CN208087394U - Strong brine crystallization treatment device - Google Patents
Strong brine crystallization treatment device Download PDFInfo
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- CN208087394U CN208087394U CN201820174557.0U CN201820174557U CN208087394U CN 208087394 U CN208087394 U CN 208087394U CN 201820174557 U CN201820174557 U CN 201820174557U CN 208087394 U CN208087394 U CN 208087394U
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Abstract
The utility model provides a kind of strong brine crystallization treatment device.The strong brine crystallization treatment device includes pretreatment unit, GE evaporators, crystal system and centrifugal drying system, the pretreatment unit is connect with the GE evaporators, the crystal system is connect with the GE evaporators, and the centrifugal drying system is connect with the crystal system.A kind of strong brine crystallization treatment device provided by the utility model uses brine after-treatment device, it saves and utilizes vinyl chloride raw materials for production, vinyl chloride production will be put into after HCl treatment again, the salinity of haline water and other impurities are detached in solid form, sewage discharge is reduced, is reduced environmental pollution.
Description
Technical field
The utility model is related to chemical production equipment field more particularly to a kind of strong brine crystallization treatment devices.
Background technology
In course of production of chloroethylene, it may appear that a variety of excess raw materials or a variety of haline water intermediate products and waste water.It is existing
There is sewage-treatment plant to generally comprise biochemical treatment system, GE sewage deeps reclaiming system, GE evaporation process systems.Biochemical treatment
System mainly handles the waste water such as PVC treatment of wastewater from stripping, centrifuge mother liquor, sanitary sewage, sodium hypochlorite waste water, GE sewage deep reuses system
Waste water after system main processing loop water sewerage, desalted water concentrated water and biochemical treatment, GE vapo(u)rization systems mainly handle GE sewage
The haline water of depth reclaiming system is discharged into drying pond (also referred to as evaporation pond) after maximum minimizing.Sewage disposal
Device is relatively simple, has a single function, and cannot be recycled to excess raw material and intermediate product, and material recycle rate is low.
Utility model content
In order to solve the above technical problems, sewage-treatment plant work(in a kind of course of production of chloroethylene of the utility model offer
Can be various, excess raw material and intermediate product can be recycled, the high strong brine crystallization treatment of material recycle rate
Device.
Strong brine crystallization treatment device provided by the utility model include pretreatment unit, GE evaporators, crystal system and
Centrifugal drying system, the pretreatment unit are connect with the GE evaporators, the crystal system and the GE evaporators
Connection, the centrifugal drying system are connect with the crystal system；
The pretreatment unit includes front end water quality adjustment pond, water softening system, efficient sedimentation tank and PH regulating tanks, institute
It states water softening system to connect with front end water quality adjustment pond, the efficient sedimentation tank is connect with the water softening system, described
PH regulating tanks are connect with the efficient sedimentation tank；
The crystal system includes forced circulation heat exchanger, flash tank, dewaterer and condenser, the GE evaporators and institute
Flash tank connection is stated, the forced circulation heat exchanger connect with the flash tank, the dewaterer and the flash tank and described
Forced circulation heat exchanger connects, and the condenser is connect with the flash tank.
In a kind of preferred embodiment of strong brine crystallization treatment device provided by the utility model, the water softening system is
Caustic soda softens settler.
In a kind of preferred embodiment of strong brine crystallization treatment device provided by the utility model, the efficient sedimentation tank packet
Coagulation area, flocculation zone, sloping plate deposition district and sludge treatment equipment are included, the coagulation area is connect with the water softening system, described
Flocculation zone is connect with the coagulation area, and the sloping plate deposition district is connect with the flocculation zone, the sludge treatment equipment with it is described
Sloping plate deposition district connects.
In a kind of preferred embodiment of strong brine crystallization treatment device provided by the utility model, the sludge treatment equipment
It is set to including sludge-tank, sludge-tank blender, chamber-type press filter, sewage sludge feed pump and flush water pump, the sludge-tank blender
In the sludge-tank, the chamber-type press filter is connect with the sludge-tank, and the sewage sludge feed pump is set to the sludge-tank and institute
Between stating sloping plate deposition district, the flush water pump is connect with the chamber-type press filter.
In a kind of preferred embodiment of strong brine crystallization treatment device provided by the utility model, at the strong brine crystallization
It further includes sewage after-treatment device to manage device, and the sewage after-treatment device is connect with efficient sedimentation tank, the sewage post-processing
Device includes microbial biochemical reaction processing unit, reverse osmosis membrane processing device and vaporising device, the microbial biochemical reaction
Device is connect with the reverse osmosis membrane processing device, and the vaporising device is connect with the reverse osmosis membrane processing device.
The working principle and beneficial effect of the strong brine crystallization treatment device of the utility model：
Using brine after-treatment device, the salinity of haline water and other impurities are detached in solid form, reduce sewage row
It puts, reduces environmental pollution.
And the sewage after-treatment device is used, and after sewage disposal, the moisturizing for devices such as hydrochloric acid after-treatment devices
It is required that.The waste water for the concentrated water and VCM device neutralisation treatments that reverse osmosis membrane generates, into vapo(u)rization system, and is concentrated, and generate
Condensed water (also referred to as distilled water), the distilled water of generation can reuse to process water or boiler feedwater.
The strong brine and VCM waste water of existing evaporator, it is contemplated that the continuous-stable of follow-up mixed salt production, operation cost and
Situations such as design capacity of crystallizer, according to current practical water quality, into before existing evaporator, to reverse osmosis concentrated water and
VCM waste water does sofening treatment, and part hardness therein is removed, and crystallization treatment is done again to the strong brine come out from evaporator.It is former
Water through double alkali softening precipitations, not only can remove the temporary hardness in water, but also can remove the permanent hardness in water first.
Efficient sedimentation tank
Efficient sedimentation tank is collection coagulation, chemical method except hardness, sludge circulation, inclined plate (inclined tube) separation and sludge condensation etc.
It is a variety of theoretical in one, the mud-water separation developed by rational waterpower and structure design and sludge condensation functions it is heavy
Shallow lake technique.The special reaction zone of efficient sedimentation tank and settling section design make it be to substitute traditional coagulative precipitation tank, machinery clarification
The novel depositing technology in pond etc..Its operation principle is based on the following aspects：
The flocculation tank of integration in protonotion；
Pulling flow type reaction tank is to the transmission at a slow speed between sedimentation basin；
The external recirculation system of sludge；
Tube settling mechanism.
Efficient sedimentation tank technological principle is specific as follows：
High-rate sedimentation pool process completes body refuse, medicament, raw water in hybrid reaction area by the promotion immixture of blender
Quick aggregation, then through impeller be promoted to plug-flow reaction zone carry out flocculation reaction at a slow speed, to form larger floccule body.
Entire reaction zone (mixing and plug-flow reaction zone) can get a large amount of high density homogeneous alumen ustum, and this highdensity alumen ustum allows to sink
The settling velocity in shallow lake area is larger, without influencing effluent quality.
1) coagulation area
Lime, soda ash and coagulant dosage in raw water, under the action of flash mixer with raw water in suspended matter it is quick
Mixing, the negative electrical charge by neutralizing particle surface make particle " de- steady ", form small flco subsequently into flocculation basin.
2) flocculation zone
Flocculant promotes small flco by the flco of absorption, electrically neutralization and mutual bridging action formation bigger, slowly
The effect of fast blender had not only enable medicament and flco be sufficiently mixed but also will not destroy established big flocculating body.
3) tube settling district
Water outlet flows upward to upper-part centralized pool after entering settling zone after flocculation, and particle and flco are deposited on the surface of inclined tube
And it glides under the effect of gravity.60 ° of higher upflow velocity and inclined tube, which tilt, can form a continuous process scraped certainly, make wadding
Body will not be accumulated on inclined tube.
The sludge of precipitation slips down to bottom of pond along inclined tube, and sludge is concentrated in bottom of pond.Grizzly bar on mud scraper can improve
Sludge condensation effect, the mud scraper rotated at a slow speed continuously blow into sludge center collection mud pit.Thickened sludge is set according to certain
Determine program or controlled by mud level meter to reach the sludge concentration of an optimization, is then discontinuously discharged to Treatment of Sludge system
System.
Efficient sedimentation tank has the characteristics that：
A. highly dense and uniform alumen ustum；
B. the flocculation reaction optimized；
C. high settling rate, is precipitated using efficient inclined plate (inclined tube), and raw water is divided evenly in entire pond body；
D. the structure of highly compact, special flocculation reactor design, plug-flow transition is used from flocculation zone to settling zone；
E. perfect reflux control, settling zone to flocculation zone is by the way of controllable external sludge backflow and adds high score
Sub- flocculant, make flocculation formed even floccule and it is intensive, have very high sinking speed, therefore efficient sedimentation tank have processing
Construction investment and floor space is greatly saved in advantage efficient, unit area water yield is big；
F. sludge dewatering is not necessarily to pre-concentration, and sedimentation basin lower part is arranged larger enrichment region, makes the solid content of discharge sludge more
Height, without other sludge condensation facilities, is conducive to follow-up Treatment of Sludge up to 3%~5%；
G. remarkable effluent quality；
H. stable, load resistance and changes in flow rate impact.
Sludge treating system includes：Sludge-tank, sludge-tank blender, chamber-type press filter, sewage sludge feed pump, flush water pump etc.
It constitutes.The sludge that efficient sedimentation tank generates makes the water in sludge be discharged by filter cloth, to reach sludge by the extruding of sheet frame
The purpose of dehydration.Spoil disposal initially enters in sludge-tank, and being lifted into filter press through sewage sludge feed pump carries out press dewatering, sludge-tank
Inside it is provided with machine mixer.By the stirring action of impeller, the effects that reaching mixing, plug-flow, prevent sludge settling.
The filtrate of filter press is expelled to regulating reservoir, after dehydration mud cake by transported on trucks to factory outside.Plate and frame filter press operation one
The section time need to be rinsed filter cloth, and one to biweekly filter cloth is rinsed using high-pressure plunger pump, is removed and is blocked up on filter cloth
The sludge of plug.
Crystal system, main heat exchanger containing forced circulation, flash tank, dewaterer, the several units of condenser.By taking TVR as an example,
Crystallizer uses the steam drive of 0.4MPa (g), can adjust crystallization by adjusting the mode of crystallizer heat exchanger shell pass pressure
The evaporation efficiency of device, therefore this operating method provides larger adjusting elasticity.
In view of hardness is higher in raw water, salinity is complicated in water, therefore crystallizer uses forced circulation form.The pressure
Circulation crystallization device can be run under conditions of a variety of not syncrystallizations generate.And falling liquid film system can be in the condition for having crystal of calcium sulfate
Lower operation (since crystal of calcium sulfate kinetic reaction rate is relatively slow), but if there is other crystalline deposits, then system is very
It is fragile.
The design of forced circulation is very reliable, needs less cleaning than falling liquid film design.Forced circulation design for viscosity
The related problem such as increasing to suspended matter has good resistance, as water distribution unevenness, heat exchanger tube cannot be soaked fully and low be changed
Heating rate etc..
Applied to extra hydrochloric acid and by-product acid is removed during synthesizing polyvinyl chloride, the hydrogen chloride in hydrochloric acid is carried out most
Bigization desorption, and spent acid is not generated, hydrochloric acid depth desorption effect is good.The hydrochloric acid of concentration about 30%, with acid pump pressurization after with chlorination
After the one jet mixer mixing of the calcium chloride solution of calcium circulating pump conveying, into desorption tower, mixed solution is from stripping tower top
Portion enters, by the way that efficient mass transfer process occurs when filler and internals during flowing downward under gravity.Meanwhile it is molten
Liquid is constantly heated by thermal siphon Natural Circulation reboiler, and in this way, steam, which is distilled, isolates and flow up in this behaviour
During work, hydrogen chloride gas is stripped from hydrochloric acid and calcium chloride mixed solution and is discharged from tower top.Calcium chloride solution is conduct
Azeotropic breaks object, and the partial pressure of water vapour is inhibited for the partial pressure of hydrogen chloride gas.
The hydrogen chloride saturated acid vapour being stripped off obtains dry hydrogen chloride and send after B-grade condensation and demisting remove the acid mist of deentrainment
VCM is synthesized.And bottom of tower obtains dilute calcium chloride solution containing micro HCL, into calcium chloride flash concentration part.It is introduced into chlorine
Change calcium concentration tower, which is connected with thermal siphon natural-circulation evaporator.In this stage, excessive water is flashed
It is evaporated, it is collected into wastewater trough after water vapour fully condense by evaporated vapor condenser, returns to water scrubber, made
It is used for supplement absorbent (clear water).Calcium chloride solution after concentration recycles pumped back desorption tower with calcium chloride and recycles.
Description of the drawings
It is required in being described below to embodiment in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
Attached drawing to be used is briefly described, it should be apparent that, the accompanying drawings in the following description is only some realities of the utility model
Example is applied, it for those of ordinary skill in the art, without creative efforts, can also be according to these attached drawings
Other attached drawings are obtained, wherein：
Fig. 1 is the structural schematic diagram of one preferred embodiment of strong brine crystallization treatment device provided by the utility model.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describing, it is clear that described embodiment is only a part of the embodiment of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The all other embodiment obtained, shall fall within the protection scope of the present invention.
Referring to Fig. 1, the structure that Fig. 1 is one preferred embodiment of strong brine crystallization treatment device provided by the utility model is shown
It is intended to.
The strong brine crystallization treatment device includes pretreatment unit 31, GE evaporators 32, crystal system 33, centrifugal dehydration
Drying system 34 and sewage after-treatment device 4.The pretreatment unit 31 is connect with the GE evaporators 32, the crystal system
33 connect with the GE evaporators 32, and the centrifugal drying system 34 is connect with the crystal system 33.
The pretreatment unit 31 includes front end water quality adjustment pond 311, water softening system 312, efficient sedimentation tank 313 and PH
Regulating tank 314.The water softening system 312 is connect with front end water quality adjustment pond 311, the efficient sedimentation tank 313 with
The water softening system 312 connects, and the PH regulating tanks 314 are connect with the efficient sedimentation tank 313.After the sewage
Reason device 4 is connect with efficient sedimentation tank 313.
The water softening system 312 is that caustic soda softens settler.
The efficient sedimentation tank 313 includes coagulation area 51, flocculation zone 52, sloping plate deposition district 53 and sludge treatment equipment 54.
The coagulation area 51 is connect with the water softening system 312, and the flocculation zone 52 is connect with the coagulation area 51, and the inclined plate is heavy
Shallow lake area 53 is connect with the flocculation zone 52, and the sludge treatment equipment 54 is connect with the sloping plate deposition district 53.
The sludge treatment equipment 54 include sludge-tank 301, sludge-tank blender 302, chamber-type press filter 303, sludge into
Material pump 304 and flush water pump 305.The sludge-tank blender 302 is set in the sludge-tank 301, the chamber-type press filter
303 connect with the sludge-tank 301, and the sewage sludge feed pump 304 is set to the sludge-tank 301 and the sloping plate deposition district 333
Between, the flush water pump 305 is connect with the chamber-type press filter 303.
The crystal system 33 includes forced circulation heat exchanger 331, flash tank 332, dewaterer 333 and condenser 334.
The GE evaporators 32 are connect with the flash tank 332, and the forced circulation heat exchanger 331 is connect with the flash vessel 332, institute
It states dewaterer 333 to connect with the flash tank 33 and the forced circulation heat exchanger 331, the condenser 334 and the flash distillation
Tank 332 connects.
The sewage after-treatment device 4 include microbial biochemical reaction processing unit 41, reverse osmosis membrane processing device 42 and
Vaporising device 43.The microbial biochemical reaction device 41 is connect with the reverse osmosis membrane processing device 42, the vaporising device
43 connect with the reverse osmosis membrane processing device 43.
The working principle and beneficial effect of the strong brine crystallization treatment device of the utility model：
Using brine after-treatment device, the salinity of haline water and other impurities are detached in solid form, reduce sewage row
It puts, reduces environmental pollution.
And the sewage after-treatment device 4 is used, and after sewage disposal, the moisturizing for devices such as hydrochloric acid after-treatment devices
It is required that.The waste water for the concentrated water and VCM device neutralisation treatments that reverse osmosis membrane generates, into vapo(u)rization system, and is concentrated, and generate
Condensed water (also referred to as distilled water), the distilled water of generation can reuse to process water or boiler feedwater.
The strong brine and VCM waste water of existing evaporator, it is contemplated that the continuous-stable of follow-up mixed salt production, operation cost and
Situations such as design capacity of crystallizer, according to current practical water quality, into before existing evaporator, to reverse osmosis concentrated water and
VCM waste water does sofening treatment, and part hardness therein is removed, and crystallization treatment is done again to the strong brine come out from evaporator.It is former
Water through double alkali softening precipitations, not only can remove the temporary hardness in water, but also can remove the permanent hardness in water first.
Efficient sedimentation tank 313
Efficient sedimentation tank 313 is collection coagulation, chemical method except hardness, sludge circulation, inclined plate (inclined tube) separation and sludge condensation
It is theoretical in one etc. a variety of, the mud-water separation developed by rational waterpower and structure design and sludge condensation functions
Depositing technology.The special reaction zone of efficient sedimentation tank and settling section design make it be the traditional coagulative precipitation tank of replacement, are mechanical clear
The novel depositing technology in clear pond etc..Its operation principle is based on the following aspects：
The flocculation tank of integration in protonotion；
Pulling flow type reaction tank is to the transmission at a slow speed between sedimentation basin；
The external recirculation system of sludge；
Tube settling mechanism.
313 technological principle of efficient sedimentation tank is specific as follows：
313 technique of efficient sedimentation tank completes body refuse, medicament, original in hybrid reaction area by the promotion immixture of blender
Then the quick aggregation of water is promoted to plug-flow reaction zone through impeller and carries out flocculation reaction at a slow speed, to form larger flocculation
Body.Entire reaction zone (mixing and plug-flow reaction zone) can get a large amount of high density homogeneous alumen ustum, and this highdensity alumen ustum is permitted
Perhaps the settling velocity of settling zone is larger, without influencing effluent quality.
1) coagulation area 51
Lime, soda ash and coagulant dosage in raw water, under the action of flash mixer with raw water in suspended matter it is quick
Mixing, the negative electrical charge by neutralizing particle surface make particle " de- steady ", form small flco subsequently into flocculation basin.
2) flocculation zone 52
Flocculant promotes small flco by the flco of absorption, electrically neutralization and mutual bridging action formation bigger, slowly
The effect of fast blender had not only enable medicament and flco be sufficiently mixed but also will not destroy established big flocculating body.
3) tube settling district 53
Water outlet flows upward to upper-part centralized pool after entering settling zone after flocculation, and particle and flco are deposited on the surface of inclined tube
And it glides under the effect of gravity.60 ° of higher upflow velocity and inclined tube, which tilt, can form a continuous process scraped certainly, make wadding
Body will not be accumulated on inclined tube.
The sludge of precipitation slips down to bottom of pond along inclined tube, and sludge is concentrated in bottom of pond.Grizzly bar on mud scraper can improve
Sludge condensation effect, the mud scraper rotated at a slow speed continuously blow into sludge center collection mud pit.Thickened sludge is set according to certain
Determine program or controlled by mud level meter to reach the sludge concentration of an optimization, is then discontinuously discharged to Treatment of Sludge system
System.
Efficient sedimentation tank 313 has the characteristics that：
A. highly dense and uniform alumen ustum；
B. the flocculation reaction optimized；
C. high settling rate, is precipitated using efficient inclined plate (inclined tube), and raw water is divided evenly in entire pond body；
D. the structure of highly compact, special flocculation reactor design, plug-flow transition is used from flocculation zone to settling zone；
E. perfect reflux control, settling zone to flocculation zone is by the way of controllable external sludge backflow and adds high score
Sub- flocculant, make flocculation formed even floccule and it is intensive, have very high sinking speed, therefore efficient sedimentation tank have processing
Construction investment and floor space is greatly saved in advantage efficient, unit area water yield is big；
F. sludge dewatering is not necessarily to pre-concentration, and sedimentation basin lower part is arranged larger enrichment region, makes the solid content of discharge sludge more
Height, without other sludge condensation facilities, is conducive to follow-up Treatment of Sludge up to 3%~5%；
G. remarkable effluent quality；
H. stable, load resistance and changes in flow rate impact.
Sludge treating system includes：Sludge-tank 301, sludge-tank blender 302, chamber-type press filter 302, sewage sludge feed pump
303, the compositions such as flush water pump 305.The sludge that efficient sedimentation tank 313 generates makes the water in sludge pass through by the extruding of sheet frame
Filter cloth is discharged, to achieve the purpose that sludge dewatering.Spoil disposal initially enters in sludge-tank 304, is lifted into through sewage sludge feed pump
Chamber-type press filter 302 carries out press dewatering, and machine mixer 32 is provided in sludge-tank 301.By the stirring action of impeller, reach
To mixing, plug-flow, the effects that preventing sludge settling.
The filtrate of chamber-type press filter 302 is expelled to regulating reservoir, after dehydration mud cake by transported on trucks to factory outside.Plate and frame filter press
Operation a period of time need to be rinsed filter cloth, and one to biweekly filter cloth is rinsed using high-pressure plunger pump, and removal is filtered
The sludge blocked on cloth.
Crystal system 33, main heat exchanger containing forced circulation 331, flash tank 332, dewaterer 333, condenser 334 are several
Unit.By taking TVR as an example, crystallizer uses the steam drive of 0.4MPa (g), can be by adjusting crystallizer heat exchanger shell pass pressure
The mode of power adjusts the evaporation efficiency of crystallizer, therefore this operating method provides larger adjusting elasticity.
In view of hardness is higher in raw water, salinity is complicated in water, therefore crystallizer uses forced circulation form.The pressure
Circulation crystallization device can be run under conditions of a variety of not syncrystallizations generate.And falling liquid film system can be in the condition for having crystal of calcium sulfate
Lower operation (since crystal of calcium sulfate kinetic reaction rate is relatively slow), but if there is other crystalline deposits, then system is very
It is fragile.
The design of forced circulation is very reliable, needs less cleaning than falling liquid film design.Forced circulation design for viscosity
The related problem such as increasing to suspended matter has good resistance, as water distribution unevenness, heat exchanger tube cannot be soaked fully and low be changed
Heating rate etc..
Applied to extra hydrochloric acid and by-product acid is removed during synthesizing polyvinyl chloride, the hydrogen chloride in hydrochloric acid is carried out most
Bigization desorption, and spent acid is not generated, hydrochloric acid depth desorption effect is good.The hydrochloric acid of concentration about 30%, with acid pump pressurization after with chlorination
After the one jet mixer mixing of the calcium chloride solution of calcium circulating pump conveying, into desorption tower, mixed solution is from stripping tower top
Portion enters, by the way that efficient mass transfer process occurs when filler and internals during flowing downward under gravity.Meanwhile it is molten
Liquid is constantly heated by thermal siphon Natural Circulation reboiler, and in this way, steam, which is distilled, isolates and flow up in this behaviour
During work, hydrogen chloride gas is stripped from hydrochloric acid and calcium chloride mixed solution and is discharged from tower top.Calcium chloride solution is conduct
Azeotropic breaks object, and the partial pressure of water vapour is inhibited for the partial pressure of hydrogen chloride gas.
The hydrogen chloride saturated acid vapour being stripped off obtains dry hydrogen chloride and send after B-grade condensation and demisting remove the acid mist of deentrainment
VCM is synthesized.And bottom of tower obtains dilute calcium chloride solution containing micro HCL, into calcium chloride flash concentration part.It is introduced into chlorine
Change calcium concentration tower, which is connected with thermal siphon natural-circulation evaporator.In this stage, excessive water is flashed
It is evaporated, it is collected into wastewater trough after water vapour fully condense by evaporated vapor condenser, returns to water scrubber, made
It is used for supplement absorbent (clear water).Calcium chloride solution after concentration recycles pumped back desorption tower with calcium chloride and recycles.
The above description is only the embodiments of the present invention, and it does not limit the scope of the patent of the present invention, every
Equivalent structure or equivalent flow shift made based on the specification and figures of the utility model, is applied directly or indirectly in
Other relevant technical fields, are equally included in the patent within the scope of the utility model.
Claims (5)
1. a kind of strong brine crystallization treatment device, which is characterized in that including pretreatment unit, GE evaporators, crystal system and from
Heart dehydration drying system, the pretreatment unit are connect with the GE evaporators, and the crystal system connects with the GE evaporators
It connects, the centrifugal drying system is connect with the crystal system；
The pretreatment unit includes front end water quality adjustment pond, water softening system, efficient sedimentation tank and PH regulating tanks, the water
Melded system is connect with front end water quality adjustment pond, and the efficient sedimentation tank is connect with the water softening system, the PH tune
Water-saving box is connect with the efficient sedimentation tank；
The crystal system includes forced circulation heat exchanger, flash tank, dewaterer and condenser, the GE evaporators and the sudden strain of a muscle
Steaming pot connects, and the forced circulation heat exchanger is connect with the flash tank, the dewaterer and the flash tank and the pressure
Circulation heat exchanger connects, and the condenser is connect with the flash tank.
2. strong brine crystallization treatment device according to claim 1, which is characterized in that the water softening system is that caustic soda is soft
Change settler.
3. strong brine crystallization treatment device according to claim 1, which is characterized in that the efficient sedimentation tank includes coagulation
Area, flocculation zone, sloping plate deposition district and sludge treatment equipment, the coagulation area are connect with the water softening system, the flocculation zone
It is connect with the coagulation area, the sloping plate deposition district is connect with the flocculation zone, and the sludge treatment equipment is heavy with the inclined plate
Shallow lake area connects.
4. strong brine crystallization treatment device according to claim 3, which is characterized in that the sludge treatment equipment includes dirt
Mud sump, sludge-tank blender, chamber-type press filter, sewage sludge feed pump and flush water pump, the sludge-tank blender are set to the dirt
In mud sump, the chamber-type press filter is connect with the sludge-tank, and the sewage sludge feed pump is set to the sludge-tank and the inclined plate
Between settling zone, the flush water pump is connect with the chamber-type press filter.
5. strong brine crystallization treatment device according to claim 1, which is characterized in that the strong brine crystallization treatment device
Further include sewage after-treatment device, the sewage after-treatment device is connect with the efficient sedimentation tank, the sewage post-processing dress
It sets including microbial biochemical reaction processing unit, reverse osmosis membrane processing device and vaporising device, the microbial biochemical reaction dress
It sets and is connect with the reverse osmosis membrane processing device, the vaporising device is connect with the reverse osmosis membrane processing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820174557.0U CN208087394U (en) | 2018-02-01 | 2018-02-01 | Strong brine crystallization treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820174557.0U CN208087394U (en) | 2018-02-01 | 2018-02-01 | Strong brine crystallization treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208087394U true CN208087394U (en) | 2018-11-13 |
Family
ID=64063092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820174557.0U Active CN208087394U (en) | 2018-02-01 | 2018-02-01 | Strong brine crystallization treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208087394U (en) |
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2018
- 2018-02-01 CN CN201820174557.0U patent/CN208087394U/en active Active
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