CN207811299U - A kind of waste water treatment system, multichannel process system and multi-level handling system - Google Patents
A kind of waste water treatment system, multichannel process system and multi-level handling system Download PDFInfo
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- CN207811299U CN207811299U CN201721910892.4U CN201721910892U CN207811299U CN 207811299 U CN207811299 U CN 207811299U CN 201721910892 U CN201721910892 U CN 201721910892U CN 207811299 U CN207811299 U CN 207811299U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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Abstract
The utility model is related to a kind of waste water treatment system, multichannel process system and multi-level handling systems, including preevaporator, wind turbine, boiler furnace, slag well, ash gate, slag extractor, its core is the flue gas recirculation circuit of preevaporator, wind turbine and slag well by flue connection composition, specifically slag well is connect by low-voltage high-temperature flue with wind turbine, wind turbine is connect by high pressure-temperature flue with preevaporator, and preevaporator connect to form enclosed flue gas recirculation circuit with slag well by low-pressure low-temperature flue；The waterwater entrance of preevaporator is equipped with waste water water supply line, and wastewater outlet is connect with slag well by waste water Drainage pipe.The utility model makes full use of furnace bottom waste heat and afterheat of slags, waste water preheating, concentration, evaporation and crystallization treatment are realized by flue gas recirculation circuit, realize the utilization of wastewater treatment and afterheat of slags, reduce investment and the operating cost of wastewater treatment, and improve equipment dependability, it reduces furnace bottom simultaneously to leak out, improves boiler efficiency.
Description
Technical field
The utility model is related to a kind of waste water treatment system, multichannel process system and multi-level handling systems, belong to firepower hair
Electric technical field of waste water processing.
Background technology
The wastewater treatment of coal-fired station mainly has steam multiple-effect evaporation, membrane process+MVC/MVR evaporations+crystallization, cigarette
Road evaporation, membrane distillation (MD) technology etc..By taking the thermal power plant of 2 × 600MW grades as an example, power plant's about 20 tons of wastewater flow rate of production/when, such as
MVC evaporation/crystallization technologies are sprayed using U.S.'s horizontal film, gross investment is 60,000,000 yuan, about 12,000,000 yuan of annual operating cost.It is useless
Water treatment facilities investment is high, and operating cost is higher, increases the production cost of electric power enterprise.On the other hand, current waste water
Processing equipment failure rate is higher, and service life is shorter, and a set of membrane process+MVC/MVR evaporation equipments are usually run less than 4 years with regard to face
The problem of facing replacement membrane element, high expense make most of enterprise can't bear the heavy load.Cost for wastewater treatment how is reduced, and is carried
The reliability of high sewage treatment equipment is urgent need to solve the problem in industry.
On the other hand, the deslagging temperature of coal-fired power station boiler is generally up to 600 DEG C or more, this partial heat does not obtain profit
With, need additional low-temperature receiver instead and configure slag extractor come realize cooling.Air-cooled slag extractor must largely be passed through cold wind, this part
Cold wind enters boiler furnace during cooled slag, forms furnace bottom and leaks out, boiler efficiency is made to reduce about 0.5%.In the market
It is badly in need of a kind of new technology, afterheat of slags can be efficiently used, and reduces furnace bottom and leak out loss.
In view of the case where above-mentioned cost for wastewater treatment is high and afterheat of slags is unable to get utilization, existing wastewater treatment system
System has and handles waste water using afterheat of slags, such as the waste water treatment system that notification number is CN204897464U, is provided with and firepower
Waste water in waste water baffle-box, the warm sludge of slag well is sprayed onto by spray tube by the waste water baffle-box of power-plant waste outlet
On, it is intended that by warm sludge waste heat by waste water moisture evaporating completely, while reaching cooling warm sludge purpose.The simple system is practical, but
Being that there are problems is：1, the easy fouling of spray tube nozzle, blocking；2, boiler slag removal mouth heating surface high temperature salification corrosion is easily caused；3、
Processing waste water ability is limited, and wet slag problem is more serious.Since wastewater treatment process does not form cyclic process, only waste water is logical
It crosses spray tube and sprays to warm sludge, the waste heat by warm sludge is impossible to reach that evaporation is complete, leads to the aqueous height of clinker of output, is needed pair
Clinker is dehydrated, and is reprocessed to the waste water of abjection, cost higher.
The technical solution is clearly appreciated that waste water evaporating completely is difficult, therefore in order to keep the waste water energy for entering slag well real
Showing evaporating completely, be preferably provided with compressed air unit in the patent document is atomized the waste water that warm sludge is sprayed to from nozzle as possible, but
It is that atomization will produce a large amount of salt fog clouds for carrying corrosive ions and drop, boiler slag removal mouth high temperature salification is caused to corrode.
Utility model content
The utility model in view of the deficienciess of the prior art, provide a kind of waste water treatment system, multichannel process system and
Multi-level handling system realizes the circulating-heating to waste water using the formation flue gas recirculation circuit of furnace bottom waste heat, afterheat of slags,
Make waste water evaporation, crystallization, realize waste water low-cost processes, while avoid waste water influence clinker processing, reduce waste water, clinker and
Pollution to environment, while improving boiler efficiency.
The technical solution that the utility model solves above-mentioned technical problem is as follows：A kind of waste water treatment system, including prevapourising
Device, wind turbine, slag well and ash gate in slag bottom is set, the slag well is arranged in the bottom of boiler furnace, the ash gate
Lower section be equipped with slag extractor, the partial radiation heat in the boiler furnace is mainly passed to slag well in furnace bottom with radiation mode, referred to as
Furnace bottom waste heat；High temperature furnace slag drops on the ash gate of the slag bottom simultaneously, the preevaporator, slag well and wind turbine
Between by connecting flue form enclosed flue gas recirculation circuit, the connection flue includes for connecting the slag well and the wind
The low-voltage high-temperature flue of machine entrance, the high pressure-temperature cigarette for connecting the fan outlet and the smoke inlet of the preevaporator
Road, and exhanst gas outlet and the slag well for connecting preevaporator low-pressure low-temperature flue, the preevaporator is equipped with useless
Water inlet, the first wastewater outlet and the second wastewater outlet, the waterwater entrance are equipped with waste water water supply line, first waste water
Outlet is equipped with waste water Drainage pipe, and the bottom of the slag well is led in the outlet of the waste water Drainage pipe.
Boiler furnace generates furnace bottom waste heat and enters slag well, while high temperature furnace slag is fallen into slag well, furnace high-temperature flue gas and slag
Well communicates, and the ash gate of slag bottom is in normally off, maintains slag well temperature field to stablize, and prevent furnace bottom from leaking
Wind, core are that preevaporator, wind turbine and slag well connect to form flue gas recirculation circuit by flue, efficiently use furnace bottom waste heat with
Afterheat of slags realizes efficient concentration, the crystallization of waste water by the mixed heat transfer of flue gas and waste water.
The utility model has the beneficial effects that：Waste water enters preevaporator by waste water water supply line, by boiler furnace bottom
The high-temperature flue gas extracted out in the slag well in portion is sufficiently mixed heat exchange with it, temperature raising, up to boiling point, at this time a part of water vapour with
Flue gas is taken away, while low temperature wet flue gas is drained back to by preevaporator in slag well；In slag well, low temperature wet flue gas and the heat in slag well
Flue gas is mixed and is heated by radiation of burner hearth heat and clinker, and temperature increases, and forms high-temperature flue gas, high-temperature flue gas is then again introduced into pre-
In evaporator, the circulating-heating to waste water is realized.Above-mentioned flue gas recirculation process completes the preheating to waste water, concentration and part
Evaporation；Waste water becomes concentrate after preevaporator is handled, and a part of salt reaches crystallization dissolved click and starts to precipitate crystal,
It is contacted with high temperature furnace slag after being discharged into slag well, temperature further increases, and most of moisture evaporation is water vapour, and remainder crystallization is
Solid salt.The ash gate of slag bottom is in normally closed, regular deslagging state, keeps maintaining higher temperature in slag well, play simultaneously
The effect of slag extractor is isolated, maintains slag extractor reliability service.In short, the utility model passes through preevaporator, slag well, wind turbine and cigarette
Road, pipeline form flue gas recirculation circuit, make full use of furnace bottom waste heat and afterheat of slags, realize waste water preheating, concentration, evaporation and knot
Crystalline substance processing, while wastewater treatment and UTILIZATION OF VESIDUAL HEAT IN are realized, investment and the operating cost of wastewater treatment are reduced, and improve and set
Standby reliability, while reducing furnace bottom and leaking out, improve boiler efficiency.
Based on the above technical solution, the utility model can also do following improvement.
Further, it is equipped in the slag well and leads slag wall and the drainage region for installing drainage structure, the drainage region is set
It sets at the back for leading slag wall, the drainage structure includes that drain supervisor and multiple cloth liquid spoons, the cloth liquid spoon are distributed on institute
The bottom of drain supervisor is stated, the liquid outlet of the cloth liquid spoon leads to the ash gate, diversion trench, institute are equipped in the drain supervisor
State the outlet of the inlet and the waste water Drainage pipe of drain supervisor.
Advantageous effect using above-mentioned further scheme is that the cloth liquid spoon is carried out to entering the waste liquid in drain supervisor
Drainage, waste liquid is uniformly led on the ash gate of slag bottom, and for the bad working environments for adapting in slag well, drainage structure is set to row
In the drainage region of slag bottom above slag door, drainage region is arranged in the back of the body stream zone position for leading slag wall, prevent drainage structure by
The impact of high temperature furnace slag；The supervisor of drain simultaneously is sleeve structure, is internally provided with diversion trench, realizes that Waste water concentrating liquid uniformly drains to
On ash gate, and prevent drainage structure from blocking.It effectively prevent waste water crystallization process to form salt fog cloud and boiler heating surface is caused to send out
Raw salification corrosion, while it being effectively prevent drain blockage or damage, improve operational reliability.
Further, disturbance pipe network is equipped in the preevaporator, the disturbance pipe network includes multiple disturbance pipes, the height
Super pressure-high temperature flue is connect with the entrance of the disturbance pipe, and the exit of each disturbance pipe is equipped with nozzle.
Advantageous effect using above-mentioned further scheme is to be passed into high-temperature flue gas in waste water with air blast perturbation scheme,
Ensure that high-temperature flue gas is sufficiently mixed mass transfer heat exchange with waste water, waste water temperature is made to increase, until boiling point, effluent part evaporation, with cigarette
Gas emits.
The invention also discloses a kind of waste water multichannel process systems, including preevaporator, wind turbine, setting are in Boiler Furnace
The lower section of multiple slag wells of thorax bottom and the ash gate for being correspondingly arranged at each slag bottom, multiple ash gates is equipped with deslagging
Machine, the high temperature furnace slag in the boiler furnace drop on the ash gate of the slag bottom；The wind turbine, preevaporator and more
Form flue gas recirculation circuit by connecting flue between a slag well, the connection flue include for connect the fan outlet and
The high pressure-temperature flue of the smoke inlet of the preevaporator, the low pressure for connecting the fans entrance and multiple slag wells
High temperature flue collector and multiple low-voltage high-temperature by-pass flues and the exhanst gas outlet for connecting preevaporator and multiple slag wells
The waterwater entrance of low-pressure low-temperature flue collector and multiple low-pressure low-temperature by-pass flues, the preevaporator is equipped with waste water feed pipe
The waste liquid outlet in road, the preevaporator is connect by drain main line and multiple drain branch lines with multiple slag wells,
It is respectively equipped with control valve on the low-voltage high-temperature by-pass flue, low-pressure low-temperature by-pass flue and drain branch line.
The utility model has the beneficial effects that preevaporator can obtain a greater amount of high-temperature flue gas, high-temperature flue gas simultaneously
It after entering preevaporator, is sufficiently mixed with waste water, so that most of waste water is evaporated to vapor and return to slag well with flue gas, enter
Burner hearth is discharged；And the Waste water concentrating liquid in preevaporator after evaporation, concentration can then be discharged into each slag well or be discharged into any simultaneously
One slag well, makes concentrate be contacted with high temperature furnace slag, evaporates remaining moisture, and then crystallization is in solid, and is risen and fallen with clinker one
Enter in slag extractor, completes slag dumping.The utility model forms multichannel high-temperature flue, low temperature flue and waste water drain line, obtains more
More furnace bottom waste heats and afterheat of slags further increase the treatment effeciency of waste water；Multichannel flue, pipeline setting even wherein
One slag well servicing, will not influence the processing of waste water.
The invention also discloses a kind of waste water multi-level handling systems, including multistage wastewater treatment system as described above
Second wastewater outlet of system, prime is connected by waste water supercharging pipeline and the waterwater entrance of rear class, and the waste water increases
Pressure pipeline is pumped equipped with waste water supercharging；The first control valve and the second control are respectively equipped on every grade of the waste water Drainage pipe
Valve；The connecting line for the waste water Drainage pipe for leading to prime is additionally provided on the waste water Drainage pipe of rear class.Rear class
Connecting line and the first control valve and the second control valve of prime between waste water Drainage pipe connect.
The utility model has the beneficial effects that：Slag extractor is arranged in the lower section of the slag well of the multistage waste water treatment system.
The waste water treatment system waste water of the first order is increased by the second wastewater outlet of first order preevaporator by waste water after being concentrated by evaporation
Press pump, waste water supercharging pipeline enter the preevaporator of the second level, and the Waste water concentrating liquid into the second level mixes again with high-temperature flue gas
It closes, further evaporation, concentration；3rd level preevaporator, the 4th grade of preevaporator are entered back into later until n-th grade of preevaporator, are made
Waste water is constantly evaporated, is concentrated, and most of moisture is changed into water vapour, and slag well is returned to via low-pressure low-temperature pipeline with flue gas.Concentration
Wastewater liquid afterwards is discharged into slag well, is contacted with high temperature furnace slag, while by radiation of burner hearth heat effect, and remaining moisture content is all evaporated to
Water vapour, waste water crystallization concentrate, which is then mixed with clinker, generates solid salt, and slag extractor is fallen into through ash gate, finally complete by slag extractor
At slag dumping.Multiple-stage watewater disposal system is sequentially connected in series arrangement by the utility model, and rear class waste water treatment system evaporates prime dense
Waste water concentrating liquid after contracting is further concentrated by evaporation, and waste water is more complete by multistep treatment evaporation, avoids the place for influencing clinker
Reason reduces the pollution of waste water, clinker to environment.
Description of the drawings
Fig. 1 is the schematic diagram of the waste water treatment system of the utility model；
Fig. 2 is the structural schematic diagram of the waste water treatment system of the utility model；
Fig. 3 is the slag well drainage structure layout structure schematic diagram of the utility model；
Fig. 4 is the structural schematic diagram of the waste water multichannel process system of the utility model；
Fig. 5 is the structural schematic diagram of the waste water multi-level handling system of the utility model；
In figure, 1, wind turbine；2, preevaporator；3, boiler furnace；4, slag well；5, ash gate；6, slag extractor；7, control valve
Door；8, the first control valve；9, the second control valve；10, slag wall is led；11, drainage region；12, drain is responsible for；13, drain is in charge of；14、
Diversion trench；15, crystal salt；G1, low-voltage high-temperature flue；G2, high pressure-temperature flue；G3, low-pressure low-temperature flue；G4, waste water supply water
Pipeline；G5, waste water Drainage pipe；G6, waste water supercharging pipeline；P1, waste water supercharging pump；G9, low-voltage high-temperature flue collector；G10, low pressure
High temperature branch flue；G11, drain main line；G12, drain branch line；G13, low-pressure low-temperature flue collector；G14, low-pressure low-temperature
By-pass flue；G15, connecting line.
Specific implementation mode
The principles of the present invention and feature are described below in conjunction with example, example is served only for explaining this practicality
It is novel, it is not intended to limit the scope of the utility model.
As shown in Figure 1-Figure 3, a kind of waste water treatment system, including preevaporator 2, wind turbine 1, slag well 4 and setting are in slag well
The ash gate 5 of bottom, the slag well are arranged in the bottom of boiler furnace, and the lower section of the ash gate is equipped with slag extractor 6, the pot
The furnace bottom waste heat of stove enters slag well, while high temperature furnace slag drops on the ash gate of the slag bottom, the prevapourising
Flue gas recirculation circuit is formed by connecting flue between device, slag well and wind turbine, the connection flue includes for connecting the slag
Low-voltage high-temperature flue G1, the smoke inlet for connecting the fan outlet and the preevaporator of well and the fans entrance
High pressure-temperature flue G2 and low-pressure low-temperature flue G3 for connecting the exhanst gas outlet of preevaporator and the slag well, it is described pre-
Evaporator is equipped with waterwater entrance, the first wastewater outlet and the second wastewater outlet, and the waterwater entrance is equipped with waste water feed pipe
Road G4, first wastewater outlet are equipped with waste water Drainage pipe G5, and the slag well is led in the outlet of the waste water Drainage pipe
Bottom.
It is equipped in the slag well and leads slag wall 10 and the drainage region 11 for installing drainage structure, the drainage region is arranged in institute
The back for leading slag wall is stated, the drainage structure includes that drain supervisor 12 and multiple cloth liquid spoons, the cloth liquid spoon are distributed on the row
The liquid outlet of the bottom of liquid supervisor, the cloth liquid spoon leads to the ash gate, and diversion trench 14 is equipped in the drain supervisor, described
The outlet of the inlet and the waste water Drainage pipe of drain supervisor.For the bad working environments for adapting in slag well, drainage structure
It is set in the drainage region of the slag bottom above ash gate, drainage region is arranged in the back of the body stream zone position for leading slag wall, prevents drain
Structure is impacted by high temperature furnace slag；The supervisor of drain simultaneously is sleeve structure, is internally provided with diversion trench, realizes that Waste water concentrating liquid is equal
It is even to drain on ash gate, and prevent drainage structure from blocking.It effectively prevent waste water crystallization process to form salt fog cloud and cause boiler
Salification corrosion occurs for heating surface, while effectivelying prevent drain blockage or damage, improves operational reliability.
Disturbance pipe network is equipped in the preevaporator, the disturbance pipe network includes multiple disturbance pipes, the high pressure-temperature cigarette
Road is connect with the entrance of the disturbance pipe, and the exit of each disturbance pipe is equipped with nozzle.High-temperature flue gas is disturbed with air blast
Mode is passed into waste water, ensures that high-temperature flue gas is sufficiently mixed heat exchange with waste water, waste water temperature is made to increase, until boiling point, part
Moisture evaporation is gone out with flue gas emission.
Boiler generates furnace bottom waste heat, high temperature furnace slag enters, falls into slag well, while high-temperature flue gas is communicated with slag well,
Waste water enters preevaporator, the high temperature cigarette extracted out by the left side of the slag well of boiler furnace bottom in Fig. 1 by waste water water supply line
Gas enters low-voltage high-temperature flue, and enters high pressure-temperature flue after wind turbine pressurizes, and is then sprayed by high pressure-temperature flue
In preevaporator；In preevaporator, high-temperature flue gas is sufficiently mixed with waste water, and waste water temperature is made to increase, until boiling point, at this time one
Part water vapour returns to slag well with flue gas, and into burner hearth, while low temperature wet flue gas is drained back to by preevaporator in slag well, by slag well
Right side enter slag well；In slag well, low temperature wet flue gas mixes with the heat smoke in slag well and by radiation of burner hearth heat and clinker
Heating, temperature increase, and form high-temperature flue gas, and high-temperature flue gas is then again introduced into preevaporator, realize the circulating-heating to waste water.
Waste water becomes concentrate after preevaporator is handled, and is discharged on the ash gate in the slag well of boiler furnace bottom, with high temperature
Clinker contacts, and temperature further increases, and most of moisture evaporation is water vapour, and remainder crystallization is solid salt, concentrating spent liquor
It is directed directly on ash gate, salt fog cloud will not be formed, avoid that boiler slag removal mouth is caused to be corroded.The ash gate of slag bottom is in
Normally closed, regular deslagging state keeps maintaining higher temperature in slag well, while playing the role of that slag extractor is isolated, and maintains slag extractor
Reliability service.
As shown in figure 4, a kind of waste water multichannel process system, including preevaporator 2, wind turbine 1, setting are in boiler furnace bottom
Multiple slag wells 4 and be correspondingly arranged at the ash gate 5 of each slag bottom, the lower section of multiple ash gates is equipped with slag extractor 6,
High temperature furnace slag in the boiler furnace drops on the ash gate of the slag bottom；The wind turbine, preevaporator and multiple
Flue gas recirculation circuit is formed by connecting flue between slag well, the connection flue includes for connecting the fan outlet and institute
The high pressure-temperature flue G2 that states the smoke inlet of preevaporator, the low pressure for connecting the fans entrance and multiple slag wells
High temperature flue collector G9 and multiple low-voltage high-temperature by-pass flue G10 and the exhanst gas outlet for connecting preevaporator and multiple slags
The low-pressure low-temperature flue collector G13 of well and multiple low-pressure low-temperature by-pass flue G14, the waterwater entrance of the preevaporator, which is equipped with, to give up
Water water supply line G4, the waste liquid outlet of the preevaporator by drain main line G11 and multiple drain branch line G12 with it is more
A slag well connects, and is respectively equipped on the low-voltage high-temperature by-pass flue, low-pressure low-temperature by-pass flue and drain branch line
Control valve 7.
Boiler furnace bottom shown in Fig. 4 is provided with 3 slag wells, and preevaporator can obtain a greater amount of high temperature cigarettes simultaneously
Gas after high-temperature flue gas enters evaporator, is sufficiently mixed with waste water, and most of waste water is made to be evaporated to vapor and be returned with flue gas
Slag well is discharged into burner hearth；And preevaporator in evaporation, concentration after Waste water concentrating liquid can then be discharged into simultaneously each slag well or
It is discharged into any one slag well, concentrate is contacted with high temperature furnace slag in slag well, evaporates remaining moisture, and then crystallization is in solid,
And fallen into slag extractor together with clinker, complete slag dumping.Multiple slag wells are set under boiler, and the bottom setting of boiler is corresponding with slag well
Ash gate, if one of slag well is problematic, other slag wells can still work normally, and be completed using waste heat by other slag wells useless
Water process.
As shown in figure 5, the invention also discloses a kind of waste water multi-level handling system, including it is multistage as described above useless
Second wastewater outlet of water treatment system, prime is connected by waste water supercharging pipeline G6 and the waterwater entrance of rear class,
The waste water supercharging pipeline is equipped with waste water supercharging and pumps P1；It is respectively equipped with the first control valve on every grade of the waste water Drainage pipe
7 and second control valve 8；The company for the waste water Drainage pipe for leading to prime is additionally provided on the waste water Drainage pipe of rear class
Take over road G15.On waste water Drainage pipe between the connecting line of rear class and the first control valve of prime and the second control valve.Afterwards
Grade waste water drain line can enter under the action of this grade of control valve in corresponding slag well, or enter prime by connecting line
In slag well.
4 grades of waste water treatment systems are set in Fig. 5, turns left from the right side and is followed successively by the 1st grade of waste water treatment system, from the 2nd grade of waste water
Reason system, 3rd level waste water treatment system and the 4th grade of waste water treatment system, after the 1st grade of waste water treatment system waste water is concentrated by evaporation
Enter by waste water supercharging pump, waste water supercharging pipeline the 2nd grade of preevaporator by the 2nd wastewater outlet of the 1st grade of preevaporator,
It is mixed again with high-temperature flue gas into the 2nd grade of Waste water concentrating liquid, further evaporation, concentration；3rd level prevapourising is entered back into later
Device, the 4th grade of preevaporator, make waste water constantly evaporate, concentrate, most of moisture is changed into water vapour, low via low pressure with flue gas
Warm pipeline returns to slag well.Wastewater liquid after concentration is discharged into slag well, is contacted with high temperature furnace slag, while being made by radiation of burner hearth heat
With remaining moisture content is all evaporated to water vapour, and the solid salt that waste water crystallization generates then is mixed with clinker, and deslagging is fallen into through ash gate
Machine finally completes slag dumping by slag extractor.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all in this practicality
Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model
Within the scope of shield.
Claims (5)
1. a kind of waste water treatment system, which is characterized in that including preevaporator, wind turbine, slag well and row in slag bottom is arranged
Slag door, the slag well are arranged in the bottom of boiler furnace, and the lower section of the ash gate is equipped with slag extractor, the preevaporator, slag
Flue gas recirculation circuit is formed by connecting flue between well and wind turbine, the connection flue includes for connecting the slag well and institute
Low-voltage high-temperature flue, the high pressure height for connecting the fan outlet with the smoke inlet of the preevaporator for stating fans entrance
The low-pressure low-temperature flue of warm flue and exhanst gas outlet and the slag well for connecting preevaporator, the preevaporator are equipped with
Waterwater entrance, the first wastewater outlet and the second wastewater outlet, the waterwater entrance are equipped with waste water water supply line, and described first is useless
Water out is equipped with waste water Drainage pipe, and the bottom of the slag well is led in the outlet of the waste water Drainage pipe.
2. waste water treatment system according to claim 1, which is characterized in that be equipped in the slag well and lead slag wall and for pacifying
The drainage region of drainage structure is filled, the drainage region is arranged at the back for leading slag wall, and the drainage structure includes drain supervisor
And multiple cloth liquid spoons, the cloth liquid spoon are distributed on the bottom of the drain supervisor, liquid outlet leads to the ash gate, the row
Diversion trench, the outlet of the inlet and the waste water Drainage pipe of the drain supervisor are equipped in liquid supervisor.
3. waste water treatment system according to claim 1 or 2, which is characterized in that be equipped with disturbance pipe in the preevaporator
Net, the disturbance pipe network include multiple disturbance pipes, and the high pressure-temperature flue is connect with the entrance of the disturbance pipe, each described
The exit for disturbing pipe is equipped with nozzle.
4. a kind of waste water multichannel process system, which is characterized in that including preevaporator, wind turbine, be arranged in boiler furnace bottom
The lower section of multiple slag wells and the ash gate for being correspondingly arranged at each slag bottom, multiple ash gates is equipped with slag extractor；It is described
Flue gas recirculation circuit is formed by connecting flue between wind turbine, preevaporator and multiple slag wells, the connection flue includes being used for
Connect the fan outlet with the high pressure-temperature flue of the smoke inlet of the preevaporator, for connect the fans entrance with
The low-voltage high-temperature flue collector and multiple low-voltage high-temperature by-pass flues of multiple slag wells, and flue gas for connecting preevaporator go out
Low-pressure low-temperature flue collector and multiple low-pressure low-temperature by-pass flue of the mouth with multiple slag wells, the waterwater entrance of the preevaporator
Be equipped with waste water water supply line, the waste liquid outlet of the preevaporator by drain main line and multiple drain branch lines with it is more
A slag well connects, and is respectively equipped on the low-voltage high-temperature by-pass flue, low-pressure low-temperature by-pass flue and drain branch line
Control valve.
5. a kind of waste water multi-level handling system, which is characterized in that at multistage waste water as described in any one of claims 1-3
Second wastewater outlet of reason system, prime is connected by waste water supercharging pipeline and the waterwater entrance of rear class, described useless
Water pressure pipeline is pumped equipped with waste water supercharging；The first control valve and the second control are respectively equipped on every grade of the waste water Drainage pipe
Valve processed；The connecting line for the waste water Drainage pipe for leading to prime is additionally provided on the waste water Drainage pipe of rear class.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721910892.4U CN207811299U (en) | 2017-12-30 | 2017-12-30 | A kind of waste water treatment system, multichannel process system and multi-level handling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721910892.4U CN207811299U (en) | 2017-12-30 | 2017-12-30 | A kind of waste water treatment system, multichannel process system and multi-level handling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207811299U true CN207811299U (en) | 2018-09-04 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201721910892.4U Active CN207811299U (en) | 2017-12-30 | 2017-12-30 | A kind of waste water treatment system, multichannel process system and multi-level handling system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107973357A (en) * | 2017-12-30 | 2018-05-01 | 刘春晓 | A kind of waste water treatment system, multichannel process system and multi-level handling system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107973357A (en) * | 2017-12-30 | 2018-05-01 | 刘春晓 | A kind of waste water treatment system, multichannel process system and multi-level handling system |
| CN107973357B (en) * | 2017-12-30 | 2024-08-20 | 京能（锡林郭勒）发电有限公司 | Wastewater treatment system, multi-path treatment system and multi-stage treatment system |
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