated the Zero emission device that concentration is evaporated waste water using boiler smoke waste heat,
It is characterized in that the drying tower are as follows: drying tower tank body internal upper part is provided with sprayer, and sprayer entrance is by being mounted on pipeline
On concentrated water pump be connected with waste water tank, drying tower tank body lower part is provided with buffering ash can.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2020108135A1 (en) * | 2018-11-29 | 2020-06-04 | 国家电投集团远达环保工程有限公司重庆科技分公司 | Desulfurization wastewater treatment system and desulfurization wastewater treatment method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| WO2020108135A1 (en) * | 2018-11-29 | 2020-06-04 | 国家电投集团远达环保工程有限公司重庆科技分公司 | Desulfurization wastewater treatment system and desulfurization wastewater treatment method |
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