CN205907052U - Evaporating treatment system of high salinity waste water - Google Patents
Evaporating treatment system of high salinity waste water Download PDFInfo
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- CN205907052U CN205907052U CN201620491338.6U CN201620491338U CN205907052U CN 205907052 U CN205907052 U CN 205907052U CN 201620491338 U CN201620491338 U CN 201620491338U CN 205907052 U CN205907052 U CN 205907052U
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- waste water
- high salinity
- evaporation
- water
- salinity waste
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Abstract
The utility model provides an evaporating treatment system of high salinity waste water, this system include steam generating device and evaporation plant, and evaporation plant's top is connected exhaust apparatus respectively and is sent the water installation, air supply plant and drainage device are connected respectively to evaporation plant's bottom, exhaust apparatus and air supply plant are linked together with steam generating device respectively, evaporation plant's top is provided with spray component, and spray component's below is provided with on -metal heat conduction evaporation tubulation. The utility model provides a mode of evaporating treatment system of high salinity waste water by heating water provides high -temperature steam, high -temperature steam evaporates tubulation department with high salinity waste water in on -metal heat conduction and carries out the heat exchange, realize the evaporating treatment of high salinity waste water, the evaporating treatment in -process can not produce the scale deposit, and during the high -temperature steam who does not form water in the steam that produces and the heat conduction evaporation tubulation emits into steam generating device through exhaust apparatus together, realize the recovery of heat energy, and then the rational utilization of realization heat energy, the small household multiple -effect heat pump system saves resources.
Description
Technical field
This utility model is related to technical field of waste water processing, more particularly, to a kind of evaporation process system of high salinity waste water
System.
Background technology
Waste water is the general name of the water and runoff rainwater discharged in life, and it includes sanitary sewage, industrial wastewater and first rain footpath
The useless water of other that stream enters, wherein, sanitary sewage and industrial wastewater occupy the overwhelming majority.At present, water resource lacks, waste water
In being applied to again live and produce after certain process, therefore, the process of waste water is also just particularly important.
With industrialized development, all can discharge a large amount of in chemical plant production, the collection course of processing of oil and natural gas
Industrial wastewater and also have other approach to produce industrial wastewaters, thus the water yield of industrial wastewater also increases year by year.High salinity is high
The waste water of fouling rate is one of industrial wastewater, and its total salinity at least accounts for the 1% of wastewater quality.High salinity high fouling rate
Waste component complicated, containing comprising cl-、so4 2-、na+、ca2+Etc. multiple salts substances, the species of Organic substance and chemical property
Differ greatly, solid suspension content is higher, hardness of water is larger.
Process for the waste water of high salinity high fouling rate is carried out typically by the way of moisture evaporation at present.Due to height
The waste water salinity of salinity high fouling rate compared with high, solid suspension content is high, hardness is big, existing wastewater treatment equipment is entering
During the wastewater treatment of row high salinity high fouling rate, easy fouling, what impact was evaporated is normally carried out.Wastewater treatment dress after fouling
Put and carry out again to consume substantial amounts of energy during wastewater treatment, and wastewater treatment equipment also needs to periodically carry out fouling process, work
Cheng Hao great, wastes huge manpower and material resources.
Utility model content
For overcoming problem present in correlation technique, this utility model provides a kind of evaporation process system of high salinity waste water
System.
The evaporation process system of the high salinity waste water that this utility model provides includes steam generation device and vaporising device,
Wherein, the top of described vaporising device connects exhaust apparatus and water sending device respectively；The bottom of described vaporising device connects respectively
Air supply plant and drainage arrangement；Described exhaust apparatus is connected with described steam generation device respectively with described air supply plant；Institute
The top stating vaporising device is provided with sprinkler part, and the lower section of described sprinkler part is provided with nonmetallic heat conduction evaporation tubulation.
Preferably, described steam generation device includes tank body and is arranged at the electromagnetic heater of described tank base.
Preferably, the bottom of described vaporising device arranges catcher and the water tank of parallel arranged；Described vaporising device also wraps
Include return duct, the two ends of described return duct are respectively communicated with described heat conduction evaporation tubulation and described water tank.
Preferably, the described heat conduction that tubulation is evaporated in described nonmetallic heat conduction and described water tank is graphite polypropylene material is steamed
Send out tubulation and described water tank.
Preferably, described exhaust apparatus includes pressure fan and exhaustor, and described pressure fan is respectively communicated with described evaporation
The top of device and one end of described exhaustor, and the other end of described exhaustor is located at the bottom within described steam generation device
End.
Preferably, described air supply plant includes blower fan and snorkel, and described blower fan is respectively communicated with the bottom of described vaporising device
Portion and one end of described snorkel, and the other end of described snorkel is connected with described steam generation device.
Preferably, described water sending device includes flow pipe and the dosing pump being arranged on described flow pipe, described flow pipe
Two ends connect described sprinkler part and wastewater disposal basin respectively.
Preferably, described drainage arrangement includes drain pipe and the water pump being arranged on described drain pipe, described drain pipe
Two ends connect water tank and the clear water reserviors of described vaporising device respectively.
Preferably, described water sending device also includes heat exchanger, and described flow pipe and described drain pipe are all by described heat exchange
Device, described heat exchanger is located between described dosing pump and described sprinkler part, and heat exchanger is located at described water pump and described clear water
Between pond.
Preferably, described heat exchanger is plate type heat exchanger.
The technical scheme that embodiment of the present utility model provides can include following beneficial effect:
The evaporation process system of the high salinity waste water that this utility model provides includes steam generation device and vaporising device,
Wherein, the top of described vaporising device connects exhaust apparatus and water sending device respectively；The bottom of described vaporising device connects respectively
Air supply plant and drainage arrangement；Described exhaust apparatus is connected with described steam generation device respectively with described air supply plant；Institute
The top stating vaporising device is provided with sprinkler part, and the lower section of described sprinkler part is provided with nonmetallic heat conduction evaporation tubulation.
The evaporation process system of the high salinity waste water that this utility model provides produces high-temperature steam by steam generation device, is produced
High-temperature steam pass through air supply plant by vaporising device bottom send into heat conduction evaporate tubulation in, high-temperature steam heat conduction evaporate row
From bottom to top run in pipe.There is high-temperature steam inside due to heat conduction evaporation tubulation, and therefore, heat conduction evaporation tubulation has very high
Temperature.After water sending device is opened, high salinity waste water is sprayed to heat conduction evaporation row by the sprinkler part at vaporising device top
Guan Shang, high salinity waste water touch high temperature heat conduction evaporation tubulation after be evaporated.Because heat conduction evaporation tubulation is nonmetallic
Material, thus the crystalline material such as salt being separated out in high salinity waste water evaporation process will not evaporate the surface of tubulation in heat conduction
Upper fouling, but fall into the bottom of vaporising device in the presence of self gravitation, further relate to providing using this utility model
The evaporation process system of high salinity waste water just do not interfering with high salinity waste water when carrying out high salinity wastewater treatment
Often process.In evaporation process, after high salinity waste water is contacted with the heat conduction evaporation tubulation of high temperature, due to heat exchange, heat conduction is steamed
Send out in tubulation and have water and formed, and steam in vaporising device, can be produced, the water being formed is discharged by drainage arrangement, produced
The high-temperature steam not forming water in steam and heat conduction evaporation tubulation then enters in steam generation device by exhaust apparatus together,
Realize the recovery of heat energy, and then realize the reasonable utilization of heat energy, economize on resources.
It should be appreciated that above general description and detailed description hereinafter are only exemplary and explanatory, not
This utility model can be limited.
Brief description
Accompanying drawing herein is merged in description and constitutes the part of this specification, show meet of the present utility model
Embodiment, and be used for explaining principle of the present utility model together with description.
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or in description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, for ordinary skill people
For member, without having to pay creative labor, other accompanying drawings can also be obtained according to these accompanying drawings.
The structure chart of the evaporation process system of the high salinity waste water that Fig. 1 provides for this utility model embodiment；
The evaporation process system of the high salinity waste water that Fig. 2 provides for this utility model embodiment processes the flow process of waste water
Figure；
Symbol represents: 1- steam generation device, 2- vaporising device, 3- exhaust apparatus, 4- water sending device, 5- air supply plant,
6- drainage arrangement, 7- sprinkler part, 8- heat conduction evaporation tubulation, 9- tank body, 10- electromagnetic heater, 11- catcher, 12- water tank,
13- return duct, 14- pressure fan, 15- exhaustor, 16- blower fan, 17- snorkel, 18- flow pipe, 19- dosing pump, 20- waste water
Pond, 21- drain pipe, 22- water pump, 23- clear water reserviors, 24- heat exchanger.
Specific embodiment
Here will in detail exemplary embodiment be illustrated, its example is illustrated in the accompanying drawings.Explained below is related to
During accompanying drawing, unless otherwise indicated, the same numbers in different accompanying drawings represent same or analogous key element.Following exemplary embodiment
Described in embodiment do not represent all embodiments consistent with this utility model.On the contrary, they be only with such as
The example of the consistent apparatus and method of some aspects being described in detail in appended claims, of the present utility model.
Refer to accompanying drawing 1, accompanying drawing 1 shows the evaporation process system of the high salinity waste water that this utility model embodiment provides
The structure chart of system.
The evaporation process system of the high salinity waste water that this utility model embodiment provides includes steam generation device 1 and steams
Transmitting apparatus 2, wherein, the top of described vaporising device 2 connects exhaust apparatus 3 and water sending device 4 respectively；Described vaporising device 2
Bottom connects air supply plant 5 and drainage arrangement 6 respectively；Described exhaust apparatus 3 and described air supply plant 5 are produced with described steam respectively
Generating apparatus 1 are connected；The top of described vaporising device 2 is provided with sprinkler part 7, and the lower section of described sprinkler part 7 is provided with non-
The heat conduction evaporation tubulation 8 of metal.
Specifically, the device that steam generation device 1 produces for high-temperature steam, steam generation device 1 specifically includes tank body 9 He
It is arranged at the electromagnetic heater 10 of tank body 9 bottom.Tank body 9 is used for holding the clear water producing high-temperature steam, as firing equipment
Electromagnetic heater 10 is arranged at the bottom of tank body 9, and electromagnetic heater 10 has up to more than 90% mechanical efficiency, can be fast
Speed ground provides temperature for tank body 9.
The device that vaporising device 2 evaporates for high salinity waste water.Vaporising device 2 is set to multistage cavity configuration altogether, makes evaporation
Device 2 in the vertical direction is divided into multiple chambers, and then completes the evaporation process of high salinity waste water.The top of vaporising device 2
It is provided with sprinkler part 7, sprinkler part 7 enters high salinity waste water in vaporising device 2 in the form of spraying, thus carrying out height
The evaporation process of salinity waste water.In the evaporation process system of the high salinity waste water that this utility model embodiment provides, spray
Drenching part 7 is shower or spray head, and the quantity of sprinkler part 7 can be according to spray area, spray ability of sprinkler part 7 etc.
It is designed and arrange.
Further, the bottom of vaporising device 2 is provided with catcher 11 and the water tank 12 of parallel arranged, and catcher 11 is used for receiving
The salt compounds of tubulation 8 surface crystallization are evaporated in collection heat conduction, and water tank 12 is used for collecting heat conduction evaporation tubulation 8 high temperature steam condensation
High temperature clear water afterwards.When catcher 11 collects a certain amount of salt compounds, catcher 11 is sent by evaporation dress by scraper plate
Put 2, and then realize the cleaning of salt compounds in catcher 11.Catcher 11 in setting, the push for ease of scraper plate and salt
The cleaning of class compound, catcher 11 is set to infundibulate.
Vaporising device 2 also includes return duct 13, and the two ends of return duct 13 are respectively communicated with heat conduction evaporation tubulation 8 and water tank 12,
Interface between return duct 13 and heat conduction evaporation tubulation 8 can evaporate the evaporability of tubulation 8 with heat conduction and spray flux be set in
In one of chamber of vaporising device 2, remaining high salinity can be given up with the heat conduction evaporation tubulation 8 realized under this chamber
Water evaporating completely, in the heat conduction evaporation tubulation 8 on this chamber, condensed high temperature clear water is back to water tank by return duct 13
In 12.
Tubulation 8 is evaporated in the nonmetallic heat conduction that is internally provided with of vaporising device 2, and heat conduction evaporation tubulation 8 is located at spray portion
The lower section of part 7.The part that tubulation 8 is hollow is evaporated in heat conduction, is filled with high-temperature steam, the evaporation process of waste water is just being led inside it
Carry out on thermal evaporation tubulation 8.Heat conduction evaporation tubulation 8 can be in vertical-type, flap type or the distribution of s type in vaporising device 2, heat conduction
The quantity of evaporation tubulation 8 is set according to the waste treatment capacity of the evaporation process system of high salinity waste water.Heat conduction is evaporated
When tubulation 8 is in that s type is distributed, heat conduction evaporation tubulation 8 is overall to tilt 5 ° to water tank 12 end, and this is due in the evaporation of high salinity waste water
In processing procedure, high-temperature steam evaporates, by heat conduction, the clear water that tubulation 8 tube wall can separate out high temperature, and the inclination of tubulation 8 is evaporated in heat conduction
High temperature clear water can be made smoothly to discharge vaporising device 2.When high temperature clear water discharges vaporising device 2, steam with heat conduction positioned at return duct 13
The heat conduction sending out the interface bottom of tubulation 8 is evaporated the high temperature clear water that separated out of tubulation 8 and is directly discharged into positioned at vaporising device 2 bottom
In water tank 12, the high temperature that the heat conduction evaporation tubulation 8 positioned at return duct 13 and the interface top of heat conduction evaporation tubulation 8 is separated out is clear
Water is back in water tank 12 by return duct 13, and the high temperature clear water being finally pooled in water tank 12 is expelled to by drainage arrangement 6
Clear water reserviors 23.High temperature clear water can also be squeezed in steam generation device 1, because high temperature is clear by connecting tube by clear water reserviors 23 again
Water has higher temperature, and therefore electromagnetic heater 10 can effectively reduce the consumption of electric energy when heating clear water, and then saves
The energy.
Further, due to high salinity waste water heat conduction evaporate tubulation 8 on be evaporated when, inorganic salt, solid suspend
Thing etc. all can form the solid matter of crystal class material or other forms, therefore, for preventing solid matter from evaporating tubulation 8 in heat conduction
Upper fouling, in the evaporation process system of the high salinity waste water that this utility model embodiment provides, heat conduction evaporation tubulation 8 is adopted
With non-metallic material it is preferable that heat conduction evaporation tubulation 8 adopts good heat conductivity, corrosion-resistant, resistance to oxidation and less scaling graphite
Polypropylene material, it is of course also possible to adopt the nonmetallic materials such as polyethylene, politef, every employing non-metallic material
Heat conduction evaporation tubulation 8 is all within protection domain of the present utility model.Meanwhile, evaporate the consumption of tubulation 8 for saving heat conduction, at this
In utility model, the wall thickness that tubulation 8 is evaporated in heat conduction is 0.1-0.2mm.Likewise, water tank 12 uses afterwards through long-time, water
The surface of case 12 also can fouling inorganic salts material, for extending using and preventing water tank 12 fouling of water tank 12, water tank 12 is also adopted
Evaporate the nonmetallic materials of tubulation 8 phase same material with same heat conduction.
Exhaust apparatus 3 is the device entering the excessive gas in vaporising device 2 in steam generation device 1.Exhaust apparatus 3
Including pressure fan 14 and exhaustor 15, pressure fan 14 is connected with the top of vaporising device 2, and pressure fan 14 is suppressing work
Together brought into the steam being formed when uncooled high-temperature steam in the lower evaporation tubulation 8 by heat conduction and the evaporation of high salinity waste water
In steam generation device 1, and then realize the maximum recovery of the recycling of vapourss, energy, it is equivalent to the 30 of multiple-effect evaporation
Effect.Pressure fan 14 is also connected with one end of exhaustor 15, and the other end of exhaustor 15 is located within steam generation device 1
Bottom.Preferably, the aerofluxuss open height of exhaustor 15 will be less than the liquid level of steam generation device 1, and such exhaustor 15 is discharged
Gas is issued to higher temperature in the heat effect of electromagnetic heater 10, and then is easy to high salinity waste water in vaporising device 2
Evaporation.
Air supply plant 5 is the device that the high-temperature steam producing steam generation device 1 sends into logical vaporising device 2.Supply gas dress
Put 5 and include blower fan 16 and snorkel 17, blower fan 16 is respectively communicated with the bottom of vaporising device 2 and one end of snorkel 17, and supplies gas
The other end of pipe 17 is connected with steam generation device 1 it is preferable that snorkel 17 is connected with the upper end of steam generation device 1,
And then steam generation device 1 can be made to hold more clear water, infrequently add clear water.Blower fan 16 passes through snorkel 17 by steam
Generator 1 plus thermogenetic high-temperature steam are sent in heat conduction evaporation tubulation 8.The high saliferous providing in this utility model embodiment
In the evaporation process system of amount waste water, blower fan 16 adopts other gas transportation facilitieses such as blower fan.
Water sending device 4 is the device that high salinity waste water is sent into vaporising device 2 from wastewater disposal basin 20.Water sending device 4 includes
Flow pipe 18 and the dosing pump 19 being arranged on flow pipe 18, the two ends of flow pipe 18 connect sprinkler part 7 and wastewater disposal basin respectively
20.Flow pipe 18 is used for conveying high salinity waste water in coupled wastewater disposal basin 20, and dosing pump 19 is used for calculating height and contains
The input quantity of salt amount waste water, spraying into the high salinity waste water in vaporising device 2 with realization by sprinkler part 7 can steam completely
Send out.
Drainage arrangement 6 is that the high temperature clear water evaporating heat conduction in evaporation process after tubulation 8 condenses enters from vaporising device 2
The device of clear water reserviors 23.Drainage arrangement 6 includes drain pipe 21 and the water pump 22 being arranged on drain pipe 21, the two ends of drain pipe 21
Connect water tank 12 and the clear water reserviors 23 of vaporising device 2 respectively.Drain pipe 21 is used for conveying the height in coupled water tank 12
Warm clear water, water pump 22 is used for extracting the high temperature clear water in water tank 12, and high temperature clear water is entered in clear water reserviors 23.In setting draining
During the connection of pipe 21 and water tank 12, drain pipe 21 can be directly connected it is also possible to be arranged on water tank with the least significant end of water tank 12
At 12 certain altitude, so that water tank 12 has certain water-holding capacity.
Further, in the evaporation process system of the high salinity waste water that this utility model embodiment provides, water sending device 4
Also include heat exchanger 24, flow pipe 18 and drain pipe 21 all pass through heat exchanger 24 in setting, and heat exchanger 24, when arranging, will change
Hot device 24 is arranged between dosing pump 19 and sprinkler part 7 and between water pump 22 and clear water reserviors 23, such set-up mode energy
The high salinity waste water flowing through dosing pump 19 is enough made to carry out heat exchange with the high temperature clear water flowing through water pump 22, thus spraying to entering
High salinity waste water before part 7 is preheated, and by the evaporation process system of energy recovery to high salinity waste water, this can
Reduce steam generation device 1 quantity of steam producing and the input quantity increasing high salinity waste water, and then improve high salinity and give up
The disposal ability of evaporation of water processing system, saves energy.Further, heat exchanger 24 adopts stainless plate type heat exchanger,
This is because plate type heat exchanger has larger heat transfer area, can accelerate the exchange of hot and cold water.
The evaporation process system of the high salinity waste water being provided according to this utility model embodiment, the processing method of this system
Refer to accompanying drawing 2.The processing method of the evaporation process system of high salinity waste water that this utility model embodiment provides includes:
S01: start the production model of steam generation device, produce high-temperature steam；
S02: the production model of described steam generation device is adjusted to mode of operation；
S03: open blower fan, so that high-temperature steam enters in heat conduction evaporation tubulation from the bottom of vaporising device；
S04: open exhaust apparatus, so that the high-temperature steam entering in heat conduction evaporation tubulation evaporates the top of tubulation from heat conduction
Enter in steam generation device；
S05: after described high-temperature steam circulation, open water sending device, so that waste water is ejected to by sprinkler part leading
It is evaporated on thermal evaporation tubulation；
S06: open drainage arrangement；
S07: in evaporation process, heat conduction is evaporated the clear water cooling down in tubulation and entered in clear water reserviors by drainage arrangement；
S08: the crystallization precipitate in evaporation process falls in the catcher of vaporising device bottom；
S09: in evaporation process, waste water is inhaled thermogenetic steam and entered in steam generation device by exhaust apparatus.
Specific processing procedure is described as:
S01: start the production model of steam generation device 1, produce high-temperature steam, wherein, production model be by electromagnetism plus
The power of hot device 10 reaches maximum, so that steam generation device 1 produces high-temperature steam within the time the shortest；
S02: when high-temperature steam produces a certain amount of, the production model of steam generation device 1 is adjusted to mode of operation, that is,
The power of electromagnetic heater 10 is turned down, and tank body 10 is carried out with lasting, stable heating；
S03: when high-temperature steam reaches a certain amount of, open blower fan 16 so that high-temperature steam from tank body 10 through pervaporation
The bottom of device 2 enters in heat conduction evaporation tubulation 8；
S04: open exhaust apparatus 3 in pressure fan 14 so that enter heat conduction evaporate tubulation 8 in high-temperature steam by under
And on run to heat conduction the top evaporating tubulation 8, and then enter the tank body 9 of steam generation device 1 from the top of vaporising device
In；
S05: after high-temperature steam circulation a few minutes, open the dosing pump 19 in water sending device 4 and heat exchanger 24, with
Make quantitative being delivered in sprinkler part 7 under the control of dosing pump 19 of high salinity waste water, and then by sprinkler part 7, height is contained
Salt amount waste water is ejected to and carries out heat exchange on heat conduction evaporation tubulation 8, completes the useless evaporation of water of high salinity, realizes high salinity and give up
Evaporation of water is processed；
S06: open the water pump 22 in drainage arrangement 6；
S07: in high salinity waste water evaporation process, heat conduction evaporates the high temperature clear water of condensation in tubulation 8 by drainage arrangement 6
Enter in clear water reserviors 23；
S08: the crystallization precipitate being separated out in high salinity waste water evaporation process falls into the catcher of vaporising device 2 bottom
In 11, and then crystallization precipitate is discharged vaporising device 2, realize the useless water purification of high salinity；
S09: produced by waste water heat absorption in high salinity waste water evaporation process, steam enters steam by exhaust apparatus 3 and produces
In generating apparatus 1, realize the recovery of high-temperature gas, the purpose that the gas that reaches a high temperature recycles；Heat conduction evaporation tubulation 8 carries out heat friendship
The high temperature clear water condensing gained after changing is discharged by water pump 22, and the high temperature clear water discharging water pump 22 is counted with passing through at heat exchanger 24
The high salinity waste water of amount pump 19 carries out heat exchange, realizes the recovery of heat energy.
Those skilled in the art are considering description and practice here after the disclosure of utility model, will readily occur to this practicality
New other embodiments.The application is intended to any modification of the present utility model, purposes or adaptations, these
Modification, purposes or adaptations are followed general principle of the present utility model and are included undocumented skill of this utility model
Common knowledge in art field or conventional techniques.Description and embodiments be considered only as exemplary, of the present utility model
True scope and spirit are pointed out by claim.
It should be appreciated that this utility model is not limited to be described above and accurate knot illustrated in the accompanying drawings
Structure, and various modifications and changes can carried out without departing from the scope.Scope of the present utility model only will by appended right
Ask to limit.
Claims (10)
1. a kind of evaporation process system of high salinity waste water is it is characterised in that described evaporation process system includes steam generation
Device (1) and vaporising device (2), wherein,
The top of described vaporising device (2) connects exhaust apparatus (3) and water sending device (4) respectively；
The bottom of described vaporising device (2) connects air supply plant (5) and drainage arrangement (6) respectively；
Described exhaust apparatus (3) is connected with described steam generation device (1) respectively with described air supply plant (5)；
The top of described vaporising device (2) is provided with sprinkler part (7), and the lower section of described sprinkler part (7) is provided with nonmetallic
Heat conduction evaporation tubulation (8).
2. the evaporation process system of high salinity waste water according to claim 1 is it is characterised in that described steam produces dress
Put (1) and include tank body (9) and the electromagnetic heater (10) being arranged at described tank body (9) bottom.
3. the evaporation process system of high salinity waste water according to claim 1 is it is characterised in that described vaporising device
(2) bottom arranges catcher (11) and the water tank (12) of parallel arranged；Described vaporising device (2) also includes return duct (13),
The two ends of described return duct (13) are respectively communicated with described heat conduction evaporation tubulation (8) and described water tank (12).
4. the evaporation process system of high salinity waste water according to claim 3 is it is characterised in that described nonmetallic leading
Tubulation (8) and described water tank are evaporated in thermal evaporation tubulation (8) and the described heat conduction that described water tank (12) is graphite polypropylene material
(12).
5. the evaporation process system of high salinity waste water according to claim 1 is it is characterised in that described exhaust apparatus
(3) pressure fan (14) and exhaustor (15) are included, described pressure fan (14) is respectively communicated with the top of described vaporising device (2)
With one end of described exhaustor (15), and the other end of described exhaustor (15) to be located at described steam generation device (1) internal
Bottom.
6. the evaporation process system of high salinity waste water according to claim 1 is it is characterised in that described air supply plant
(5) include blower fan (16) and snorkel (17), described blower fan (16) is respectively communicated with the bottom of described vaporising device (2) and described send
One end of trachea (17), and the other end of described snorkel (17) is connected with described steam generation device (1).
7. the evaporation process system of high salinity waste water according to claim 1 is it is characterised in that described water sending device
(4) flow pipe (18) and the dosing pump (19) being arranged on described flow pipe (18) are included, the two ends of described flow pipe (18) are divided
Do not connect described sprinkler part (7) and wastewater disposal basin (20).
8. the evaporation process system of high salinity waste water according to claim 7 is it is characterised in that described drainage arrangement
(6) drain pipe (21) and the water pump (22) being arranged on described drain pipe (21) are included, the two ends of described drain pipe (21) are respectively
Connect water tank (12) and the clear water reserviors (23) of described vaporising device (2).
9. the evaporation process system of high salinity waste water according to claim 8 is it is characterised in that described water sending device
(4) also include heat exchanger (24), described flow pipe (18) and described drain pipe (21), all by described heat exchanger (24), described change
Hot device (24) is located between described dosing pump (19) and described sprinkler part (7), and heat exchanger (24) is located at described water pump (22)
And described clear water reserviors (23) between.
10. the evaporation process system of high salinity waste water according to claim 9 is it is characterised in that described heat exchanger
(24) it is plate type heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620491338.6U CN205907052U (en) | 2016-05-26 | 2016-05-26 | Evaporating treatment system of high salinity waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620491338.6U CN205907052U (en) | 2016-05-26 | 2016-05-26 | Evaporating treatment system of high salinity waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205907052U true CN205907052U (en) | 2017-01-25 |
Family
ID=57815586
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620491338.6U Expired - Fee Related CN205907052U (en) | 2016-05-26 | 2016-05-26 | Evaporating treatment system of high salinity waste water |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105858764A (en) * | 2016-05-26 | 2016-08-17 | 北京科清环保科技有限公司 | Evaporating treatment system and treatment method for high-salinity waste water |
-
2016
- 2016-05-26 CN CN201620491338.6U patent/CN205907052U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105858764A (en) * | 2016-05-26 | 2016-08-17 | 北京科清环保科技有限公司 | Evaporating treatment system and treatment method for high-salinity waste water |
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