CN109626681A - A kind of desalination plant - Google Patents
A kind of desalination plant Download PDFInfo
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- CN109626681A CN109626681A CN201811567904.7A CN201811567904A CN109626681A CN 109626681 A CN109626681 A CN 109626681A CN 201811567904 A CN201811567904 A CN 201811567904A CN 109626681 A CN109626681 A CN 109626681A
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- atomization
- water
- chamber
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- removal
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- 238000010612 desalination reaction Methods 0.000 title claims abstract description 19
- 238000009833 condensation Methods 0.000 claims abstract description 48
- 230000005494 condensation Effects 0.000 claims abstract description 48
- 238000000889 atomisation Methods 0.000 claims abstract description 46
- 239000012535 impurity Substances 0.000 claims abstract description 35
- 238000001914 filtration Methods 0.000 claims abstract description 32
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 23
- 230000001954 sterilising effect Effects 0.000 claims abstract description 21
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 21
- 239000013535 sea water Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 74
- 239000006260 foam Substances 0.000 claims description 39
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 29
- 238000001179 sorption measurement Methods 0.000 claims description 25
- 239000002689 soil Substances 0.000 claims description 17
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 15
- 239000001569 carbon dioxide Substances 0.000 claims description 15
- 239000007921 spray Substances 0.000 claims description 14
- 239000000919 ceramic Substances 0.000 claims description 12
- 238000009298 carbon filtering Methods 0.000 claims description 9
- 239000013505 freshwater Substances 0.000 claims description 8
- 230000010355 oscillation Effects 0.000 claims description 7
- 238000005096 rolling process Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 6
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 230000000052 comparative effect Effects 0.000 description 8
- 238000002309 gasification Methods 0.000 description 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 229960000892 attapulgite Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005562 fading Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052625 palygorskite Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Physical Water Treatments (AREA)
Abstract
The present invention relates to a kind of desalination plants, including trash chamber, atomization condensation chamber and filtration sterilization room.By the way that the trash chamber of specific structure is arranged, the seawater before condensation is subjected to preposition removal of impurities and removes dirty matter in advance, avoids the fouling in equipment when subsequent atomization condenses.By way of being first atomized seawater and then condensing again, the effect of condensation is substantially increased.
Description
Technical field
The invention belongs to hydraulic engineerings and field of seawater desalination, and in particular to a kind of desalination plant.
Background technique
For the desalination technology of seawater, at present there are many kinds of, wherein the seawater after condensation gasification is more early concerned
Technology.The advantages of this technology, is that fading effect is preferable, the disadvantage is that relatively inefficient and unit cost is higher, meanwhile, by
It after needing that first seawater gasifies and then is condensing, the impurity in seawater can be attached on part of appliance, and component is caused to damage
It is bad, and since, containing the calcareous of some, carrying out condensation for a long time after ingress of air will form scale in seawater, it will also result in
The damage of part of appliance.
Summary of the invention
In view of the above technical problems, the present invention proposes a kind of desalination plant.
It is realized by following technological means:
A kind of desalination plant, including trash chamber, atomization condensation chamber and filtration sterilization room.
The trash chamber includes removal of impurities chamber enclosure, seawater inlet, rotary jet disk, air-jeting disk air intake, rolling bearing, enters
Feed channel, air pump, carbon dioxide storage room, driving motor, high pressure spray gas nozzle, foam outlet, foam handle pipe portion part, return water
Mouth, screen and trash chamber water outlet；The interior bottom of removal of impurities chamber enclosure is arranged in the rotary jet disk, and the rotary jet disk is
Hollow discoid and its outer wall is the through-hole structure that gathers, and rotary jet pan bottom center is provided with air-jeting disk air intake, institute
It states air-jeting disk air intake to be rotatablely connected by the bottom wall of the rolling bearing and the removal of impurities chamber enclosure, the driving motor driving
The outside of removal of impurities chamber enclosure, and its is arranged in the air-jeting disk air intake and rotary jet disk rotation, the gas feeding pipe
One end is connected to the air-jeting disk air intake, and the other end is connected to the carbon dioxide storage room, is arranged on the gas feeding pipe
There is the air pump for being pressurized to gas in gas feeding pipe；Rotary jet disk top is provided with the screen, the screen
All side walls for being horizontally installed on the outer wall and removal of impurities chamber enclosure of trash chamber interior of shell and the screen are affixed, and the screen is set
It is equipped with densely covered upper lower through-hole, is provided with seawater inlet on the side wall of the removal of impurities chamber enclosure between rotary jet disk and screen,
Trash chamber water outlet is provided on the side wall of the removal of impurities chamber enclosure on the screen top；Removal of impurities chamber enclosure one side wall it is upper
Portion is provided with high pressure spray gas nozzle, is provided with foam outlet on the side wall of the removal of impurities chamber enclosure opposite with the high pressure spray gas nozzle,
The water return outlet is provided on the side wall of the removal of impurities chamber enclosure of the foam outlet lower part, the foam processing pipe portion part includes
Foam handles pipe, foamed filter plate, sundries storage bin and gas vent, and the foam processing tube top portion and the foam outlet connect
Logical, bottom is connected to the water return outlet, one or more foamed filter plates is internally provided in foam processing pipe, at one
Or it is provided with sundries storage bin on multiple foamed filter board terminals, foam processing tube top portion is provided with gas vent.
The atomization condensation chamber include atomization condensation chamber enclosure, ceramic atomizing piece, ultrasonic atomization high frequency oscillation generator,
It is atomized condensation chamber water inlet, condenser pipe, hot air outlet, hot wind pump and water condensate storage room；The atomization condensation chamber water inlet
The lower part of the side wall of atomization condensation chamber enclosure is set and is connected to the trash chamber water outlet, the ceramics atomizing piece is provided with
Horizontal plane multiple and that atomization condensation chamber is arranged in is hereinafter, multiple ceramic atomizing pieces are laterally arranged and are being atomized with setting
The ultrasonic atomization high frequency oscillation generator of condensation chamber shell exterior is electrically connected, atomization condensation chamber above the horizontal plane
It is provided with hot air outlet on the side wall of atomization condensation chamber enclosure, hot wind pump, the hot wind are provided with outside hot air outlet
Pump by the hot air outlet to be atomized condensation chamber inside hot wind is provided；In the topmost setting of atomization condensation chamber interior of shell
There are more condenser pipes, water condensate storage room is provided at the terminal of the more condenser pipes, the water condensate storage room is used for
The condensed water that the more condenser pipes are collected into temporarily is stored, the bottom of the water condensate storage room is provided with condensation
Water water outlet.
The filtration sterilization room includes filtration sterilization room water inlet, concavo-convex rod soil filtering adsorption plate, active carbon filtering absorption
Plate, ultraviolet sterilizer and freshwater storage case；Filtration sterilization room water inlet be arranged in the top of the filtration sterilization room and with
The condensed water water outlet connection, is provided with lateral concavo-convex rod soil in filtration sterilization room water inlet lower part and filters adsorption plate, institute
Stating concavo-convex rod soil filtering adsorption plate is to be clamped with concavo-convex rod soil particle among the densely covered ventilating hole plate of upper layer and lower layer；In the concavo-convex rod soil
Filtering adsorption plate lower part is provided with lateral active carbon filtering adsorption plate, and the active carbon filtering adsorption plate gathers for upper layer and lower layer
Active carbon particle is clamped among ventilating hole plate；Active carbon filtering adsorption plate lower part is provided with ultraviolet sterilizer, described ultraviolet
Sterilizer lower part is provided with freshwater storage case.
Preferably, the height and position of the carbon dioxide storage room is higher than the roof of the removal of impurities chamber enclosure.
Preferably, the driving motor drives the air-jeting disk air intake and the rotary jet disk with the air-jeting disk
Air intake is axis rotation.
Preferably, the aperture of the upper lower through-hole of the screen setting is 1.5 ~ 2.5cm, the rotary jet disk outer wall
The aperture of densely covered through-hole is 1 ~ 5mm.
Preferably, being additionally provided with booster water pump on the seawater inlet.
Preferably, the hot air outlet is obliquely installed obliquely.
Preferably, being additionally provided with atomization condensation chamber air outlet at the top of atomization condensation chamber enclosure.
Preferably, the condenser pipe inclination is arranged side by side.
Preferably, the ultraviolet sterilizer is horizontally arranged with multiple (further preferably 2 rows, every rows 3).
Preferably, being filled in the carbon dioxide storage room equipped with carbon dioxide gas or carbon dioxide enriched air.
The technical effects of the invention are that:
1, water body is atomized by the high-frequency resonant of 2.4MHz by the way that ceramic atomizing piece is arranged, then passes through air-heater
Hot wind carries out gasification process to the droplet after atomization, to realize the effect for decentralized gasification of breaking the whole up into parts, gasification efficiency and effect
Fruit has greatly improved, (most of if gasified by way of boiling so as to avoid the waste of unnecessary energy
Energy presence in the form of heat), reach the reasonable utilization of energy.
2, by the way that rotary rotary jet disk is arranged, may be implemented it is evenly dispersed by gas injection into water body,
So that bubble not only disperse, and due to the effect of centrifugal force on lateral direction bubble there is also kinetic energy (lateral rate),
To which contact of the bubble with water body is more comprehensive.During floating after bubble disperse, due to the surface tension of bubble surface,
Disperse floccule in water body and the sediment being settled out from water body can be adsorbed on bubble outer surface, with bubble
On float on water surface formed foam be collected removing.
3, it, can will be in water body by setting carbon dioxide gas as the gas (or carbon dioxide enriched air) being aerated
Calcareous formation precipitating removes, avoid forming scale in subsequent processing and the damage that causes component.
By the way that high pressure spray gas nozzle is arranged, and foam outlet is arranged on the opposite position of high pressure spray gas nozzle, can make
It obtains and forms fixed flow direction in water surface, the foam for strengthening water surface is flowed out into foam outlet；Simultaneously by gas vent
Be arranged in foam processing pipe top, thus from rotary jet disk spray gas and from high pressure spray gas nozzle spray gas from
Gas vent discharge, enhances the power of the one-way flow of water surface foam.
Solid matter is filtered to remove while brokenly bubble by the way that foamed filter plate is arranged, and as foam enters jointly
In the water body for coming back to trash chamber after filtering to the water body in foam processing pipeline.
By the way that more condenser pipes are arranged, strengthen condensation effect.
Adsorption plate is filtered by setting concavo-convex rod soil, the substances such as microorganism remaining in water body, COD can be adsorbed and be filtered
It removes.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of desalination plant of the present invention.
Wherein: 10- trash chamber horizontal plane, 11- seawater inlet, 12- rotary jet disk, 121- air-jeting disk air intake, 122-
Rolling bearing, 123- gas feeding pipe, 124- air pump, 125- carbon dioxide storage room, 126- driving motor, 131- high-pressure jet
Mouth, 132- foam outlet, 133- foamed filter plate, 134- sundries storage bin, 135- gas vent, 136- water return outlet, 14- grid
Plate, 15- trash chamber water outlet, 20- are atomized condensation chamber horizontal plane, 21- ceramics atomizing piece, 211- ultrasonic atomization high frequency oscillation hair
Raw device, 22- are atomized condensation chamber water inlet, 23- condenser pipe, 24- hot air outlet, 25- hot wind pump, 26- water condensate storage room, 3-
Filtration sterilization room, 31- filtration sterilization room water inlet, 32- concavo-convex rod soil filter adsorption plate, and 33- active carbon filters adsorption plate, 34-
Ultraviolet sterilizer, 35- freshwater storage case.
Specific embodiment
Embodiment 1
As shown in Figure 1.
A kind of desalination plant, including trash chamber, atomization condensation chamber and filtration sterilization room.
The trash chamber includes removal of impurities chamber enclosure, seawater inlet, rotary jet disk, air-jeting disk air intake, rolling bearing, enters
Feed channel, air pump, carbon dioxide storage room, driving motor, high pressure spray gas nozzle, foam outlet, foam handle pipe portion part, return water
Mouth, screen and trash chamber water outlet；The interior bottom of removal of impurities chamber enclosure is arranged in the rotary jet disk, and the rotary jet disk is
Hollow discoid and its outer wall is the through-hole structure that gathers, and rotary jet pan bottom center is provided with air-jeting disk air intake, institute
It states air-jeting disk air intake to be rotatablely connected by the bottom wall of the rolling bearing and the removal of impurities chamber enclosure, the driving motor driving
The outside of removal of impurities chamber enclosure, and its is arranged in the air-jeting disk air intake and rotary jet disk rotation, the gas feeding pipe
One end is connected to that (air-jeting disk air intake is a vertical pipeline, and in the portion being connected with gas feeding pipe with the air-jeting disk air intake
Position is provided with the opening of half, when the rotation of air-jeting disk air intake, due to the opening, gas is enabled to be connected to air-jeting disk
Air intake and gas feeding pipe), the other end is connected to the carbon dioxide storage room, is provided on the gas feeding pipe for entering
The air pump that gas is pressurized in feed channel；Rotary jet disk top is provided with the screen, the screen is horizontally installed on
The outer wall of trash chamber interior of shell and the screen and all side walls of removal of impurities chamber enclosure are affixed, and the screen is provided with densely covered
Upper lower through-hole is provided with seawater inlet on the side wall of the removal of impurities chamber enclosure between rotary jet disk and screen, in the screen
Trash chamber water outlet is provided on the side wall of the removal of impurities chamber enclosure on top；The top of the one side wall of removal of impurities chamber enclosure is provided with height
Air nozzle is pressed, foam outlet is provided on the side wall of the removal of impurities chamber enclosure opposite with the high pressure spray gas nozzle, in the foam
It exports and is provided with the water return outlet on the side wall of the removal of impurities chamber enclosure of lower part, the foam processing pipe portion part includes foam processing
Pipe, foamed filter plate, sundries storage bin and gas vent, foam processing tube top portion are connected to the foam outlet, bottom
It is connected to the water return outlet, is internally provided with 2 foamed filter plates in foam processing pipe and (is inclined in a manner of right low left high
Tiltedly), sundries storage bin (end of the i.e. lower one end of so-called terminal) is provided on 2 foamed filter board terminals,
Foam processing tube top portion is provided with gas vent.
The height and position of the carbon dioxide storage room is higher than the roof of the removal of impurities chamber enclosure, avoids when idle
Wait water body adverse current.
The driving motor drives the air-jeting disk air intake and the rotary jet disk to be with the air-jeting disk air intake
Axis rotation.
The aperture of the upper lower through-hole of the screen setting is 2cm, the aperture of the densely covered through-hole of the rotary jet disk outer wall
For 3mm.
Booster water pump is additionally provided on the seawater inlet.
The atomization condensation chamber include atomization condensation chamber enclosure, ceramic atomizing piece, ultrasonic atomization high frequency oscillation generator,
It is atomized condensation chamber water inlet, condenser pipe, hot air outlet, hot wind pump and water condensate storage room；The atomization condensation chamber water inlet
The lower part of the side wall of atomization condensation chamber enclosure is set and is connected to the trash chamber water outlet, the ceramics atomizing piece is provided with
Simultaneously the horizontal plane of atomization condensation chamber is arranged in hereinafter, 16 ceramic atomizing pieces in 2 rows, every row 8 (size can not be identical)
Laterally it is arranged and is electrically connected with the ultrasonic atomization high frequency oscillation generator that atomization condensation chamber shell exterior is arranged in,
It is provided with hot air outlet on the left side wall of the atomization condensation chamber enclosure above the horizontal plane of atomization condensation chamber, in hot air outlet
Outside is provided with hot wind pump, and hot wind pump provides hot wind to being atomized inside condensation chamber by the hot air outlet；It is being atomized
The topmost of condensation chamber interior of shell is provided with 8 condenser pipes, is provided with water condensate storage at the terminal of 8 condenser pipes
Room, the water condensate storage room is for temporarily being stored the condensed water that the more condenser pipes are collected into, in the condensation
The bottom of water storing chamber is provided with condensed water water outlet.
The hot air outlet is obliquely installed obliquely, specially the inclination of left low and right high.
Atomization condensation chamber air outlet is additionally provided at the top of atomization condensation chamber enclosure.The condenser pipe inclination is side by side
Setting.
The filtration sterilization room includes filtration sterilization room water inlet, concavo-convex rod soil filtering adsorption plate, active carbon filtering absorption
Plate, ultraviolet sterilizer and freshwater storage case；Filtration sterilization room water inlet be arranged in the top of the filtration sterilization room and with
Condensed water water outlet connection, filtration sterilization room water inlet lower part be provided with lateral concavo-convex rod soil filtering adsorption plate (
Referred to as attapulgite filters adsorption plate), the concavo-convex rod soil filtering adsorption plate is to be clamped among the densely covered ventilating hole plate of upper layer and lower layer
Concavo-convex rod soil particle；Concavo-convex rod soil filtering adsorption plate lower part is provided with lateral active carbon and filters adsorption plate, the work
Property charcoal filtering adsorption plate be upper layer and lower layer gather ventilating hole plate among be clamped with active carbon particle；Adsorption plate lower part is filtered in active carbon
It is provided with ultraviolet sterilizer, the ultraviolet sterilizer is horizontally arranged with multiple, specially 2 rows, every row 3.
The ultraviolet sterilizer lower part is provided with freshwater storage case.
Comparative example 1
This comparative example is not provided with screen, and other set-up modes are same as Example 1, by the comparison under 16 hours the same terms
Property test to obtain: the weight for the sundries being collected into the sundries storage bin of this comparative example is the 69% of embodiment 1, and in condenser pipe
Occur on outer wall compared with dot fouling.
Comparative example 2
This comparative example is not provided with ceramic atomizing piece and hot wind pump and hot air outlet, instead sets in water body lower part
Resistance heating wire is set, other set-up modes are identical as embodiment 1, test by comparative under 16 hours the same terms
To: the processing water total weight being collected into this comparative example freshwater storage case is the 82% of embodiment 1, and this comparative example power consumption
It is 3.35 times of embodiment 1.
Claims (9)
1. a kind of desalination plant, it is characterised in that: including trash chamber, atomization condensation chamber and filtration sterilization room；
The trash chamber includes removal of impurities chamber enclosure, seawater inlet, rotary jet disk, air-jeting disk air intake, rolling bearing, enters tracheae
Road, air pump, carbon dioxide storage room, driving motor, high pressure spray gas nozzle, foam outlet, foam handle pipe portion part, water return outlet, grid
Plate and trash chamber water outlet；The interior bottom of removal of impurities chamber enclosure is arranged in the rotary jet disk, and the rotary jet disk is hollow
Discoid and its outer wall be gather through-hole structure, rotary jet pan bottom center is provided with air-jeting disk air intake, the spray
Gas disk air intake is rotatablely connected by the bottom wall of the rolling bearing and the removal of impurities chamber enclosure, described in the driving motor driving
The outside of removal of impurities chamber enclosure, and one end is arranged in air-jeting disk air intake and rotary jet disk rotation, the gas feeding pipe
It is connected to the air-jeting disk air intake, the other end is connected to the carbon dioxide storage room, is arranged on the gas feeding pipe useful
The air pump that gas is pressurized in gas feeding pipe；Rotary jet disk top is provided with the screen, the screen is lateral
All side walls that the outer wall and removal of impurities chamber enclosure of trash chamber interior of shell and the screen is arranged in are affixed, and the screen is provided with
Densely covered upper lower through-hole is provided with seawater inlet on the side wall of the removal of impurities chamber enclosure between rotary jet disk and screen, in institute
It states and is provided with trash chamber water outlet on the side wall of the removal of impurities chamber enclosure on screen top；It is set on the top of the one side wall of removal of impurities chamber enclosure
It is equipped with high pressure spray gas nozzle, foam outlet is provided on the side wall of the removal of impurities chamber enclosure opposite with the high pressure spray gas nozzle, in institute
It states and is provided with the water return outlet on the side wall of the removal of impurities chamber enclosure of foam outlet lower part, the foam processing pipe portion part includes foam
Pipe, foamed filter plate, sundries storage bin and gas vent are handled, foam processing tube top portion is connected to the foam outlet,
Bottom is connected to the water return outlet, the foam processing pipe be internally provided with one or more foamed filter plates, at one or
It is provided with sundries storage bin on multiple foamed filter board terminals, foam processing tube top portion is provided with gas vent；
The atomization condensation chamber includes atomization condensation chamber enclosure, ceramic atomizing piece, ultrasonic atomization high frequency oscillation generator, atomization
Condensation chamber water inlet, condenser pipe, hot air outlet, hot wind pump and water condensate storage room；The atomization condensation chamber water inlet setting
The lower part of the side wall of chamber enclosure is condensed in atomization and is connected to the trash chamber water outlet, and the ceramics atomizing piece is provided with multiple
And the horizontal plane of atomization condensation chamber is set hereinafter, multiple ceramic atomizing pieces are laterally arranged and condense with setting in atomization
Ultrasonic atomization high frequency oscillation generator electrical connection outside chamber enclosure, in the atomization above the horizontal plane of atomization condensation chamber
It condenses and is provided with hot air outlet on the side wall of chamber enclosure, hot wind pump is provided with outside hot air outlet, the hot wind pump is logical
Cross the hot air outlet to atomization condensation chamber inside hot wind is provided；It is provided in the topmost of atomization condensation chamber interior of shell more
Root condenser pipe is provided with water condensate storage room at the terminal of the more condenser pipes, and the water condensate storage room is used for will be more
The condensed water that condenser pipe described in root is collected into temporarily is stored, and the bottom of the water condensate storage room is provided with condensed water and goes out
The mouth of a river；
The filtration sterilization room includes filtration sterilization room water inlet, concavo-convex rod soil filtering adsorption plate, active carbon filtering adsorption plate, purple
Outer sterilizer and freshwater storage case；Filtration sterilization room water inlet be arranged in the top of the filtration sterilization room and with it is described cold
The connection of condensate water outlet is provided with lateral concavo-convex rod soil in filtration sterilization room water inlet lower part and filters adsorption plate, the convex-concave
Stick soil filtering adsorption plate is to be clamped with concavo-convex rod soil particle among the densely covered ventilating hole plate of upper layer and lower layer；It filters and inhales in the concavo-convex rod soil
Attached plate lower part is provided with lateral active carbon filtering adsorption plate, and the active carbon filtering adsorption plate is the densely covered ventilating hole plate of upper layer and lower layer
Centre is clamped with active carbon particle；Active carbon filtering adsorption plate lower part is provided with ultraviolet sterilizer, in the ultraviolet sterilizer
Lower part is provided with freshwater storage case.
2. desalination plant according to claim 1, which is characterized in that the height and position of the carbon dioxide storage room
Higher than the roof of the removal of impurities chamber enclosure.
3. desalination plant according to claim 1, which is characterized in that the driving motor drives the air-jeting disk to enter
Port and the rotary jet disk are rotated by axis of the air-jeting disk air intake.
4. desalination plant according to claim 1, which is characterized in that the aperture of the upper lower through-hole of the screen setting
For 1.5 ~ 2.5cm, the aperture of the densely covered through-hole of the rotary jet disk outer wall is 1 ~ 5mm.
5. desalination plant according to claim 1, which is characterized in that be additionally provided with pressurized water on the seawater inlet
Pump.
6. desalination plant according to claim 1, which is characterized in that the hot air outlet tilts set obliquely
It sets.
7. desalination plant according to claim 1, which is characterized in that condense the top of chamber enclosure also in the atomization
It is provided with atomization condensation chamber air outlet.
8. desalination plant according to claim 1, which is characterized in that the condenser pipe inclination is arranged side by side.
9. desalination plant according to claim 1, which is characterized in that the ultraviolet sterilizer is horizontally arranged with multiple
(preferably 2 rows, every row 3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811567904.7A CN109626681A (en) | 2018-12-21 | 2018-12-21 | A kind of desalination plant |
Applications Claiming Priority (1)
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| CN201811567904.7A CN109626681A (en) | 2018-12-21 | 2018-12-21 | A kind of desalination plant |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110127920A (en) * | 2019-05-09 | 2019-08-16 | 胡妤婕 | Municipal refuse treatment device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110127920A (en) * | 2019-05-09 | 2019-08-16 | 胡妤婕 | Municipal refuse treatment device |
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Application publication date: 20190416 |