CN202193639U - Device for desalinizing sea water or purifying sewage - Google Patents
Device for desalinizing sea water or purifying sewage Download PDFInfo
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- CN202193639U CN202193639U CN2011202748555U CN201120274855U CN202193639U CN 202193639 U CN202193639 U CN 202193639U CN 2011202748555 U CN2011202748555 U CN 2011202748555U CN 201120274855 U CN201120274855 U CN 201120274855U CN 202193639 U CN202193639 U CN 202193639U
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- 239000013535 sea water Substances 0.000 title claims abstract description 82
- 239000010865 sewage Substances 0.000 title claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 210000005056 cell body Anatomy 0.000 claims description 45
- 239000000463 material Substances 0.000 claims description 19
- 239000004033 plastic Substances 0.000 claims description 4
- 229920003023 plastic Polymers 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 2
- 239000004576 sand Substances 0.000 abstract description 26
- 238000000746 purification Methods 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000010612 desalination reaction Methods 0.000 abstract description 2
- 241000276425 Xiphophorus maculatus Species 0.000 abstract 10
- 239000012780 transparent material Substances 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 60
- 239000002985 plastic film Substances 0.000 description 21
- 229920006255 plastic film Polymers 0.000 description 21
- 239000000377 silicon dioxide Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 12
- 230000035699 permeability Effects 0.000 description 7
- 230000005855 radiation Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 238000002834 transmittance Methods 0.000 description 5
- 229920006332 epoxy adhesive Polymers 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 230000008020 evaporation Effects 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000001070 adhesive effect Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 230000003760 hair shine Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001493 electron microscopy Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 229920003987 resole Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000003469 silicate cement Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Images
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model relates to a device for desalinizing sea water or purifying sewage. The utility model is characterized in that the device for desalinizing the sea water or purifying the sewage comprises a pipeline, a first platy piece and a second platy piece; the first platy piece is arranged in an inclined manner so that one end of the first platy piece is higher than the other end of the first platy piece; furthermore, the first platy piece is located above the second platy piece; the first platy piece is made of a transparent material; the second platy piece is provided with water-holding capacity; a plurality of openings are arranged on the pipeline; and due to the direction of the openings, the sea water or the sewage in the pipeline can partially or entirely flow to the second platy piece. The device for desalinizing the sea water or purifying the sewage in the utility model can be used for better desalinizing the sea water or purifying the sewage and is simple in structure, so that the cost for production and operation is saved. Preferably, sand with low cost and extensive source is applied to desalination of the sea water and purification of the sewage successfully. The device for desalinizing the sea water or purifying the sewage in the utility model can be widely applied to the field of water resource treatment.
Description
Technical field
The utility model relates to a kind of water treatment device, particularly, relates to a kind of sea water desaltination or effluent treatment plant.
Background technology
The water crisis is one of greatest problem of facing of the present whole world, therefore, develops new water resources, administers water and pollutes and become the topic that people earnestly pay close attention to.Sea water desaltination is the important channel of a kind of human lives's of obtaining water and water of productive use; At present; The method of sea water desaltination mainly contains membrane separation process, electroosmose process, distillation method and magnetic field method etc., but existing sea water distiling plant all exists complex structure, cost problem of higher.In addition, sewage purification also can be obtained human domestic water and water of productive use, but present effluent treatment plant also exists complex structure, cost problem of higher.
The utility model content
The purpose of the utility model is in order to overcome existing sea water desaltination or effluent treatment plant complex structure, cost problem of higher, a kind of new sea water desaltination or effluent treatment plant to be provided.
To achieve these goals; The utility model provides a kind of sea water desaltination or effluent treatment plant, it is characterized in that, said sea water desaltination or effluent treatment plant comprise pipeline, first plate-like piece and second plate-like piece; Said first plate-like piece is obliquely installed and makes an end of said first plate-like piece be higher than the other end; And said first plate-like piece is positioned at said second plate-like piece top, and the material of said first plate-like piece is a light transmissive material, and said second plate-like piece has water-holding power; Said pipeline has a plurality of openings, and the position of said pipeline and the direction of opening make seawater or the sewage in the pipeline partly or entirely can flow on said second plate-like piece.
Under the preferable case, said pipeline is positioned at the higher end of said first plate-like piece, and contacts with said second plate-like piece with said first plate-like piece, and the opening of said pipeline is arranged between said first plate-like piece and said second plate-like piece.
Preferably, the coefficient of permeability of said second plate-like piece is 0.01-0.07cm/s, and thickness is 5-15cm.
Sea water desaltination that the utility model provides or effluent treatment plant; Because the material of first plate-like piece is a light transmissive material, sunlight sees through first plate-like piece and shines on second plate-like piece, makes the moisture evaporation in second plate-like piece with water-holding power; Moisture evaporation is the back condensation to first plate-like piece; Because an end of first plate-like piece is higher than the other end, condensed water is dirty along the gradient of first plate-like piece, accomplishes sea water desaltination or sewage purification process.
Sea water desaltination or effluent treatment plant that the utility model provides are simple in structure; Utilize sunshine to accomplish sea water desaltination or sewage purification process; Practiced thrift production and operation cost, under the preferable case, second plate-like piece of sea water desaltination of the utility model or effluent treatment plant forms the silica sand adhesive solidification through sticker; Successfully realized the sand of low cost and wide material sources is applied to sea water desaltination or sewage purification, further practiced thrift production cost.Sea water desaltination that the utility model provides or effluent treatment plant can be widely used in water resources and handle the field.
Other feature and advantage of the utility model will partly specify in embodiment subsequently.
Description of drawings
Fig. 1 is according to the sea water desaltination of the utility model or the structural representation of effluent treatment plant.
Fig. 2 is according to the sea water desaltination with first cell body and second cell body of the utility model or the structural representation of effluent treatment plant.
Description of reference numerals
1 pipeline; 2 first plate-like pieces; 3 second plate-like pieces; 4 first cell bodies; 5 second cell bodies.
Embodiment
Be elaborated below in conjunction with the embodiment of accompanying drawing to the utility model.Should be understood that embodiment described herein only is used for explanation and explains the utility model, is not limited to the utility model.
The utility model provides a kind of sea water desaltination or effluent treatment plant; As shown in Figure 1; This sea water desaltination or effluent treatment plant comprise that pipeline 1, first plate-like piece 2 and second plate-like piece, 3, the first plate-like pieces 2 are obliquely installed makes an end of first plate-like piece 2 be higher than the other end, and first plate-like piece 2 is positioned at second plate-like piece, 3 tops; The material of first plate-like piece 2 is a light transmissive material; Second plate-like piece 3 has water-holding power, and pipeline 1 has a plurality of opening (not shown)s, and the position of pipeline 1 and the direction of opening make seawater or the sewage in the pipeline 1 partly or entirely can flow on second plate-like piece 3.
According to the utility model; Although second plate-like piece 3 has the purpose that water-holding power can realize the utility model, under the preferable case, the coefficient of permeability of second plate-like piece 3 is 0.01-0.07cm/s; Thickness is 5-15cm; Further under the preferable case, the coefficient of permeability of second plate-like piece 3 is 0.03-0.07cm/s, and thickness is 8-10cm.
For second plate-like piece 3 is not stopped up by the impurity such as silt in seawater or the sewage in the water holding process, the aperture of second plate-like piece 3 is preferably 50-200 μ m.
Second plate-like piece 3 can be made up of this area various materials with water-holding power commonly used; In order further to practice thrift cost, under the preferable case, second plate-like piece 3 forms the silica sand adhesive solidification through sticker; The median size of silica sand is preferably 100-400 μ m; Further be preferably 200-300 μ m, the weight ratio of sticker and silica sand is preferably 1-15: 100, further be preferably 5-10: 100.
Kind for silica sand does not have particular requirement, can be various silica sands, for example can be selected from silica sand, drift-sand, artificial sand, reclaimed sand, river sand and extra large sand and the mountain sand one or more.The degree of sphericity of silica sand is good more, can guarantee that more the hole of silica sand diameter is less and even, thereby further improves the effect of even water holding, and therefore, the degree of sphericity of the utility model silica sand can be 0.5-0.95, is preferably 0.7-0.8.Wherein, " degree of sphericity " refers to the relative acutance of grain corner or measuring of curvature, also can refer to the degree of particle subglobular; The measuring method of degree of sphericity is conventionally known to one of skill in the art, for example, can adopt chart method to measure.In order to reach the desired degree of sphericity requirement of the utility model, can adopt and silica sand carried out the needs that control methods known in those skilled in the art such as ball milling satisfy the silica sand degree of sphericity.
Sticker can be this area various stickers commonly used, is preferably in epoxy resin, polyvinylidene fluoride resin, water glass, resol, vinyl resin, polyamine fat resin and the silicate cement one or more.
Set-up mode for second plate-like piece 3 does not have particular requirement, as long as make second plate-like piece 3 be positioned at the below of first plate-like piece 2, can be horizontal positioned for tilting to place yet.
First plate-like piece 2 is a light transmissive material, and transmittance is preferably 85-95%, and the printing opacity in the utility model refers to through sunshine.Transmittance adopts GB/T2410-2008 to measure.In order further to reduce cost, first plate-like piece 2 is preferably plastics or glass.
First plate-like piece 2 is obliquely installed and makes an end of first plate-like piece 2 be higher than the other end; In order to make first plate-like piece 2 have bigger sunlight transmission plane that the water of condensation on first plate-like piece 2 is flowed down more easily, first plate-like piece 2 is preferably 10-30 ° with the angle of horizontal plane.As long as the distance between first plate-like piece 2 and second plate-like piece 3 makes the water that condenses on first plate-like piece 2 not by the sewage pollution that absorbs in second plate-like piece 3; Under the preferable case, any 1 o'clock vertical range to first plate-like piece 2 is 5-45cm on second plate-like piece 3.Method for first plate-like piece 2 is obliquely installed does not have particular requirement; Can adopt this area the whole bag of tricks commonly used, for example can first plate-like piece, 2 oblique cuttings be gone in the earth fixingly, also can be provided with one and hang and establish device; One end of first plate-like piece 2 is fixed on the horizontal plane; Thereby the other end adopts to hang and establishes device and sling and be obliquely installed, and a strut member can also be set, and first plate-like piece 2 is set up in the strut member setting that tilts.
Under the preferable case, pipeline 1 is positioned at the higher end of first plate-like piece 2, and contacts with second plate-like piece 3 with first plate-like piece 2; The opening of pipeline 1 is arranged between first plate-like piece 2 and second plate-like piece 3, does not have particular requirement for the set-up mode of pipeline 1, can adopt this area various set-up modes commonly used; As long as make pipeline 1 be positioned at the higher end of first plate-like piece 2; And part gets final product between first plate-like piece 2 and second plate-like piece 3 at least, for example a strut member can be set, and pipeline 1 is fixed on the strut member; Also can be provided with one and hang and establish device, pipeline 1 is hung be located on the desired position.
Under the preferable case, the direction of opening makes seawater or the sewage in the pipeline 1 all flow on second plate-like piece 3.For seawater or sewage in the pipeline 1 are as far as possible all flow on second plate-like piece 3; Under the preferable case; Sea water desaltination or effluent treatment plant also comprise the baffle plate (not shown) that is arranged between first plate-like piece 2 and second plate-like piece 3, and baffle plate is used to stop seawater or sewage in the pipeline to flow to first plate-like piece 2.One end of baffle plate can be arranged on pipeline 1 on the part between first plate-like piece 2 and second plate-like piece 3, perhaps can be tightly connected with the position A of first plate-like piece 2.For seawater or sewage in the pipeline 1 are as far as possible all flow on second plate-like piece 3; The minor increment m between A to the first plate-like piece 2 higher-end of position and the ratio than the minor increment M between the low side of position A to the first plate-like piece 2 are preferably 0-0.1: 1; The baffle plate and first plate-like piece 2 be a than the angle between the low side; The angle of first plate-like piece 2 and horizontal plane and a sum are less than 90 °, and a is greater than 0 °.Size and shape for opening do not have particular requirement, can adopt all size and shape, as long as can realize the object of the invention.
Shape and material for pipeline 1 do not have particular requirement, can adopt this area different shape and material commonly used.
Seawater after the collection desalination for ease or the sewage after the purification; As shown in Figure 2; Sea water desaltination or effluent treatment plant comprise also that preferably first cell body, 4, the first cell bodies 4 are positioned at the below of a lower end of first plate-like piece 2, are used to receive the water that flows down from first plate-like piece 2.Size, shape and material for first cell body 4 do not have particular requirement, can be for this area all size, shape and material commonly used, as long as can receive the water that flows down from first plate-like piece 2.
Preferably, sea water desaltination or effluent treatment plant comprise that also second cell body, 5, the second cell bodies 5 are positioned at the below of second plate-like piece 3, are used to receive second plate-like piece, 3 unabsorbed seawater or sewage.Size, shape and material for second cell body 5 do not have particular requirement, can be for this area all size, shape and material commonly used, as long as can receive second plate-like piece, 3 unabsorbed seawater or sewage.Can be handled again in order to make seawater or sewage in second cell body 5; Under the preferable case; Second cell body 5 is communicated with pipeline 1; And said sea water desaltination or effluent treatment plant comprise that also the water cycle that can make in second cell body returns said ducted pump, through water pump with in seawater in second cell body 5 or the sump pump return pipe road 1.Do not have particular requirement for second cell body 5 with the mode that pipeline 1 is communicated with, can be this area variety of way commonly used.
During actual the use, sea water desaltination or effluent treatment plant are placed on the solar radiation place get final product.Seawater in the pipeline 1 or sewage flow in second plate-like piece 3 with water-holding power; Sunlight sees through first plate-like piece 2 and shines on second plate-like piece 3; Make the moisture evaporation in second plate-like piece 3, moisture evaporation is the back condensation to first plate-like piece 2, and condensed water is dirty along the gradient that is obliquely installed of first plate-like piece 2; High-boiling-point impurities such as salt in seawater or the sewage then can not be evaporated on first plate-like piece 2, accomplish sea water desaltination or sewage purification process.Preferably; Flow into along the dirty water of the gradient that is obliquely installed of first plate-like piece 2 in first cell body 4 of the below of hanging down an end that is arranged on first plate-like piece 2; The seawater or the sewage inflow that are not absorbed by second plate-like piece 3 are arranged in second cell body 5 of second plate-like piece, 3 belows, and the water in second cell body 5 flows in the pipeline 1 in the effect of water pump next time.
Be not difficult to find out that through above-mentioned principle sea water desaltination of the utility model or effluent treatment plant can be used to handle the various boiling points that contain and be higher than the water resources that water or volatility are lower than the impurity of water, like seawater or various industry or sanitary wastewater.
More than combine accompanying drawing to describe the preferred implementation of the utility model in detail; But; The utility model is not limited to the detail in the above-mentioned embodiment; In the technical conceive scope of the utility model, can carry out multiple simple variant to the technical scheme of the utility model, these simple variant all belong to the protection domain of the utility model.
Need to prove in addition; Each concrete technical characterictic described in above-mentioned embodiment under reconcilable situation, can make up through any suitable manner; For fear of unnecessary repetition, the utility model is to the explanation no longer separately of various possible array modes.
In addition, also can carry out arbitrary combination between the various embodiment of the utility model, as long as its thought without prejudice to the utility model, it should be regarded as content disclosed in the utility model equally.
Embodiment
Following embodiment will be further described the utility model, but therefore not limit the utility model.
In following embodiment:
Adopt JC/T 945-2005 to test the coefficient of permeability of second plate-like piece 3.
Aperture with determination of electron microscopy second plate-like piece 3.
The hand-held light refractive type salometer that adopts Beijing sunlight hundred million things to reach trade Co., Ltd is measured salinity.
Adopt filter paper method to measure SS concentration.SS is the abbreviation of English Suspended Substance, i.e. suspended substance in the water quality.SS concentration is the concentration of suspended substance in the water, is the important indicator of water quality.It is that to make water sample be the filter membrane of 0.45 μ m through the aperture that filter paper method is measured SS concentration; The material that is trapped on the filter membrane is dried to constant weight in 103～105 ℃; Weighing is dried to the weight of the solid matter of constant weight then; With the weight of solid matter volume divided by the water sample through filter membrane, promptly get SS concentration, measure unit is mg/L.
Adopt the method for GB/T 22597-2008 to measure the COD value.COD is that COD is claimed chemical oxygen demand again; Be to utilize chemical oxidizing agent (like potassium permanganate) with an oxidisable substance in the water (like organism, nitrite, ferrous salt, sulfide etc.) oxygenolysis; Calculate the consumption of oxygen then according to the amount of residual oxygenant; Be the important indicator of expression water pollution degree, measure unit is mg/L.
In following examples, silica sand is available from blue sky, Yongdeng silica sand ltd.
Epoxy adhesive: Shandong Shengquan Chemical Industry Co., Ltd., E-44.
Plastics are contained sunlight Plastic Products Co., Ltd available from the Tianjin gold.
The salinity of the seawater in the pipeline 1 is 35 ‰
Sewage in the pipeline 1 is the sewage from the residential quarter, SS concentration 326mg/L, COD value 300mg/L.
The silica sand (median size 250 μ m, degree of sphericity 0.7) and the 8 weight part epoxy adhesives of 100 weight parts are mixed, obtain mixture; And being laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 10cm; Under 80 ℃, 20-40% relative humidity, solidified 12 hours, obtain second plate-like piece 3, wherein; The coefficient of permeability of second plate-like piece 3 is 0.03cm/s, and thickness is 10cm, and the aperture is 80-150 μ m.
Second plate-like piece 3 has been lain on the sunlit level ground, and transmittance is set above that being 90% plastic film, making plastic film become 20 ° of angles with the level ground, is 5-35cm to vertical range of plastic film a bit arbitrarily on second plate-like piece 3.
An end higher at plastic film is provided with pipeline 1, and pipeline 1 all between the plastic film and second plate-like piece 3, is provided with opening on the pipeline 1, on pipeline 1, baffle plate is set, and baffle plate and plastic film are 40 ° than the angle between the low side.
Below the low end of plastic film, first cell body 4 is set, second cell body, 5, the second cell bodies 5 is set below second plate-like piece 3 is communicated with pipeline 1, and in second cell body 5, a water pump is set, water pump can be with in the water pump return pipe road 1 in second cell body 5.
In pipeline 1, feed seawater, behind the solar radiation 10h, the salinity that records the water in first cell body 4 is seen table 1.
Perhaps in pipeline 1, feed sewage, behind the solar radiation 10h, the SS concentration and the COD value that record the water in first cell body 4 are seen table 1.
The silica sand (median size 200 μ m, degree of sphericity 0.8) and the 10 weight part epoxy adhesives of 100 weight parts are mixed, obtain mixture; And being laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 9cm; Under 80 ℃, 20-40% relative humidity, solidified 12 hours, obtain second plate-like piece 3, wherein; The coefficient of permeability of second plate-like piece 3 is 0.07cm/s, and thickness is 9cm, and the aperture is 50-100 μ m.
Second plate-like piece 3 has been tiled on the sunlit level ground, and transmittance is set above that being 95% plastic film, making plastic film become 10 ° of angles with the level ground, is 5-20cm to vertical range of plastic film a bit arbitrarily on second plate-like piece 3.
An end higher at plastic film is provided with pipeline 1, and pipeline 1 all between the plastic film and second plate-like piece 3, is provided with opening on the pipeline 1, on pipeline 1, baffle plate is set, and baffle plate and plastic film are 30 ° than the angle between the low side.
Below the low end of plastic film, first cell body 4 is set, second cell body, 5, the second cell bodies 5 is set below second plate-like piece 3 is communicated with pipeline 1, and in second cell body 5, a water pump is set, water pump can be with in the water pump return pipe road 1 in second cell body 5.
In pipeline 1, feed seawater, behind the solar radiation 10h, the salinity that records the water in first cell body 4 is seen table 1.
Perhaps in pipeline 1, feed sewage, behind the solar radiation 10h, the SS concentration and the COD value that record the water in first cell body 4 are seen table 1.
The silica sand (median size 300 μ m, degree of sphericity 0.7) and the 5 weight part epoxy adhesives of 100 weight parts are mixed, obtain mixture; And being laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 8cm; Under 80 ℃, 20-40% relative humidity, solidified 12 hours, obtain second plate-like piece 3, wherein; The coefficient of permeability of second plate-like piece 3 is 0.07cm/s, and thickness is 8cm, and the aperture is 100-200 μ m.
Second plate-like piece 3 has been tiled on the sunlit level ground, and transmittance is set above that being 85% plastic film, making plastic film become 30 ° of angles with the level ground, is 5-45cm to vertical range of plastic film a bit arbitrarily on second plate-like piece 3.
An end higher at plastic film is provided with pipeline 1, and pipeline 1 all between the plastic film and second plate-like piece 3, is provided with opening on the pipeline 1, on pipeline 1, baffle plate is set, and baffle plate and plastic film are 20 ° than the angle between the low side.
Below the low end of plastic film, first cell body 4 is set, second cell body, 5, the second cell bodies 5 is set below second plate-like piece 3 is communicated with pipeline 1, and in second cell body 5, a water pump is set, water pump can be with in the water pump return pipe road 1 in second cell body 5.
In pipeline 1, feed seawater, behind the solar radiation 10h, the salinity that records the water in first cell body 4 is seen table 1.
Perhaps in pipeline 1, feed sewage, behind the solar radiation 10h, the SS concentration and the COD value that record the water in first cell body 4 are seen table 1.
Table 1
| Embodiment | Salinity (‰) | SS concentration (mg/L) | COD value (mg/L) |
| 1 | 0.4 | 12 | 3 |
| 2 | 0.2 | 8 | 2.8 |
| 3 | 0.6 | 16 | 3.6 |
From table 1, can find out; Sea water desaltination that the utility model provides or effluent treatment plant can play good sea water desaltination or sewage purification effect; And sea water desaltination or effluent treatment plant that the utility model provides are simple in structure, utilize sunshine to accomplish sea water desaltination or sewage purification process, have practiced thrift production and operation cost; Under the preferable case; Second plate-like piece of sea water desaltination of the utility model or effluent treatment plant forms the silica sand adhesive solidification through sticker, has successfully realized the sand of low cost and wide material sources is applied to sea water desaltination or sewage purification, has further practiced thrift production cost.Sea water desaltination that the utility model provides or effluent treatment plant can be widely used in water resources and handle the field.
Claims (12)
1. sea water desaltination or effluent treatment plant; It is characterized in that; Said sea water desaltination or effluent treatment plant comprise pipeline, first plate-like piece and second plate-like piece, and said first plate-like piece is obliquely installed and makes an end of said first plate-like piece be higher than the other end, and said first plate-like piece is positioned at said second plate-like piece top; The material of said first plate-like piece is a light transmissive material; Said second plate-like piece has water-holding power, and said pipeline has a plurality of openings, and the position of said pipeline and the direction of opening make seawater or the sewage in the pipeline partly or entirely can flow on said second plate-like piece.
2. sea water desaltination according to claim 1 or effluent treatment plant; It is characterized in that; Said pipeline is positioned at the higher end of said first plate-like piece; And contact with said second plate-like piece with said first plate-like piece, the opening of said pipeline is arranged between said first plate-like piece and said second plate-like piece.
3. sea water desaltination according to claim 1 and 2 or effluent treatment plant is characterized in that, the thickness of said second plate-like piece is 5-15cm.
4. sea water desaltination according to claim 1 and 2 or effluent treatment plant is characterized in that, the aperture of said second plate-like piece is 50-200 μ m.
5. sea water desaltination according to claim 1 and 2 or effluent treatment plant, wherein, said first plate-like piece is plastics or glass.
6. sea water desaltination according to claim 1 and 2 or effluent treatment plant is characterized in that, the angle of said first plate-like piece and horizontal plane is 10-30 °.
7. sea water desaltination according to claim 1 and 2 or effluent treatment plant is characterized in that, any some vertical range to said first plate-like piece is 5-45cm on said second plate-like piece.
8. sea water desaltination according to claim 1 and 2 or effluent treatment plant; It is characterized in that; Said sea water desaltination or effluent treatment plant also comprise the baffle plate that is arranged between said first plate-like piece and said second plate-like piece, and said baffle plate is used to stop seawater or sewage in the pipeline to flow to said first plate-like piece.
9. sea water desaltination according to claim 8 or effluent treatment plant; It is characterized in that; One end of said baffle plate is arranged on the part between said first plate-like piece and said second plate-like piece or with the position A of said first plate-like piece, being tightly connected of said pipeline; The minor increment m of said position A between the said first plate-like piece higher-end and said position the A extremely ratio than the minor increment M between the low side of said first plate-like piece are 0-0.1: 1; Said baffle plate and said first plate-like piece be a than the angle between the low side, the angle of said first plate-like piece and horizontal plane and a sum are less than 90 °, and a is greater than 0 °.
10. sea water desaltination according to claim 1 and 2 or effluent treatment plant; It is characterized in that; Said sea water desaltination or effluent treatment plant also comprise first cell body that is used to receive the water that flows down from said first plate-like piece, and said first cell body is positioned at the below of a lower end of said first plate-like piece.
11. sea water desaltination according to claim 1 and 2 or effluent treatment plant; It is characterized in that; Said sea water desaltination or effluent treatment plant also comprise second cell body that is used to receive unabsorbed seawater of said second plate-like piece or sewage, and said second cell body is positioned at the below of said second plate-like piece.
12. sea water desaltination according to claim 11 or effluent treatment plant; It is characterized in that; Said second cell body is communicated with said pipeline, and said sea water desaltination or effluent treatment plant comprise that also the water cycle that can make in second cell body returns said ducted pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202748555U CN202193639U (en) | 2011-07-29 | 2011-07-29 | Device for desalinizing sea water or purifying sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202748555U CN202193639U (en) | 2011-07-29 | 2011-07-29 | Device for desalinizing sea water or purifying sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202193639U true CN202193639U (en) | 2012-04-18 |
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ID=45948560
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202748555U Expired - Fee Related CN202193639U (en) | 2011-07-29 | 2011-07-29 | Device for desalinizing sea water or purifying sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202193639U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897858A (en) * | 2011-07-29 | 2013-01-30 | 北京仁创科技集团有限公司 | Seawater desalination or sewage purification device |
-
2011
- 2011-07-29 CN CN2011202748555U patent/CN202193639U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897858A (en) * | 2011-07-29 | 2013-01-30 | 北京仁创科技集团有限公司 | Seawater desalination or sewage purification device |
| CN102897858B (en) * | 2011-07-29 | 2016-04-27 | 北京仁创科技集团有限公司 | A kind of sea water desaltination or effluent treatment plant |
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