The preparation method of a kind of sea water desaltination or effluent treatment plant
Technical field
The present invention relates to a kind of preparation method of water treatment device, particularly, relate to the preparation method of 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 desalinating plant all exists complex structure, problem that cost is 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, problem that cost is higher.
Summary of the invention
The objective of the invention is provides a kind of new sea water desaltination or the preparation method of effluent treatment plant in order to overcome existing sea water desaltination or effluent treatment plant complex structure, problem that cost is higher.
To achieve these goals, the invention provides the preparation method of a kind of sea water desaltination or effluent treatment plant, it is characterized in that, described method comprises:
(1) binding agent and silica sand are mixed and curing molding to form the second plate-like piece;
(2) the first plate-like piece is inclined at the top of described the second plate-like piece, makes an end of described the first plate-like piece be higher than the other end, the material of described the first plate-like piece is light transmissive material;
(3) at pipeline a plurality of openings are set, the position of described pipeline and the direction of opening so that described pipeline in seawater or sewage partly or entirely can flow on described the second plate-like piece.
Preferably, described install pipeline at the higher end of described the first plate-like piece, and is contacted with described the second plate-like piece with described the first plate-like piece, the opening of described pipeline is arranged between described the first plate-like piece and described the second plate-like piece.
The preparation method of sea water desaltination provided by the invention or effluent treatment plant, simple, saved production and operation cost; The inventive method forms the second plate-like piece with water-holding power by binding agent with the silica sand adhesive solidification, has successfully realized the sand of low cost and wide material sources is applied to sea water desaltination or sewage purification, has further saved production cost; The inventive method can be widely used in water resources and process the field.
Other features and advantages of the present invention will partly be described in detail in embodiment subsequently.
Description of drawings
Fig. 1 is sea water desaltination prepared according to the methods of the invention or the structural representation of effluent treatment plant.
Fig. 2 is the sea water desaltination with the first cell body and second cell body prepared according to the methods of the invention 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
Below in conjunction with accompanying drawing the specific embodiment of the present invention is elaborated.Should be understood that embodiment described herein only is used for description and interpretation the present invention, is not limited to the present invention.
As shown in Figure 1, the invention provides the preparation method of a kind of sea water desaltination or effluent treatment plant, described method comprises:
(1) binding agent and silica sand are mixed and curing molding to form the second plate-like piece 3;
(2) the first plate-like piece 2 is inclined at the top of described the second plate-like piece 3, makes an end of described the first plate-like piece 2 be higher than the other end, the material of described the first plate-like piece 2 is light transmissive material;
(3) at pipeline 1 a plurality of openings are set, the position of pipeline 1 and the direction of opening so that seawater or sewage in the pipeline 1 partly or entirely can flow on the second plate-like piece 3.
Although binding agent and silica sand are mixed also curing molding, can form the second plate-like piece 3 with water-holding power, but in order to make the second plate-like piece 3 can have good water-holding power, and can take full advantage of again the heat energy of irradiation, the thickness that the second plate-like piece 3 is laid is preferably 5-15cm, more preferably 8-10cm.
Among the present invention, the median size of silica sand is preferably 100-400 μ m, 200-300 μ m more preferably, and the weight ratio of binding agent and silica sand is preferably 1-15: 100,5-10 more preferably: 100.Without particular requirement, can be various silica sands for the kind of silica sand, for example can be selected from quartz sand, drift-sand, artificial sand, reclaimed sand, river sand, extra large sand and the mountain sand one or more.The degree of sphericity of silica sand is better, 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 silica sand of the present invention 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 degree of sphericity requirement of the presently claimed invention, can adopt and silica sand be carried out the needs that the control methods known in those skilled in the art such as ball milling satisfy the silica sand degree of sphericity.
Among the present invention, binding agent can be this area various binding agents commonly used, is preferably in Resins, epoxy, polyvinylidene fluoride resin, water glass, resol, acrylic resin, polyurethane resin and the silicate cement one or more.
The first plate-like piece 2 is light transmissive material, and transmittance is preferably 85-95%, and the printing opacity among the present invention refers to through sunlight.Transmittance adopts GB/T2410-2008 to measure.In order further to reduce cost, the first plate-like piece 2 is preferably plastics or glass.
The first plate-like piece 2 is obliquely installed makes an end of the first plate-like piece 2 be higher than the other end, in order to make the first plate-like piece 2 have larger sunlight transmission plane to make again easier the flowing down of water of condensation on the first plate-like piece 2, the first plate-like piece 2 is preferably 10-30 ° with the angle of horizontal plane.The method that is obliquely installed for the first plate-like piece 2 is without particular requirement, can adopt this area the whole bag of tricks commonly used, for example the first plate-like piece 2 oblique cuttings can be entered in the earth fixing, also can arrange one hangs and establishes device, one end of the 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 the first plate-like piece 2 is set up in the strut member setting that tilts.Without particular requirement, as long as make the second plate-like piece 3 be positioned at the below of the first plate-like piece 2, slant setting can be for the set-up mode of the second plate-like piece 3, also horizontal positioned can be.
As long as the distance between the first plate-like piece 2 and the second plate-like piece 3 makes the water that condenses on the first plate-like piece 2 not by the sewage pollution that absorbs in the second plate-like piece 3, under the preferable case, any point is 5-45cm to the vertical range of the first plate-like piece 2 on the second plate-like piece 3.
Under the preferable case, pipeline 1 is arranged on the higher end of the first plate-like piece 2, and contacts with the second plate-like piece 3 with the first plate-like piece 2, the opening of pipeline 1 is arranged between the first plate-like piece 2 and the second plate-like piece 3.For the set-up mode of pipeline 1 without particular requirement, can adopt this area various set-up modes commonly used, as long as make pipeline 1 be positioned at the higher end of the first plate-like piece 2, and at least part ofly between the first plate-like piece 2 and the second plate-like piece 3, get final product, for example a strut member can be set, pipeline 1 is fixed on the strut member, also can arranges one and hang and establish device, pipeline 1 is hung be located on the desired position.
Under the preferable case, the direction of opening so that seawater or sewage in the pipeline 1 all flow on the second plate-like piece 3.For seawater or sewage in the pipeline 1 are as far as possible all flow on the second plate-like piece 3, under the preferable case, the inventive method also is included between the first plate-like piece 2 and the second plate-like piece 3 the baffle plate (not shown) is set, and described baffle plate is used for stoping seawater or sewage in the pipeline 1 to flow to the first plate-like piece 2.One end of baffle plate can be arranged on pipeline 1 on the part between the first plate-like piece 2 and the second plate-like piece 3, perhaps can be tightly connected with the position A of the first plate-like piece 2.For seawater or sewage in the pipeline 1 are as far as possible all flow on the second plate-like piece 3, 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, baffle plate and the first plate-like piece 2 be a than the angle between the low side, the angle of the first plate-like piece 2 and horizontal plane and a sum are less than 90 °, and a is greater than 0 °.For the size and shape of opening without particular requirement, can the setup cost those skilled in the art thinkable all size of institute and shape, as long as can realize purpose of the present invention.
Without particular requirement, can adopt this area different shape and material commonly used for the shape of pipeline 1 and material.
For the seawater after the convenient collection desalination or the sewage after the purification, as shown in Figure 2, the below that the inventive method also is included in a lower end of the first plate-like piece 2 arranges the first cell body 4, makes the first cell body 4 be used for receiving the water that flows down from the first plate-like piece 2.Without particular requirement, can adopt this area all size, shape and material commonly used, as long as can receive the water that flows down from the first plate-like piece 2 for size, shape and the material of the first cell body 4.
Preferably, the below that the inventive method also is included in the second plate-like piece 3 arranges the second cell body 5, makes the second cell body 5 be used for receiving the second plate-like piece 3 unabsorbed seawater or sewage.Without particular requirement, can adopt this area all size, shape and material commonly used, as long as can receive the second plate-like piece 3 unabsorbed seawater or sewage for size, shape and the material of the second cell body 5.For seawater or sewage in the second cell body 5 can be processed again, under the preferable case, the inventive method also comprises the second cell body 5 is communicated with pipeline 1, and the water in the second cell body 5 can be looped back in the pipeline 1.The mode that is communicated with pipeline 1 for the second cell body 5 can be this area variety of way commonly used without particular requirement.Without particular requirement, can adopt this area the whole bag of tricks commonly used for the method in the water cycle return pipe road 1 in the second cell body 5, for example a water pump can be set, by water pump with in the seawater in the second cell body 5 or the sump pump return pipe road 1.
When the sea water desaltination of the inventive method preparation or the actual use of effluent treatment plant, be placed on the solar radiation place and get final product.Seawater in the pipeline 1 or sewage flow in the second plate-like piece 3 with water-holding power, sunlight sees through the first plate-like piece 2 and shines on the second plate-like piece 3, the second plate-like piece 3 absorbing heats, make the moisture evaporation in the second plate-like piece 3, condensation after moisture is evaporated on the first plate-like piece 2, condensed water is dirty along the gradient that is obliquely installed of the first plate-like piece 2, and the high boiling point impurity such as salt in seawater or the sewage then can not be evaporated on the first plate-like piece 2, finishes sea water desaltination or sewage purification process.Preferably, flow into along the dirty water of the gradient that is obliquely installed of the first plate-like piece 2 in the first cell body 4 of the below of hanging down an end that is arranged on the first plate-like piece 2, the seawater or the sewage inflow that are not absorbed by the second plate-like piece 3 are arranged in the second cell body 5 of the second plate-like piece 3 belows, and the water in the second cell body 5 is back in the pipeline 1 under the effect of water pump.
Be not difficult to find out that by above-mentioned principle the sea water desaltination of the inventive method preparation or effluent treatment plant can be higher than the water resources that water or volatility are lower than the impurity of water for the treatment of the various boiling points that contain, such as seawater or various industry or sanitary wastewater.
Below describe by reference to the accompanying drawings preferred implementation of the present invention in detail; but; the present invention is not limited to the detail in the above-mentioned embodiment; in technical conceive scope of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.
Need to prove in addition, each concrete technical characterictic described in above-mentioned embodiment in reconcilable situation, can make up by any suitable mode, for fear of unnecessary repetition, the present invention is to the no longer separately explanation of various possible array modes.
In addition, also can carry out arbitrary combination between the various embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.
Embodiment
Following embodiment will the present invention is further illustrated, but therefore do not limit the present invention.
In the following embodiments:
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 by 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 ℃, then weighing is dried to the weight of the solid matter of constant weight, with the weight of the solid matter volume divided by the water sample by filter membrane, namely get SS concentration, measure unit is mg/L.
Adopt the method for GB/T 22597-2008 to measure the COD value.COD is that chemical oxygen demand (COD) claims again chemical oxygen demand, to utilize chemical oxidizing agent (such as potassium permanganate) with an oxidisable substance in the water (such as organism, nitrite, ferrous salt, sulfide etc.) oxygenolysis, then calculate the consumption of oxygen according to the amount of residual oxygenant, be the important indicator of expression water pollution degree, measure unit is mg/L.
In following examples, quartz sand is available from blue sky, Yongdeng quartz sand company limited.
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 sanitary sewage from the residential quarter, SS concentration 326mg/L, COD value 300mg/L.
Embodiment 1
Quartz sand (median size 250 μ m with 100 weight parts, degree of sphericity 0.7) and 8 weight part epoxy adhesives mix, obtain mixture, and be laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 10cm, solidifies 12 hours under 80 ℃, 20-40% relative humidity, obtains the second plate-like piece 3, wherein, the coefficient of permeability of the second plate-like piece 3 is 0.03cm/s, and thickness is 10cm, and the aperture is 80-150 μ m.
The second plate-like piece 3 has been lain on the sunlit level ground, and transmittance is set is 90% plastic film that make plastic film become 20 ° of angles with the level ground, any point is 5-35cm to the vertical range of plastic film on the second plate-like piece 3 thereon.
An end higher at plastic film arranges pipeline 1, and pipeline 1 all between plastic film and the second plate-like piece 3, arranges opening on the pipeline 1, at 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 the first cell body 4 is set, the second cell body 5, the second cell bodies 5 is set below the second plate-like piece 3 is communicated with pipeline 1, and in the second cell body 5 water pump is set, water pump can be with in the water pump return pipe road 1 in the second cell body 5.
Pass into seawater in pipeline 1, behind the solar radiation 10h, the salinity that records the water in the first cell body 4 sees Table 1.
Perhaps pass into sewage in pipeline 1, behind the solar radiation 10h, the SS concentration and the COD value that record the water in the first cell body 4 see Table 1.
Embodiment 2
Quartz sand (median size 200 μ m with 100 weight parts, degree of sphericity 0.8) and 10 weight part epoxy adhesives mix, obtain mixture, and be laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 9cm, solidifies 12 hours under 80 ℃, 20-40% relative humidity, obtains the second plate-like piece 3, wherein, the coefficient of permeability of the second plate-like piece 3 is 0.05cm/s, and thickness is 9cm, and the aperture is 50-100 μ m.
The second plate-like piece 3 has been tiled on the sunlit level ground, and transmittance is set is 95% plastic film that make plastic film become 10 ° of angles with the level ground, any point is 5-20cm to the vertical range of plastic film on the second plate-like piece 3 thereon.
An end higher at plastic film arranges pipeline 1, and pipeline 1 all between plastic film and the second plate-like piece 3, arranges opening on the pipeline 1, at 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 the first cell body 4 is set, the second cell body 5, the second cell bodies 5 is set below the second plate-like piece 3 is communicated with pipeline 1, and in the second cell body 5 water pump is set, water pump can be with in the water pump return pipe road 1 in the second cell body 5.
Pass into seawater in pipeline 1, behind the solar radiation 10h, the salinity that records the water in the first cell body 4 sees Table 1.
Perhaps pass into sewage in pipeline 1, behind the solar radiation 10h, the SS concentration and the COD value that record the water in the first cell body 4 see Table 1.
Embodiment 3
Quartz sand (median size 300 μ m with 100 weight parts, degree of sphericity 0.7) and 5 weight part epoxy adhesives mix, obtain mixture, and be laid on long 90cm, in the rectangular die of wide 60cm, laying depth is 8cm, solidifies 12 hours under 80 ℃, 20-40% relative humidity, obtains the second plate-like piece 3, wherein, the coefficient of permeability of the second plate-like piece 3 is 0.07cm/s, and thickness is 8cm, and the aperture is 100-200 μ m.
The second plate-like piece 3 has been tiled on the sunlit level ground, and transmittance is set is 85% plastic film that make plastic film become 30 ° of angles with the level ground, any point is 5-45cm to the vertical range of plastic film on the second plate-like piece 3 thereon.
An end higher at plastic film arranges pipeline 1, and pipeline 1 all between plastic film and the second plate-like piece 3, arranges opening on the pipeline 1, at 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 the first cell body 4 is set, the second cell body 5, the second cell bodies 5 is set below the second plate-like piece 3 is communicated with pipeline 1, and in the second cell body 5 water pump is set, water pump can be with in the water pump return pipe road 1 in the second cell body 5.
Pass into seawater in pipeline 1, behind the solar radiation 10h, the salinity that records the water in the first cell body 4 sees Table 1.
Perhaps pass into sewage in pipeline 1, behind the solar radiation 10h, the SS concentration and the COD value that record the water in the first cell body 4 see 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 |
As can be seen from Table 1, sea water desaltination or the effluent treatment plant of the inventive method preparation can play good sea water desaltination or sewage purification effect.The preparation method of sea water desaltination provided by the invention or effluent treatment plant, simple, saved production and operation cost; The inventive method with the silica sand adhesive solidification, forms the second plate-like piece with water-holding power by binding agent, has successfully realized the sand of low cost and wide material sources is applied to sea water desaltination or sewage purification, has further saved production cost; The inventive method can be widely used in water resources and process the field.