CN203741144U - Integrated device for desalting and pre-treating seawater - Google Patents
Integrated device for desalting and pre-treating seawater Download PDFInfo
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- CN203741144U CN203741144U CN201320840115.2U CN201320840115U CN203741144U CN 203741144 U CN203741144 U CN 203741144U CN 201320840115 U CN201320840115 U CN 201320840115U CN 203741144 U CN203741144 U CN 203741144U
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 78
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Removal Of Floating Material (AREA)
Abstract
The utility model discloses an integrated device for desalting and pre-treating seawater. The integrated device comprises a water inlet pipe, a water outlet pipe, a master sludge discharge pipe, a coagulation area, a water distributing area, a water-air contact area, a sludge-water separating area, a clear water outlet area and a plurality of sludge discharge branched pipes, wherein the coagulation area, the water distributing area, the water-air contact area, the sludge-water separating area and the clear water outlet area are sequentially matched between the water inlet pipe and the water outlet pipe; the plurality of sludge discharge branched pipes serve as the branches of the master sludge discharge pipe, and are respectively matched into sludge buckets at the bottom parts of the coagulation area, the water distributing area, the water-air contact area, the sludge-water separating area and the clear water outlet area. With the adoption of the integrated device for desalting and pre-treating sweater, the defects of poor working stability, low water production efficiency, high operation cost and the like in the prior art can be overcome, and the advantages of high working stability, high water production efficiency and low operation cost can be realized.
Description
Technical field
The utility model relates to water treating equipment technical field, particularly, relates to a kind of sea water desaltination pre-treatment integrated apparatus.
Background technology
At present, the seawater cleaning treatment process in domestic embrane method Seawater Desalination Project has: " coagulation+precipitation+filtration " technique, " coagulation+air supporting+filtration " technique, " clarification+filtration " technique, " coagulation+floating depositing pool+filtration " etc.The pollution substances such as turbidity in the seawater after purification process technique, colloid, algae, oils, organism are effectively removed, then enter reverse osmosis membrane system and carry out desalting processing.
But domestic marine site is vast, seawater quality is complicated and changeable, as: be subject to the turbidity of sea water fluctuation that stormy waves and rainfall cause, the alga eruption that seawater eutrophication causes, floating pollution by oil, the low turbid phenomenon of northern marine site winter low temperature etc.Due to the fluctuation of seawater quality, make reverse osmosis membrane desalination process cannot steady in a long-termly move, even occur the problems such as producing water ratio decline, membrane lifetime shortening, running cost rising.
Realizing in process of the present utility model, contriver finds at least to exist in prior art poor work stability, produce the defects such as the low and running cost of water efficiency is high.
Utility model content
The purpose of this utility model is, for the problems referred to above, proposes a kind of sea water desaltination pre-treatment integrated apparatus, to realize good operating stability, to produce the advantage that water efficiency is high and running cost is low.
For achieving the above object, the technical solution adopted in the utility model is: a kind of sea water desaltination pre-treatment integrated apparatus, comprise water inlet pipe, rising pipe and spoil disposal house steward, be equipped with successively coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district between described water inlet pipe and rising pipe, and as described spoil disposal house steward's branch and be equipped with respectively the multiple spoil disposal arms in described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and bottom, clarification and effluent district bucket.
Further, described coagulation district, comprise close described water inlet pipe setting and the mixing pit being communicated with water inlet pipe, near described mixing pit setting and for carrying out multiple nonmetal grid or the grid packing assembly of waterpower flocculation, and be arranged on described multiple nonmetal grid or grid packing assembly away from the upper end of mixing pit one side and the water side that is communicated with cloth pool;
In described mixing pit, be provided with the dicyclo umbrella aeration head for adopting the blast aeration of dicyclo umbrella to stir; In described water inlet pipe, mixing pit, multiple nonmetal grid or grid packing assembly, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, be provided with the multiple water holes of crossing that are communicated with successively; Be positioned at multiple spoil disposal arms in coagulation district, be separately positioned on the bottom of multiple nonmetal grids or grid packing assembly below bucket.
Further, above described water inlet pipe, be provided with the aeration tube that is communicated to described dicyclo umbrella aeration head; Below described water inlet pipe, be provided with successively reuse water pipe and mud return line.
Further, described cloth pool, comprises cloth pond, and the water inlet that is arranged on upper end, described cloth pond and is communicated with coagulation district is arranged on the water outlet of lower end, described cloth pond, and the water distribution hoarding of water distribution grid is set in vertical direction layering;
Described water outlet, is communicated with aqueous vapor zone of action by the water distribution hoarding that is positioned at lower floor; Be positioned at multiple spoil disposal arms in cloth pool, be separately positioned on the bottom of laminates boom wall below bucket.
Further, described aqueous vapor zone of action, comprise aqueous vapor contact tank, the water inlet that is arranged on described aqueous vapor contact tank lower end and is communicated with cloth pool, and arrange and for by the separated training wall of aqueous vapor contact tank and mud-water separation district near described mud-water separation district;
In the bottom of described aqueous vapor contact tank, be provided with the dissolved air release of non-metallic material; At the top of described aqueous vapor contact tank, be provided with the multiple dissolved air water water inlet pipes that are communicated to described dissolved air release; Described multiple dissolved air water water inlet pipe is positioned at the pipeline of water surface top, adopts flange to connect; Be positioned at multiple spoil disposal arms of aqueous vapor zone of action, be separately positioned on the bottom of bucket in aqueous vapor contact tank.
Further, match with described dissolved air release, be provided with multiple water distribution grid.
Further, described mud-water separation district, comprise mud-water separation pond, the vertically parallel multiple water sides training wall being arranged in described mud-water separation pond, be horizontally set on the swash plate installing zone of training wall top, described multiple water sides, be positioned at described swash plate installing zone top and be arranged on the scum machine of scraping on top, mud-water separation pond, and be close to described swash plate installation region end, with scrape scum machine and match and be arranged on the enlarging scum silica frost receiving tank of upper end, mud-water separation pond;
Below the water surface of described swash plate installing zone, multiple non-metallic material swash plates are installed; Be positioned at multiple spoil disposal arms in mud-water separation district, be separately positioned on the bottom of training wall below, multiple water sides bucket; Clear water enters clarification and effluent district at described swash plate layout area end through the water hole of crossing under water.
Further, described in scrape scum machine, comprise that the running type that is arranged on water surface top scrapes scum silica frost equipment; This running type is scraped scum silica frost equipment, the scum silica frost scraper plate that the part contacting with the water surface is quality of rubber materials;
On described enlarging scum silica frost receiving tank, be provided with the adjustable round crested weir for adjust operation water level.
Further, described clarification and effluent district, comprises settling pond, is arranged in the inclined tube installing zone in described settling pond, is located at described settling pond top and the adjustable effluent overflow weir water for adjust operation water level; At described inclined tube installing zone, the non-metallic material inclined tube for uniform water distribution and shallow layer precipitating is installed.
Further, described spoil disposal house steward and multiple spoil disposal arm, specifically comprise for the perforated pipe by gravity spoil disposal;
And/or,
Described spoil disposal house steward and multiple spoil disposal arm, specifically comprise for by the perforated pipe of gravity spoil disposal, and be connected with described perforated pipe and for aspirating the sludge pump of spoil disposal.
Further, described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, with wide and same high setting; In the bottom in described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, uniform bucket and nonmetal perforated pipe spoil disposal.
The sea water desaltination pre-treatment integrated apparatus of the each embodiment of the utility model, owing to comprising water inlet pipe, rising pipe and spoil disposal house steward, be equipped with successively coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district between water inlet pipe and rising pipe, and as spoil disposal house steward's branch and be equipped with respectively the multiple spoil disposal arms in coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and bottom, clarification and effluent district bucket; Coagulation, air supporting, three PROCESS COUPLING of precipitation can be completed in a device, both ensure that technique operation steady in a long-term, the effluent quality in seawater cleaning process is good; Can at utmost reduce again working cost; Reduce use, reduction facility investment and the maintenance cost of submarine mechanical equipment; Thereby can overcome poor work stability in prior art, produce the defect that water efficiency is low and running cost is high, to realize good operating stability, to produce the advantage that water efficiency is high and running cost is low.
Other features and advantages of the utility model will be set forth in the following description, and, partly from specification sheets, become apparent, or understand by implementing the utility model.
Below by drawings and Examples, the technical solution of the utility model is described in further detail.
Brief description of the drawings
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for specification sheets, is used from explanation the utility model with embodiment mono-of the present utility model, does not form restriction of the present utility model.In the accompanying drawings:
Fig. 1 is the two dimensional structure schematic diagram of the utility model sea water desaltination pre-treatment integrated apparatus;
Fig. 2 be in Fig. 1 A-A to sectional structure schematic diagram;
Fig. 3 be in Fig. 1 B-B to sectional structure schematic diagram (mud-water separation district under water cross water hole);
Fig. 4 be in Fig. 1 C-C to sectional structure schematic diagram (mud-water separation district water side diversion trench and enlarging scum silica frost receiving tank);
Fig. 5 be in Fig. 1 D-D to sectional structure schematic diagram (mud-water separation district training wall);
Fig. 6 be in Fig. 1 E-E to sectional structure schematic diagram (aqueous vapor zone of action water distribution hoarding);
Fig. 7 be in Fig. 1 F-F to sectional structure schematic diagram;
Fig. 8 is the local enlarged diagram (enlarging scum silica frost receiving tank and adjustable round crested weir) of A portion in Fig. 2;
Fig. 9 be in Fig. 8 1-1 to local structure schematic diagram;
Figure 10 is the local enlarged diagram (adjustable effluent overflow weir water) of B portion in Fig. 3;
Figure 11 be in Figure 10 2-2 to sectional structure schematic diagram.
By reference to the accompanying drawings, in the utility model embodiment, Reference numeral is as follows:
1-spoil disposal house steward; 2-rising pipe; 3-effluent overflow weir water; 4-enlarging scum silica frost receiving tank; 5-dissolved air water water inlet pipe; 6-dissolved air release; 7-dicyclo umbrella aeration head; 8-water inlet pipe, reuse water pipe, mud return line; 81-water inlet pipe; 82-reuse water pipe; 83-mud return line; 9-aeration tube; 10-scrapes scum machine; 11-swash plate installing zone; 12-row scum silica frost pipe; 13-is adjustable effluent overflow weir water; 14-inclined tube installing zone; 15-grid or grid packing installing zone; 16-crosses water hole; 17-water distribution grid; 18-water side training wall; 19-crosses water hole under water; 20-spoil disposal arm; 21-training wall; 22-crosses water hole; 23-bolt hole (slotted hole).
By reference to the accompanying drawings, in the utility model embodiment, accompanying drawing legend is as follows:
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for description and interpretation the utility model, and be not used in restriction the utility model.
According to the utility model embodiment, as Figure 1-Figure 11, a kind of sea water desaltination pre-treatment integrated apparatus is provided, coagulation, air supporting, three PROCESS COUPLING of precipitation have been completed in a device, both ensured that technique operation steady in a long-term, the effluent quality in seawater cleaning process is good; Can at utmost reduce again working cost; Reduce use, reduction facility investment and the maintenance cost of submarine mechanical equipment.
The sea water desaltination pre-treatment integrated apparatus of the present embodiment, comprise water inlet pipe (as water inlet pipe 81), rising pipe (as rising pipe 2) and spoil disposal house steward (as spoil disposal house steward 1), be equipped with successively coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district between water inlet pipe and rising pipe, and as spoil disposal house steward's branch and be equipped with respectively the multiple spoil disposal arms (as spoil disposal arm 20) in coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and bottom, clarification and effluent district bucket.
Here, coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, with wide and same high setting; In coagulation district, bottom, uniform bucket and the nonmetal perforated pipe spoil disposal in cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district.Spoil disposal house steward and multiple spoil disposal arm, specifically comprise for the perforated pipe by gravity spoil disposal; And/or spoil disposal house steward and multiple spoil disposal arm, specifically comprise for by the perforated pipe of gravity spoil disposal, and be connected with perforated pipe and for aspirating the sludge pump of spoil disposal.
Particularly, above-mentioned coagulation district, comprise close water inlet pipe setting and the mixing pit being communicated with water inlet pipe, near mixing pit setting and for carrying out multiple nonmetal grid or the grid packing assembly (multiple nonmetal grids or grid packing assembly are arranged on grid or grid packing installing zone 15) of waterpower flocculation, and be arranged on multiple nonmetal grids or grid packing assembly away from the upper end of mixing pit one side and the water side that is communicated with cloth pool; In mixing pit, be provided with the dicyclo umbrella aeration head (as dicyclo umbrella aeration head 7) for adopting the blast aeration of dicyclo umbrella to stir; In water inlet pipe, mixing pit, multiple nonmetal grid or grid packing assembly, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, be provided with the multiple water holes (as crossed water hole 16, cross water hole 22 and crossing water hole 19 under water) of crossing that are communicated with successively; Be positioned at multiple spoil disposal arms in coagulation district, be separately positioned on the bottom of multiple nonmetal grids or grid packing assembly.Above water inlet pipe, be provided with the aeration tube (as aeration tube 9) that is communicated to dicyclo umbrella aeration head; Below water inlet pipe, be provided with successively reuse water pipe (as reuse water pipe 82) and mud return line (as mud return line 83).
Above-mentioned cloth pool, comprises cloth pond, and the water inlet that is arranged on upper end, cloth pond and is communicated with coagulation district is arranged on the water outlet of lower end, cloth pond, and the laminates boom wall arranging in vertical direction layering; Water outlet, is communicated with aqueous vapor zone of action by the cloth waterwall grid that are positioned at lower floor; Be positioned at multiple spoil disposal arms in cloth pool, be separately positioned on the bottom of laminates boom wall below bucket.
Above-mentioned aqueous vapor zone of action, comprises aqueous vapor contact tank, the water inlet that is arranged on aqueous vapor contact tank lower end and is communicated with cloth pool, and arrange and for by the separated training wall of aqueous vapor contact tank and mud-water separation district (as training wall 21) near mud-water separation district; In the bottom of aqueous vapor contact tank, be provided with dissolved air release (as dissolved air release 6); At the top of aqueous vapor contact tank, be provided with the multiple dissolved air water water inlet pipes (as dissolved air water water inlet pipe 5) that are communicated to dissolved air release; Multiple dissolved air water water inlet pipes are positioned at the pipeline of water surface top, adopt flange to connect; Be positioned at multiple spoil disposal arms of aqueous vapor zone of action, be separately positioned on the bottom of aqueous vapor contact tank below bucket.Match with dissolved air release, be provided with multiple water distribution grid (as water distribution grid 17).
Above-mentioned mud-water separation district, comprise mud-water separation pond, the vertically parallel multiple water sides training wall (as water side training wall 18) being arranged in mud-water separation pond, be horizontally set on the swash plate installing zone (as swash plate installing zone 11) of training wall top, multiple water sides, be positioned at swash plate installing zone top, and what be arranged on top, mud-water separation pond scrapes scum machine (as scraping scum machine 10), and next-door neighbour swash plate installation region end, with scrape scum machine and match and be arranged on the enlarging scum silica frost receiving tank (as enlarging scum silica frost receiving tank 4) of upper end, mud-water separation pond, be equipped with row's scum silica frost pipe (as row's scum silica frost pipe 12) with enlarging scum silica frost receiving tank, below the water surface of swash plate installing zone, multiple non-metallic material swash plates are installed, be positioned at multiple spoil disposal arms in mud-water separation district, be separately positioned on the bottom of training wall below, multiple water sides bucket, clear water enters clarification and effluent district at swash plate layout area end through the water hole of crossing under water.Scrape scum machine, comprise that the running type that is arranged on water surface top scrapes scum silica frost equipment; This running type is scraped scum silica frost equipment, the scum silica frost scraper plate that the part contacting with the water surface is quality of rubber materials; On enlarging scum silica frost receiving tank, be provided with the adjustable round crested weir (being effluent overflow weir water 3) for adjust operation water level.At enlarging scum silica frost receiving tank and adjustable round crested weir, be provided with the bolt hole (as bolt hole 23) of slotted hole shape.
Above-mentioned clarification and effluent district, comprises settling pond, is arranged in the inclined tube installing zone (as inclined tube installing zone 14) in settling pond, is located at settling pond top and the adjustable effluent overflow weir water (as adjustable effluent overflow weir water 13) for adjust operation water level; At inclined tube installing zone, the non-metallic material inclined tube for uniform water distribution and shallow layer precipitating is installed.
The sea water desaltination pre-treatment integrated apparatus of above-described embodiment, can be divided into coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district 5 major parts by horizontal direction, and each district is with wide, same to height, compact construction, complete combination.In coagulation district, former seawater with reuse waste water, backflow active sludge, chemical agent etc. after blast aeration stirring action fully mixes, then through doing the complete pulling flow type of the up-and-down reciprocating flocculation process that move, the connection of Yu Bu pool, water side, top; Cloth pool lower floor water side is communicated with aqueous vapor zone of action by water distribution hoarding; Aqueous vapor zone of action has training wall that itself and partial division of mud-water separation district are opened, and the seawater that enters aqueous vapor zone of action first does to pulling flow type motion, then with the horizontal pulling flow type mud-water separation district that flows through completely, completes mud-water separation; Clear water enters clarification and effluent district at swash plate layout area end through crossing water hole under water; Clear water needs upwards completely after inclined tube district water distribution uniformity, then through overflow weir water outlet.
In actual moving process, can the variation with integrated apparatus water inlet hydraulic load according to this sea water desaltination pre-treatment, height of weir by adjustable effluent overflow weir water in the adjustable round crested weir on enlarging scum silica frost receiving tank in mud-water separation district and clarification and effluent district regulates, control the operating water level in integrated apparatus for this sea water desaltination pre-treatment, guarantee that scum silica frost is smooth and easy, discharge efficiently.
The uniform bucket in bottom and the nonmetal perforated pipe spoil disposal of all subregions of integrated apparatus for this sea water desaltination pre-treatment, without configuration underwater mud scraper.Coagulation district front end, adopts the blast aeration of dicyclo umbrella to stir and mixes, and dicyclo umbrella cloth gas can be avoided the generation of latch up phenomenon; Rear end, coagulation district coordinates nonmetal grid or grid packing to carry out waterpower flocculation.Mud-water separation district water surface arranged beneath non-metallic material swash plate, strengthening mud-water separation efficiency; Water surface top arranges running type and scrapes scum silica frost equipment, guarantees scum silica frost noresidue, and the scum silica frost scraper plate contacting with liquid level is quality of rubber materials.Dissolved air water suction culvert and the dissolved air release of aqueous vapor zone of action are non-metallic material, above the water surface pipeline adopt flange connect, for convenience detach, safeguard, change.In clarification and effluent district, arrange non-metallic material inclined tube, the effect of existing upward flow uniform water distribution, has again shallow layer precipitating effect, guarantees lower suspension content in the water outlet of integrated apparatus top layer.
The sea water desaltination pre-treatment integrated apparatus of above-described embodiment, has following characteristics:
(1) this sea water desaltination pre-treatment can be divided into distribution sequence and the unitized construction form of coagulation district, cloth pool, aqueous vapor zone of action, 5 the composition subregions in mud-water separation district and clarification and effluent district by horizontal direction with integrated apparatus;
(2) coagulation district adopts blast aeration to stir, and the each strand of medium that enters this district fully mixed;
(3) the inclined tube setting in clarification and effluent district, assurance device top layer effluent quality is good, stable;
(4) mud-water separation district, adopts the design of enlarging scum silica frost receiving tank;
(5) the design of adjustable effluent overflow weir water in the adjustable round crested weir on enlarging scum silica frost receiving tank and clarification and effluent district, the operating water level in flexible adjusting device;
(6) under water without any metal material mechanical means design.
The sea water desaltination pre-treatment integrated apparatus of above-described embodiment, has the following advantages:
(1) this sea water desaltination pre-treatment integrated apparatus, is coupling in coagulation, air supporting, three technological processs of precipitation in a pond and completes, and is convenient to maintenance management; Farthest reduce the head loss of system, guaranteed that the alumen ustum flco that flocculation process forms can also keep good form entering behind aqueous vapor zone of action and mud-water separation district, can improve mud-water separation efficiency;
(2) this sea water desaltination pre-treatment form subregion with integrated apparatus by 5, each district with wide, with high, physical dimension is regular, be convenient to two covering devices altogether wall build jointly, reduce floor space, saving construction investment;
(3) air supporting precipitation process and separately precipitation process switchover operation at any time, guarantee that mud-water separation effect is still stable, and follow-up filtration procedure is played a very good protection under seawater quality condition complicated and changeable;
(4) adopt blast aeration to mix, the each strand of media such as former seawater, reuse waste water, backflow active sludge, chemical agent are fully mixed, reduce the investment of metal material mechanical means under water, reduce operation expense; Meanwhile, when this sea water desaltination pre-treatment is stopped transport with integrated apparatus, dicyclo umbrella aeration head also can not stop up;
(5) this sea water desaltination pre-treatment can be by the hydrostatic head in structures, through perforated pipe gravity spoil disposal with integrated apparatus bottom deposition; Also can adopt perforated pipe to connect sludge pump suction spoil disposal; The difference of two kinds of spoil disposal form visual technique waterpower elevations and site planning requires to select;
(6) be close to the enlarging scum silica frost receiving tank design of swash plate installation region end, guarantee in air supporting precipitation operational process, avoid because appearance part after a large amount of scum silica frost gatherings of liquid level sinks to affecting the problem of delivery turbidity;
(7) the water outlet of middle layer under water in mud-water separation district, be aided with again inclined tube water distribution and the overflow weir water outlet design in clarification and effluent district, guarantee no matter be precipitate operational process or precipitate separately operational process in air supporting, all can ensure the good effluent quality in top layer of this sea water desaltination pre-treatment integrated apparatus;
(8) the design of the adjustable effluent overflow weir water of the adjustable round crested weir on enlarging scum silica frost receiving tank and clarification and effluent district, can eliminate due to air supporting depositing technology with separately when depositing technology switchover operation or the disadvantageous effect of the flooding quantity fluctuation level fluctuation that causes hydraulic load to change causing to scum silica frost discharge generation;
(9) without any mechanical means of metal under water configuration, extend the work-ing life of subsea equipment, reduce cost of equipment maintenance.
When concrete enforcement, the sea water desaltination pre-treatment integrated apparatus of above-described embodiment, can also adopt following replacement scheme can complete equally goal of the invention:
(1) adopt mechanically mixing and the machinery alternative blast aeration mixing of flocculation and waterpower flocculation, although can realize identical technique object, increase electric installation and submarine mechanical equipment, facility investment and maintenance cost raise;
(2) adopt the alternative sludge bucket of underwater mud scraper and perforated pipe spoil disposal, although can realize technique object, increase submarine mechanical equipment, facility investment and maintenance cost raise;
(3) the alternative running type air supporting of fixed air supporting mud scraper mud scraper, near the phenomenon that although can realize the main scum silica frost function of scraping, may have that scum silica frost removes that thoroughly problem occurs, pool wall may have scum silica frost to adhere to the water surface, affects sense organ effect;
(4) adopt electronic adjustable effluent weir to substitute adjustable round crested weir on mud-water separation district's enlarging scum silica frost receiving tank and the adjustable effluent overflow weir water in clarification and effluent district, but can greatly increase investment, the operation and maintenance cost of equipment;
(5) the inclined tube in clarification and effluent district can substitute with swash plate, but may not have the uniformity of water distribution of inclined tube good.
The sea water desaltination pre-treatment integrated apparatus of above-described embodiment, process explanation used is as follows:
(1) first, precipitation and air-float technology are the approximately uniform two kinds of techniques of cleaning principle and cleaning action.Conventionally " flocculation+precipitation " technique has extraordinary removal effect to turbidity, colloid, but more poor than the removal effect of the little material of seawater and dissolved organic matter matter to algae, oils isodensity." flocculation+air supporting " technique is very effective to algae, oils and organism; But in the time that the turbidity in former seawater is too high, the outlet effect of air flotation pool will be subject to serious impact.Especially not ideal enough to being subject to stormy waves, precipitation affects turbidity of sea water to change the decontamination effect improving of muddy coast seawater greatly; If run into, oil slick pollutes, eutrophication seriously causes the phenomenons such as alga eruption again, effluent quality after precipitation or air supporting worsens, filtration procedure will be born the water quality impact load of fluctuation, and the operation stability of purification process technique will face comparatively stern challenge.
(2) secondly, " flocculation+floating depositing pool " technique is the coupling technique of " precipitation and air supporting " two kinds of techniques, can solve the decontamination effect improving of polluted seawaters such as being subject to turbidity, oil slick, algae.But adopt top layer water outlet because traditional air-float technology adopts bottom water outlet, depositing technology, after coupling, floating depositing pool technique must adopt middle layer water outlet, so be difficult to a certain extent ensure out that water suspension long-term stability is in lower level.In addition, mixing process also needs independent configuration.
The different medias such as reuse waste water in seawater cleaning process again, (comprising: the supernatant liquor of concentrated, the dehydration of media filtration backwash water, chemical sludge etc.), backflow active sludge, chemical agent all need to enter into together with former seawater that coagulation basin front end mixes, flocculation reaction.Need to ensure the abundant mixing of each medium in coagulation basin; Reuse water is directly delivered to coagulation basin front end, avoids mixing and carrying out again second lift with former water before total inlet water lifting pumps.
(3) last, the severe corrosive of seawater is very large on the impact in work-ing life of the metal material submarine mechanical equipment such as the mechanical flocculation reaction agitator of tradition, settling tank (or settling pond) mud scraper.Ensureing, under the prerequisite of process function, to reduce the use of submarine mechanical equipment.
Sea water desaltination pre-treatment in the utility model the various embodiments described above is used in integrated apparatus, and the explanation of nouns of relevant technical terms is as follows:
(1) coagulation and coagulation basin: coagulation is divided into and mixes and two kinds of technological processs of flocculation.The process that the medicament dropping into is spread in rapidly in processed water equably to create sound response condition is called coagulation.The colloid that completes cohesion mutually collides, assembles under certain outer force-disturbance, is called flocculation with the process that forms larger cotton-shaped particle; Coagulation basin has been the device of mixing and flocculation process.
(2) precipitation and settling tank: under action of gravity, at the bottom of making in water cotton-shaped particle that the suspended matter heavier than water, flocculation generate etc. be precipitated to pond, realize a kind of water treatment process that particle separates with water and cry and precipitate.Settling tank has been the device of precipitation process.
(3) air supporting and air flotation pool: utilize and add a large amount of micro-bubbles in water, and it is sticked on algae, oils, cotton-shaped particle, common floating upward quickly is to the water surface with it, realizes a kind of water treatment process that particle separates with water air supporting.Air flotation pool has been the device of air supporting process.
(4) filter: cry filtration by a kind of water treatment process of foreign material in granulated material or porous medium amputation water.General media filtration or the ultrafiltration membrance filters such as sand filtration/hard coal of adopting in seawater cleaning treatment process.
Finally it should be noted that: the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although the utility model is had been described in detail with reference to previous embodiment, for a person skilled in the art, its technical scheme that still can record aforementioned each embodiment is modified, or part technical characterictic is wherein equal to replacement.All within spirit of the present utility model and principle, any amendment of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (10)
1. a sea water desaltination pre-treatment integrated apparatus, it is characterized in that, comprise water inlet pipe, rising pipe and spoil disposal house steward, be equipped with successively coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district between described water inlet pipe and rising pipe, and as described spoil disposal house steward's branch and be equipped with respectively the multiple spoil disposal arms in described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and bottom, clarification and effluent district bucket.
2. sea water desaltination pre-treatment integrated apparatus according to claim 1, it is characterized in that, described coagulation district, comprise close described water inlet pipe setting and the mixing pit being communicated with water inlet pipe, near described mixing pit setting and for carrying out multiple nonmetal grid or the grid packing assembly of waterpower flocculation, and be arranged on described multiple nonmetal grid or grid packing assembly away from the upper end of mixing pit one side and the water side that is communicated with cloth pool;
In described mixing pit, be provided with the dicyclo umbrella aeration head for adopting the blast aeration of dicyclo umbrella to stir; In described water inlet pipe, mixing pit, multiple nonmetal grid or grid packing assembly, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, be provided with the multiple water holes of crossing that are communicated with successively; Be positioned at multiple spoil disposal arms in coagulation district, be separately positioned on the bottom of multiple nonmetal grids or grid packing assembly below bucket.
3. sea water desaltination pre-treatment integrated apparatus according to claim 2, is characterized in that, above described water inlet pipe, is provided with the aeration tube that is communicated to described dicyclo umbrella aeration head; Below described water inlet pipe, be provided with successively reuse water pipe and mud return line.
4. sea water desaltination pre-treatment integrated apparatus according to claim 1, it is characterized in that, described cloth pool, comprise cloth pond, the water inlet that is arranged on upper end, described cloth pond and is communicated with coagulation district, be arranged on the water outlet of lower end, described cloth pond, and the water distribution hoarding of water distribution grid is set in vertical direction layering;
Described water outlet, is communicated with aqueous vapor zone of action by the water distribution hoarding that is positioned at lower floor; Be positioned at the spoil disposal arm in cloth pool, be separately positioned on the bottom of laminates boom wall below bucket.
5. sea water desaltination pre-treatment integrated apparatus according to claim 1, it is characterized in that, described aqueous vapor zone of action, comprise aqueous vapor contact tank, the water inlet that is arranged on described aqueous vapor contact tank lower end and is communicated with cloth pool, and arrange and for by the separated training wall of aqueous vapor contact tank and mud-water separation district near described mud-water separation district;
In the bottom of described aqueous vapor contact tank, be provided with the dissolved air release of non-metallic material; At the top of described aqueous vapor contact tank, be provided with the multiple dissolved air water water inlet pipes that are communicated to described dissolved air release; Described multiple dissolved air water water inlet pipe is positioned at the pipeline of water surface top, adopts flange to connect; Be positioned at multiple spoil disposal arms of aqueous vapor zone of action, be separately positioned on the bottom of bucket in aqueous vapor contact tank;
Match with described dissolved air release, be provided with multiple water distribution grid.
6. sea water desaltination pre-treatment integrated apparatus according to claim 1, it is characterized in that, described mud-water separation district, comprise mud-water separation pond, the vertically parallel multiple water sides training wall being arranged in described mud-water separation pond, be horizontally set on the swash plate installing zone of training wall top, described multiple water sides, be positioned at described swash plate installing zone top and be arranged on the scum machine of scraping on top, mud-water separation pond, and be close to described swash plate installation region end, with scrape scum machine and match and be arranged on the enlarging scum silica frost receiving tank of upper end, mud-water separation pond;
Below the water surface of described swash plate installing zone, multiple non-metallic material swash plates are installed; Be positioned at multiple spoil disposal arms in mud-water separation district, be separately positioned on the bottom of training wall below, multiple water sides bucket; Clear water enters clarification and effluent district at described swash plate layout area end through the water hole of crossing under water.
7. sea water desaltination pre-treatment integrated apparatus according to claim 6, is characterized in that, described in scrape scum machine, comprise that the running type that is arranged on water surface top scrapes scum silica frost equipment; This running type is scraped scum silica frost equipment, the scum silica frost scraper plate that the part contacting with the water surface is quality of rubber materials;
On described enlarging scum silica frost receiving tank, be provided with the adjustable round crested weir for adjust operation water level.
8. sea water desaltination pre-treatment integrated apparatus according to claim 1, it is characterized in that, described clarification and effluent district, comprises settling pond, be arranged in the inclined tube installing zone in described settling pond, be located at described settling pond top and the adjustable effluent overflow weir water for adjust operation water level; At described inclined tube installing zone, the non-metallic material inclined tube for uniform water distribution and shallow layer precipitating is installed.
9. according to the sea water desaltination pre-treatment integrated apparatus described in any one in claim 1-8, it is characterized in that described spoil disposal house steward and multiple spoil disposal arm specifically comprise for the perforated pipe by gravity spoil disposal;
And/or,
Described spoil disposal house steward and multiple spoil disposal arm, specifically comprise for by the perforated pipe of gravity spoil disposal, and be connected with described perforated pipe and for aspirating the sludge pump of spoil disposal.
10. according to the sea water desaltination pre-treatment integrated apparatus described in any one in claim 1-8, it is characterized in that, described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, with wide and same high setting; In the bottom in described coagulation district, cloth pool, aqueous vapor zone of action, mud-water separation district and clarification and effluent district, uniform bucket and nonmetal perforated pipe spoil disposal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320840115.2U CN203741144U (en) | 2013-12-18 | 2013-12-18 | Integrated device for desalting and pre-treating seawater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320840115.2U CN203741144U (en) | 2013-12-18 | 2013-12-18 | Integrated device for desalting and pre-treating seawater |
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| Publication Number | Publication Date |
|---|---|
| CN203741144U true CN203741144U (en) | 2014-07-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320840115.2U Expired - Lifetime CN203741144U (en) | 2013-12-18 | 2013-12-18 | Integrated device for desalting and pre-treating seawater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203741144U (en) |
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2013
- 2013-12-18 CN CN201320840115.2U patent/CN203741144U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171219 Address after: 100088 Beijing city Haidian District Xitucheng Road No. 33 Co-patentee after: CENTRAL RESEARCH INSTITUTE OF BUILDING AND CONSTRUCTION CO., LTD. MCC Group Patentee after: MCC ENERGY SAVING ENVIRONMENTAL PROTECTION Co.,Ltd. Co-patentee after: CHINA JINGYE ENGINEERING Co.,Ltd. Address before: 100029, room 5, building 2, No. 1118 middle Sheng Road, Chaoyang District, Beijing Patentee before: MCC SEAWATER DESALINATION INVESTMENT CO.,LTD. |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140730 |