CN205294888U - Utilize circulation waste water enrichment facility of solar energy - Google Patents

Utilize circulation waste water enrichment facility of solar energy Download PDF

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Publication number
CN205294888U
CN205294888U CN201521139869.0U CN201521139869U CN205294888U CN 205294888 U CN205294888 U CN 205294888U CN 201521139869 U CN201521139869 U CN 201521139869U CN 205294888 U CN205294888 U CN 205294888U
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CN
China
Prior art keywords
waste water
thickener
waste
dividing plate
chamber
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201521139869.0U
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Chinese (zh)
Inventor
徐临超
朱凯翔
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Zhejiang Industry and Trade Vocational College
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Zhejiang Industry and Trade Vocational College
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Publication date
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Priority to CN201521139869.0U priority Critical patent/CN205294888U/en
Application granted granted Critical
Publication of CN205294888U publication Critical patent/CN205294888U/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Abstract

The utility model discloses an utilize circulation waste water enrichment facility of solar energy, including the solar energy electrothermal tube, be equipped with cold water water inlet and hot water delivery port on the solar energy electrothermal tube, be connected with the cold water inlet tube on the cold water water inlet, be equipped with the hot water outlet pipe on the hot water delivery port, still include the concentrated mechanism of waste water, the concentrated mechanism of waste water includes the support frame, sets up on the support frame and the concentrated groove of taking the lid, and lid and the sealed cooperation in concentrated groove, concentrated inslot are equipped with well cavity, and the cavity intracavity is equipped with that the baffle is two -layer about being divided into well cavity to be waste water cavity respectively and to heat the chamber, be equipped with the deflector along radial interval distribution on waste water cavity's the bottom surface, the length of deflector is less than waste water cavity's length, and the width of deflector equals or be less than waste water cavity's height, the one end of deflector connect on the inner wall of one side of waste water cavity the other end and waste water cavity opposite side clearance fit and along radial crisscross the distribution on the baffle.

Description

A kind of recycling waste water enrichment facility utilizing solar energy
Technical field
This utility model belongs to technical field of waste water processing, especially a kind of recycling waste water enrichment facility utilizing solar energy.
Background technology
At present, solving the waste discharge problem that above-mentioned middle-size and small-size processing enterprise faces, have two ways, one is by chemically treated method, it is necessary to reacted by multi-step chemical, therefore often introduces substantial amounts of chemicals and system process is complicated; Two is by being carried in cell therefor, the waste water treatment plant transporting specialty goes to process, so can reach the requirement of environmental protection, but need so again to solve transportation problem, substantial amounts of waste liquid, waste water there will be again problem in transport, also very inconvenient, once leakage will result in again the pollution to environment, meanwhile, freight also will increase the cost of business processes waste liquid, waste water. If after substantial amounts of waste water being concentrated, concentrated solution being transported to wastewater treatment point again process, be thus solve above-mentioned problems faced, generally concentration waste water needs to use vaporizer, separator etc., so the water in waste water can be separated, discharge or recycle further, but in this processing procedure, vaporizer heats, evaporating after reaching the boiling point of waste water, this will consume the substantial amounts of energy, and therefore how reducing energy consumption is the direction that we need to consider.
Utility model content
In order to overcome the deficiencies in the prior art, this utility model provides a kind of ratio prior art energy-conserving and environment-protective, and cost is low, the Waste water concentrating device of operation capable of circulation.
To achieve these goals, the technical solution adopted in the utility model is: a kind of recycling waste water enrichment facility utilizing solar energy, it is characterized in that: include solar-electricity heat pipe, solar-electricity heat pipe is provided with cold water inlet and hot water outlet, cold water inlet is connected to cold water inlet, hot water outlet is provided with hot water outlet pipe, also include Waste water concentrating mechanism, Waste water concentrating mechanism includes bracing frame, it is arranged on bracing frame and thickener with lid, lid seals with thickener and coordinates, cavity it is provided with in thickener, it is provided with dividing plate in cavity and cavity is divided into upper and lower two-layer respectively waste water chamber and heating chamber, the bottom surface in described waste water chamber is provided with the guide plate of axially spaced distribution, the length of guide plate is less than the width in waste water chamber, the height of guide plate is equal to or less than the height in waste water chamber, opposite side matched in clearance radially that one end of guide plate is connected on the side inwall radially of waste water chamber the other end and waste water chamber and axially staggered be distributed on dividing plate.
In said structure, heat cold water by solar-electricity heat pipe and will not produce the waste of the energy, do not result in secondary pollution, energy-conserving and environment-protective, save again the cost of wastewater treatment, thickener is divided into heating chamber and waste water chamber, cold water flows to heating chamber through the heating of solar-electricity heat pipe, waste water chamber, upper strata utilizes the hot water in lower floor's heating chamber to be heated, waste water intracavity is provided with the guide plate being interspersed, waste water enters from the side in waste water chamber, the track that flows to shown along guide plate flows successively through waste water chamber, such being disposed to extends waste water in waste water intracavity residence time, the waste water in the unit interval is made to have the sufficient time to be heated, steam in abundant evaporating waste water, concentrated effect is better, the height of preferred guide plate is equal to the height in waste water chamber, if the height less than waste water chamber, space is there is between upper bottom surface and the guide plate in waste water chamber, when the entrance flow of waste water is bigger, when waste water has not arrived original circulation track, the liquid level of waste water has just reached the height of guide plate, current guide plate will be crossed to next guide plate diffluence, thus do not reach the effect extending retention time of sewage, if otherwise the height of guide plate is equal to the height in waste water chamber, the so no matter uninterrupted of waste water, all can circulate according to the track of guide plate distribution, effect is more preferably.
As further setting of the present utility model, it is protruding that the surface of described guide plate is provided with equally distributed cambered surface vertically, this cambered surface projection connects formation waveform face, support frame as described above is inclined plane towards the end face of thickener, thickener slant setting is on support frame as described above, thickener quadrangularly, two of which relative to side become up and down place formed tilt upside and inclined underside, the relative side of two other is that parallel placement forms parallel sides, the position corresponding with heating chamber, described inclination upside is provided with the port of export, this port of export connects with cold water inlet, the inclined underside position corresponding with heating chamber is provided with entrance point, this entrance point connects with hot water outlet pipe, cold water inlet and hot water outlet pipe are equipped with control valve.
In said structure, the cambered surface projection on guide plate surface is disposed to increase the resistance on the guide plate surface that waste water flows through, reduce flow velocity, extend the heat time heating time of waste water in the unit interval, make steam evaporation more abundant, thickener slant setting is on bracing frame, preferred entrance point is positioned close to the position of bottom surface, the port of export is positioned close to the position of dividing plate, make hot water can be adequately exposed to the better heat conduction of dividing plate, reduce heat radiation, hot water enters from inclined underside and sidles toward tilting, waste water enters generation convection current from tilting upside, when hot water fills heating chamber time, unnecessary hot water is entered solar-electricity heat pipe by cold water inlet again and reheats, certain water yield thus can be utilized to be repeated heating use, the slant setting of thickener not only extends hot water and the waste water holdup time at heating chamber and waste water intracavity, and contribute to the hot water near inclined underside and shift to an earlier date and baffle contacts, improve the utilization rate of hot water, the valve that controls on cold water inlet and hot water outlet pipe is used for regulating the turnover flow of cold water and hot water, .
As further setting of the present utility model, the inwall of described thickener is provided with and forms the spacing defining flange coordinated with dividing plate, the outer peripheral face of dividing plate abuts with the inwall of thickener, the parallel sides outer wall of thickener is positioned at the position above dividing plate and is provided with pin-and-hole, pin-and-hole is provided with and forms the spacing steady pin abutted with dividing plate, dividing plate forms removable cooperation with thickener, described thickener is provided with cannelure towards the end face of lid, being provided with sealing ring in cannelure, lid is provided with, towards the end face of thickener, the annular lug coordinated with the formation grafting of cannelure adaptation.
In said structure, dividing plate is removable cooperation with thickener, so facilitate the cleaning of heating chamber, because not cleaning for a long time and heating chamber inwall having residue, affect heats, dividing plate is placed on defining flange, but after filling hot water, dividing plate is had buoyancy and the pressure upwards pushed up by hot water, it is provided with and needs the steady pin being positioned at above dividing plate to fix dividing plate, apply downward fixation pressure, when needing to clean, only steady pin need to be pulled down, dividing plate can be taken out, arranging of lid one is to prevent waste water from spilling, two be lid is removable cooperation with thickener, convenient cleaning waste water chamber.
As further setting of the present utility model, described Waste water concentrating mechanism also includes the wastewater trough and the accumulator tank that are connected with waste water chamber, wastewater trough is provided with wastewater outlet, wastewater outlet is connected to waste pipe, tilt corresponding with waste water chamber and near side parallel sides position, upside and be provided with waterwater entrance, the other end of waste pipe connects with waterwater entrance, described accumulator tank is provided with thickened waste water inlet, thickened waste water inlet is connected to thickened waste waterpipe, corresponding with waste water chamber and away from waterwater entrance side the position of inclined underside is provided with thickened waste water out, the other end of thickened waste waterpipe connects with thickened waste water out, waste pipe and thickened waste waterpipe are equipped with control valve.
In said structure, the waste water that industry produces is unified to be stored in wastewater trough, waterwater entrance and thickened waste water out are separately positioned on the both sides in waste water chamber, make waste water be entered by side to flow out from opposite side by after the track circulation of guide plate, accumulator tank is flowed to after the heated concentration of waste water, the process or the secondary that carry out next step utilize, and waste pipe and the valve that controls on thickened waste waterpipe are used to the turnover flow of the waste water after regulating waste water and concentration.
As further setting of the present utility model, on described lid, the position away from waterwater entrance is provided with steam (vapor) outlet, steam (vapor) outlet is connected to jet chimney, the other end of jet chimney is connected to condenser, described condenser is provided with and is condensed out the mouth of a river, cold water inlet is provided with and is condensed out the steam branch pipe that the mouth of a river connects, jet chimney and be equipped with control valve on steam branch pipe.
In said structure, producing substantial amounts of steam after waste water is heated, steam (vapor) outlet is positioned close to the position of thickened waste water out, steam exits into condenser from steam (vapor) outlet and is condensed into cold water, flow to cold water inlet again through steam branch pipe, enter the heating of solar-electricity heat pipe, recycle.
As further setting of the present utility model, described thickener and lid are adiabatic material and make, and dividing plate is that heat-conducting is made.
In said structure, thickener is made for adiabatic and resistant material, because some waste water has corrosivity, thermal insulation can ensure that the temperature in thickener is maintained in certain temperature, avoid heat radiation too fast, improving heats, dividing plate is made up of i.e. heat conduction but also corrosion resistant material, the thermal conductivity of increase dividing plate.
Adopting such scheme, the quantitative water of reusable edible is heated concentration to waste water, and solar energy is sustainable energy, environment friendly and pollution-free, will not cause secondary pollution because of Waste water concentrating, not only reduce cost for wastewater treatment, and can reach better concentrated effect.
Below in conjunction with accompanying drawing, this utility model is further described.
Accompanying drawing explanation
Accompanying drawing 1 is this utility model specific embodiment schematic appearance;
Accompanying drawing 2 is this utility model specific embodiment thickener STRUCTURE DECOMPOSITION figure;
Accompanying drawing 3 is this utility model specific embodiment thickener structure sectional view;
Accompanying drawing 4 is this utility model specific embodiment cover body structure schematic diagram.
Detailed description of the invention
By the examples below this utility model is specifically described; it is served only for this utility model is further described; it is not intended that the restriction to this utility model protection domain, this utility model can be made some nonessential improvement and adjustment according to the content of above-mentioned utility model by the technician in this field.
Specific embodiment of the utility model is as Figure 1-4, a kind of recycling waste water enrichment facility utilizing solar energy, including solar-electricity heat pipe 1, solar-electricity heat pipe 1 is provided with cold water inlet 11 and hot water outlet 12, cold water inlet 11 is connected to cold water inlet 13, hot water outlet 12 is provided with hot water outlet pipe 14, also include Waste water concentrating mechanism 2, Waste water concentrating mechanism 2 includes bracing frame 21, it is arranged on the thickener 23 on bracing frame 21 and with lid 22, lid 22 seals with thickener 23 and coordinates, cavity 231 it is provided with in thickener 23, it is provided with dividing plate 232 in cavity 231 and cavity 231 is divided into upper and lower two-layer respectively waste water chamber 2311 and heating chamber 2312, the bottom surface in described waste water chamber 2311 is provided with the guide plate 2321 of radially spaced distribution, the length of guide plate 2321 is less than the length in waste water chamber 2311, the width of guide plate 2321 is equal to or less than the height in waste water chamber 2311, one end of guide plate 2321 is connected on the side inwall in waste water chamber 2311 other end and the opposite side matched in clearance in waste water chamber 2311 and radially interleaved be distributed on dividing plate 232.Heat cold water by solar-electricity heat pipe 1 and will not produce the waste of the energy, do not result in secondary pollution, energy-conserving and environment-protective, save again the cost of wastewater treatment, thickener 23 is divided into heating chamber 2312 and waste water chamber 2311, cold water flows to heating chamber 2312 through the heating of solar-electricity heat pipe 1, waste water chamber, upper strata 2311 utilizes the hot water in lower floor's heating chamber 2312 to be heated, the guide plate 2321 being interspersed it is provided with in waste water chamber 2311, waste water enters from the side in waste water chamber 2311, the track that flows to shown along guide plate 2321 flows successively through waste water chamber 2311, such being disposed to extends waste water residence time in waste water chamber 2311, the waste water in the unit interval is made to have the sufficient time to be heated, steam in abundant evaporating waste water, concentrated effect is better, the height of preferred guide plate 2321 is equal to the height in waste water chamber 2311, if the height less than waste water chamber 2311, space is there is between upper bottom surface and the guide plate 2321 in waste water chamber 2311, when the entrance flow of waste water is bigger, when waste water has not arrived original circulation track, the liquid level of waste water has just reached the height of guide plate 2321, current guide plate 2321 will be crossed to next guide plate 2321 diffluence, thus do not reach the effect extending retention time of sewage, if otherwise the height of guide plate 2321 is equal to the height in waste water chamber 2311, the so no matter uninterrupted of waste water, all can circulate according to the track of guide plate 2321 distribution, effect is more preferably.
The surface of above-mentioned guide plate 2321 is provided with equally distributed cambered surface projection 23211 vertically, this cambered surface protruding 23211 connects formation waveform face, support frame as described above 21 is inclined plane towards the end face of thickener 23, thickener 23 slant setting is on support frame as described above 21, thickener 23 quadrangularly, two of which relative to side become to place up and down to be formed and tilt upside 233 and inclined underside 234, the relative side of two other is that parallel placement forms parallel sides 235, described tilt the position corresponding with heating chamber 2312, upside 233 be provided with the port of export 2331, this port of export 2331 connects with cold water inlet 13, inclined underside 234 position corresponding with heating chamber 2312 is provided with entrance point 2341, this entrance point 2341 connects with hot water outlet pipe 14, cold water inlet 13 and hot water outlet pipe 14 are equipped with control valve 3. the cambered surface projection 23211 on guide plate 2321 surface is disposed to increase the resistance on guide plate 2321 surface that waste water flows through, reduce flow velocity, extend the heat time heating time of waste water in the unit interval, make steam evaporation more abundant, thickener 23 slant setting is on bracing frame 21, preferred entrance point 2341 is positioned close to the position of bottom surface, the port of export 2331 is positioned close to the position of dividing plate 232, make hot water can be adequately exposed to the better heat conduction of dividing plate 232, reduce heat radiation, hot water enters to walk toward inclination upside 233 from inclined underside 234, when hot water fills heating chamber 2312 time, unnecessary hot water is entered solar-electricity heat pipe 1 by cold water inlet 13 again and reheats, certain water yield thus can be utilized to be repeated heating use, the slant setting of thickener 23 not only extends hot water and the waste water holdup time in heating chamber 2312 and waste water chamber 2311, and contribute to the hot water near inclined underside 234 and contact with dividing plate 232 in advance, improve the utilization rate of hot water, the valve 3 that controls on cold water inlet 13 and hot water outlet pipe 14 is used for regulating the turnover flow of cold water and hot water.
The inwall of above-mentioned thickener 23 is provided with and forms the spacing defining flange 236 coordinated with dividing plate 232, the outer peripheral face of dividing plate 232 abuts with the inwall of thickener 23, parallel sides 235 outer wall of thickener 23 is positioned at the position above dividing plate 232 and is provided with pin-and-hole 2351, pin-and-hole 2351 is provided with and forms the spacing steady pin 2352 abutted with dividing plate 232, dividing plate 232 forms removable cooperation with thickener 23, described thickener 23 is provided with cannelure 237 towards the end face of lid 22, sealing ring 2371 it is provided with in cannelure 237, lid 22 is provided with, towards the end face of thickener 23, the annular lug 221 coordinated with cannelure 237 adaptive formation grafting. dividing plate 232 coordinates for removable with thickener 23, so facilitate the cleaning of heating chamber 2312, because not cleaning for a long time and heating chamber 2312 inwall having residue, affect heats, dividing plate 232 is placed on defining flange 236, but after filling hot water, dividing plate 232 is had buoyancy and the pressure upwards pushed up by hot water, it is provided with and needs the steady pin 2352 being positioned at above dividing plate 232 to fix dividing plate 232, apply downward fixation pressure, when needing to clean, only steady pin 2352 need to be pulled down, dividing plate 232 can be taken out, arranging of lid 22 one is to prevent waste water from spilling, two is that lid 22 coordinates for removable with thickener 23, convenient cleaning waste water chamber 2311.
Above-mentioned Waste water concentrating mechanism 2 also includes the wastewater trough 24 and the accumulator tank 25 that are connected with waste water chamber 2311, wastewater trough 24 is provided with wastewater outlet 241, wastewater outlet 241 is connected to waste pipe 242, tilt corresponding with waste water chamber 2311 and near side parallel sides position, upside 233 and be provided with waterwater entrance 2332, the other end of waste pipe 242 connects with waterwater entrance 2332, described accumulator tank 25 is provided with thickened waste water inlet 251, thickened waste water inlet 251 is connected to thickened waste waterpipe 252, corresponding with waste water chamber 2311 and away from waterwater entrance 2332 side the position of inclined underside 234 is provided with thickened waste water out 2342, the other end of thickened waste waterpipe 252 connects with thickened waste water out 2342, waste pipe 242 and thickened waste waterpipe 252 are equipped with control valve 3. the waste water that industry produces is unified to be stored in wastewater trough 24, waterwater entrance 2332 and thickened waste water out 2342 are separately positioned on the both sides in waste water chamber 2311, make waste water be entered by side to flow out from opposite side by after the track circulation of guide plate 2321, accumulator tank 25 is flowed to after the heated concentration of waste water, the process or the secondary that carry out next step utilize, and waste pipe 242 and the valve 3 that controls on thickened waste waterpipe 252 are used to the turnover flow of the waste water after regulating waste water and concentration.
On above-mentioned lid 22, the position away from waterwater entrance 2332 is provided with steam (vapor) outlet 222, steam (vapor) outlet 222 is connected to jet chimney 223, the other end of jet chimney 223 is connected to condenser 224, described condenser 224 is provided with and is condensed out the mouth of a river 2241, cold water inlet 13 is provided with and is condensed out the steam branch pipe 131 that the mouth of a river 2241 connects, jet chimney 223 and steam branch pipe 131 is equipped with control valve 3. Substantial amounts of steam can be produced after waste water is heated, steam (vapor) outlet 222 is positioned close to the position of thickened waste water out 2342, steam exits into condenser 224 from steam (vapor) outlet 222 and is condensed into cold water, cold water inlet 13 is flowed to again through steam branch pipe 131, enter solar-electricity heat pipe 1 to heat, recycle.
Above-mentioned thickener 23 and lid 22 are adiabatic material and make, and dividing plate 232 is made for heat-conducting.Thickener 23 is made for adiabatic and resistant material, because some waste water has corrosivity, thermal insulation can ensure that the temperature in thickener 23 is maintained in certain temperature, avoid heat radiation too fast, improve heats, dividing plate 232 is made up of i.e. heat conduction but also corrosion resistant material, increases the thermal conductivity of dividing plate 232.

Claims (6)

1. the recycling waste water enrichment facility utilizing solar energy, it is characterized in that: include solar-electricity heat pipe, solar-electricity heat pipe is provided with cold water inlet and hot water outlet, cold water inlet is connected to cold water inlet, hot water outlet is provided with hot water outlet pipe, also include Waste water concentrating mechanism, Waste water concentrating mechanism includes bracing frame, it is arranged on bracing frame and thickener with lid, lid seals with thickener and coordinates, cavity it is provided with in thickener, it is provided with dividing plate in cavity and cavity is divided into upper and lower two-layer respectively waste water chamber and heating chamber, the bottom surface in described waste water chamber is provided with the guide plate of axially spaced distribution, the length of guide plate is less than the width in waste water chamber, the height of guide plate is equal to or less than the height in waste water chamber, opposite side matched in clearance radially that one end of guide plate is connected on the side inwall radially of waste water chamber the other end and waste water chamber and axially staggered be distributed on dividing plate.
2. a kind of recycling waste water enrichment facility utilizing solar energy according to claim 1, it is characterized in that: it is protruding that the surface of described guide plate is provided with equally distributed cambered surface vertically, this cambered surface projection connects formation waveform face, support frame as described above is inclined plane towards the end face of thickener, thickener slant setting is on support frame as described above, thickener quadrangularly, two of which relative to side become up and down place formed tilt upside and inclined underside, the relative side of two other is that parallel placement forms parallel sides, the position corresponding with heating chamber, described inclination upside is provided with the port of export, this port of export connects with cold water inlet, the inclined underside position corresponding with heating chamber is provided with entrance point, this entrance point connects with hot water outlet pipe, cold water inlet and hot water outlet pipe are equipped with control valve.
3. a kind of recycling waste water enrichment facility utilizing solar energy according to claim 1, it is characterized in that: the inwall of described thickener is provided with and forms the spacing defining flange coordinated with dividing plate, the outer peripheral face of dividing plate abuts with the inwall of thickener, the parallel sides outer wall of thickener is positioned at the position above dividing plate and is provided with pin-and-hole, pin-and-hole is provided with and forms the spacing steady pin abutted with dividing plate, dividing plate forms removable cooperation with thickener, described thickener is provided with cannelure towards the end face of lid, sealing ring it is provided with in cannelure, lid is provided with, towards the end face of thickener, the annular lug coordinated with the formation grafting of cannelure adaptation.
4. a kind of recycling waste water enrichment facility utilizing solar energy according to claim 1, it is characterized in that: described Waste water concentrating mechanism also includes the wastewater trough and the accumulator tank that are connected with waste water chamber, wastewater trough is provided with wastewater outlet, wastewater outlet is connected to waste pipe, tilt corresponding with waste water chamber and near side parallel sides position, upside and be provided with waterwater entrance, the other end of waste pipe connects with waterwater entrance, described accumulator tank is provided with waterwater entrance, waterwater entrance is connected to thickened waste waterpipe, corresponding with waste water chamber and away from waterwater entrance side the position of inclined underside is provided with wastewater outlet, the other end of thickened waste waterpipe connects with wastewater outlet, waste pipe and thickened waste waterpipe are equipped with control valve.
5. a kind of recycling waste water enrichment facility utilizing solar energy according to claim 1, it is characterized in that: on described lid, the position away from waterwater entrance is provided with steam (vapor) outlet, steam (vapor) outlet is connected to jet chimney, the other end of jet chimney is connected to condenser, described condenser is provided with and is condensed out the mouth of a river, cold water inlet is provided with and is condensed out the steam branch pipe that the mouth of a river connects, jet chimney and be equipped with control valve on steam branch pipe.
6. a kind of recycling waste water enrichment facility utilizing solar energy according to claim 1-5 any one, it is characterised in that: described thickener and lid are adiabatic material and make, and dividing plate is that heat-conducting is made.
CN201521139869.0U 2015-12-31 2015-12-31 Utilize circulation waste water enrichment facility of solar energy Expired - Fee Related CN205294888U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201521139869.0U CN205294888U (en) 2015-12-31 2015-12-31 Utilize circulation waste water enrichment facility of solar energy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201521139869.0U CN205294888U (en) 2015-12-31 2015-12-31 Utilize circulation waste water enrichment facility of solar energy

Publications (1)

Publication Number Publication Date
CN205294888U true CN205294888U (en) 2016-06-08

Family

ID=56468918

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201521139869.0U Expired - Fee Related CN205294888U (en) 2015-12-31 2015-12-31 Utilize circulation waste water enrichment facility of solar energy

Country Status (1)

Country Link
CN (1) CN205294888U (en)

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Granted publication date: 20160608

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