CN104163461B - A kind of novel water treatment purifier - Google Patents
A kind of novel water treatment purifier Download PDFInfo
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- CN104163461B CN104163461B CN201410184079.8A CN201410184079A CN104163461B CN 104163461 B CN104163461 B CN 104163461B CN 201410184079 A CN201410184079 A CN 201410184079A CN 104163461 B CN104163461 B CN 104163461B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 250
- 238000003860 storage Methods 0.000 claims abstract description 104
- 230000005494 condensation Effects 0.000 claims abstract description 100
- 238000009833 condensation Methods 0.000 claims abstract description 100
- 239000012153 distilled water Substances 0.000 claims abstract description 93
- 238000001704 evaporation Methods 0.000 claims abstract description 93
- 230000008020 evaporation Effects 0.000 claims abstract description 91
- 238000010438 heat treatment Methods 0.000 claims abstract description 37
- 238000009434 installation Methods 0.000 claims abstract description 26
- 238000007667 floating Methods 0.000 claims description 35
- 239000007788 liquid Substances 0.000 claims description 31
- 239000012530 fluid Substances 0.000 claims description 30
- 239000012528 membrane Substances 0.000 claims description 30
- 239000003921 oil Substances 0.000 claims description 24
- 238000007789 sealing Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 14
- 230000008569 process Effects 0.000 claims description 13
- 230000037361 pathway Effects 0.000 claims description 10
- 238000001179 sorption measurement Methods 0.000 claims description 7
- 208000002925 dental caries Diseases 0.000 claims description 6
- 239000010687 lubricating oil Substances 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 238000009738 saturating Methods 0.000 claims description 6
- 238000003032 molecular docking Methods 0.000 claims description 4
- 238000005260 corrosion Methods 0.000 claims description 3
- 230000007797 corrosion Effects 0.000 claims description 3
- 238000009826 distribution Methods 0.000 claims description 3
- 230000001360 synchronised effect Effects 0.000 claims description 3
- 240000007643 Phytolacca americana Species 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 12
- 238000007599 discharging Methods 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 3
- 239000002351 wastewater Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 238000005292 vacuum distillation Methods 0.000 description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 230000008676 import Effects 0.000 description 3
- 239000010410 layer Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002828 fuel tank Substances 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention relates to water treating equipment.A kind of novel water treatment purifier, comprise frame, frame is provided with the water chamber with depotition cock, aqua storage tank, husky strainer, there is the evaporation device of evaporation cavity, installation cavity, heating arrangements, middle water pipe, be built in the condensation impeller of installation cavity, to the tracheae that evaporation cavity vacuumizes, distilled water recycle pump, distilled water storage chamber and Y-tube, aqua storage tank is positioned at the below of depotition cock, evaporation device also comprises the heating chamber be looped around outside evaporation cavity, former water is evaporated by evaporation unit after husky metre filter, be condensed again to be formed after impeller condensation and purify waste water and be stored in water chamber.The invention provides a kind of heat to discharging during vapor condensation to reclaim for former evaporation of water, make heat carry out the novel water treatment purifier of recycle between evaporation with condensation, solving existing water treatment purifier and using inconvenience and the problem of poor removal effect to the small-particle impurity in water.
Description
Technical field
The present invention relates to water treating equipment, particularly relate to a kind of novel water treatment purifier.
Background technology
The structure formation of existing a kind of novel water treatment purifier has multiple.As in China Patent No. ZL2005101304043, publication date be June 13 in 2007 day, be called in the patent documentation of " a kind of prevent the method and apparatus of discharge water from generating secondary pollution " and disclose a kind of novel water treatment purifier.The novel water treatment purifier of existing one many employings filtration method purifies water, needs often cleaning or changes filtering membrane, therefore not only using inconvenience but also the poor removal effect to the small-particle impurity in water.
Summary of the invention
The invention provides a kind of heat to discharging during vapor condensation to reclaim for former evaporation of water, make heat carry out the novel water treatment purifier of one of recycle between evaporation with condensation, solving existing a kind of novel water treatment purifier and using inconvenience and the problem of poor removal effect to the small-particle impurity in water.
Above technical problem is solved by following technical proposal: a kind of novel water treatment purifier, comprise frame, described frame is provided with sand filter and water chamber, described water chamber is provided with depotition cock, it is characterized in that, described frame is also provided with water chamber, be positioned at the aqua storage tank below depotition cock, be provided with the installation cavity of vacuum orifice, heating arrangements, middle water pipe, distilled water recycle pump, distilled water storage chamber, Y-tube, and be positioned at condensation impeller and the evaporation device of installation cavity, described evaporation device comprises evaporation cavity and is looped around the heating chamber outside evaporation cavity, described condensation impeller comprises the condensation impeller shaft of synchronous axial system, condensation impeller vane, conveying distilled water is to the feed pathway on condensation impeller vane surface and condensation impeller housing, vapour passage is formed between adjacent condensation impeller vane, condensation impeller housing is provided with inlet mouth, air outlet and the liquid outlet channel alignd with the outer end of condensation impeller vane, inlet mouth docks with evaporation cavity, condensation impeller housing forms heat exchanging chamber with between installation cavity, heat exchanging chamber is connected with distilled water storage chamber, middle water pipe is heat transfer tube, one end of middle water pipe links together with the exit end of sand filter, the other end is connected with evaporation cavity with after distilled water storage chamber through heat exchanging chamber successively, distilled water recycle pump is used for the distilled water in distilled water storage chamber to be transported to heating chamber, first port of described Y-tube links together with described heating chamber, second port links together with described feed pathway, 3rd port links together with described water chamber.During use, former water is transported in evaporation cavity by middle water pipe and evaporates after husky metre filter, former water in evaporation cavity absorbs the heat of the distilled water in heating chamber when evaporating, the temperature of the distilled water in heating chamber is declined, distilled water after temperature in heating chamber declines is (hereinafter referred to as low-temperature distillation water, its temperature is higher than the temperature of former water when just to have entered installation cavity) part exports through the first distilled water discharging mouth as product water, another part arrives on the surface of condensation impeller vane after flowing into feed pathway, condensation impeller rotates produced centrifugal force continuously makes the distilled water of the low temperature flowed into through feed pathway be dispersed on the surface of condensation impeller vane, vapour stream in evaporation cavity directly contacts with low-temperature distillation water and produces heat exchange and condensation in the process of vapour passage, low-temperature distillation water on the distilled water of condensation gained and condensation impeller vane mixes formation hyperthermal distilled water, hyperthermal distilled water enters heat exchanging chamber from one end away from condensation impeller shaft (i.e. outer end) of condensation impeller vane through liquid outlet channel, hyperthermal distilled water enters in the process of heat exchanging chamber to be shed on middle water pipe, spray-type heating is carried out to the former water flowing through middle water pipe, former water is forwarded in distilled water storage chamber in middle water pipe, hyperthermal distilled water converges to the part in distilled water storage chamber, middle water pipe being positioned at distilled water storage chamber under gravity and floods, carrying out impregnated to the former water flowing through middle water pipe, to be heated to the temperature of the distilled water in same distilled water storage chamber equal, former water in last middle water pipe enters in evaporation cavity and is evaporated formation steam, distilled water in distilled water storage chamber is distilled water-circulating pump and is transported in heating chamber, so far the working cycle of a heat is namely surrounded.Quote water to release through depotition cock.
The present invention also comprises the storage barrel on the exit end being arranged on middle water pipe, and be provided with the CD-ROM drive motor driving condensation impeller in storage barrel, described distilled water recycle pump is positioned at described storage barrel, and middle water pipe is connected with evaporation cavity by storage barrel.CD-ROM drive motor and distilled water recycle pump are all arranged in storage barrel, the heat discharged when CD-ROM drive motor and distilled water pump operating cycle plays the effect to former water additional heat, otherwise former water plays cooling effect to CD-ROM drive motor and distilled water recycle pump.The heat energy that CD-ROM drive motor and distilled water recycle pump produce is recycled utilization, the heat supplemented when not only can reduce evaporation, also lowers the temperature to CD-ROM drive motor and distilled water recycle pump without the need to additional mechanism providing additional operation.
As preferably, storage barrel is positioned at distilled water storage chamber, and heating arrangements is arranged in distilled water storage chamber.The beneficial effect of " storage barrel is positioned at distilled water storage chamber " is: compact construction, can prevent the loss of the heat of former water in storage barrel.The beneficial effect of " heating arrangements is arranged in distilled water storage chamber " is, while the temperature that Jiang Yuanshui is heated to needed for evaporation, by the distilled water heating in distilled water storage chamber, and heat required when making the distilled water entering heating chamber that former water can be provided to evaporate.Evaporative process can be started fast.
As preferably, evaporation device is unsettled to be arranged in installation cavity, and distilled water storage chamber is surrounded by the outer wall of evaporation device and installation cavity.Can prevent the heat losses of the distilled water in heating chamber from falling, heat recovery and utilization is effective.
As preferably, described condensation impeller is positioned at the top of described evaporation device, and described evaporation cavity is the chamber of open upper end, and condensation impeller is vertically arranged, condensation impeller housing lower end is opened wide completely and forms inlet mouth, and inlet mouth is docking together with the opening end sealing of evaporation cavity.Compact construction, the track route of steam and distilled water is short, is lost to the less calories outside installation cavity, needs to supplement the less calories gone for evaporating after making device start.Patency during steam flow is good.
As preferably, between condensation impeller and evaporation cavity, be provided with guide grids.Make steam enter vapour passage with the traffic direction vertically risen, condensation effect is good.
As preferably, the side surface of described evaporation cavity forms generating surface, the vacuum liquid film forming structure can rotated along the circumference of evaporation cavity is provided with in described evaporation cavity, described vacuum liquid film forming structure comprise set gradually from front to back according to the turning direction of vacuum liquid film forming structure blade, concentrated solution adsorption tube and combination film forming device, described combination film forming device comprise some directions of level distribution along the vertical direction extend film forming bar and by raw water to the water distributing pipe of film forming bar.In the process that vacuum liquid film forming structure is rotated along evaporation cavity, generating surface carries out on the one hand removing, makes water surface of evaporation non-scaling, ensures that follow-up former water has clean water surface of evaporation, is convenient to the transmission of the adhesion of liquid film and heat by blade, steam simultaneously in vane drive evaporation cavity rises, and makes steam immediately leave generating surface and forms a negative pressure band higher than the vacuum tightness in vacuum vessel at the rear (directed with turning direction) of blade; The concentrated solution remained on generating surface adsorbs to walk by concentrated solution adsorption tube immediately that be positioned at blade rear, can not assemble concentrated solution on evaporation cavity especially generating surface, ensures the clean of generating surface further; When former water flows out from the film forming bar combination film forming device, due to the effect of centrifugal force, former water forms liquid film and evaporates part on the surface of film forming bar, when the liquid film be not evaporated is transported to the generating surface being positioned at negative pressure band place, the thinner thickness of liquid film, liquid film one contacts generating surface and is namely fallen by flash evaporation.Now remain in and generating surface is concentrated solution, concentrated solution is adsorbed to walk by the concentrated solution adsorption tube arrived soon after in time.
As preferably, in described evaporation cavity, be provided with dope receiving tank, described dope receiving tank be provided with between described sand filter by dope receiving tank from concentrated solution described in the concentrated solution recovery pump of sand filter feed-water end.The utilization ratio of water can be improved.
The present invention also comprises feet, and described feet can slide up and down to be connected to described frame.Height of the present invention can be adjusted, to meet requirement for height when different spaces uses.
The present invention also comprises refueling device, described refueling device comprises storage tank, oil discharge passage, rupture of membranes bar and corrosive fluid bin, described oil discharge passage is used for the matching part lubricating oil in described storage tank being transported to described feet and frame, described storage tank comprises at least two sheathed successively and cavitys be fixed together, the lower wall of described cavity is provided with oil outlet, described oil outlet is sealedly connected with sealing membrane, described rupture of membranes bar vertically extends and is positioned at the below of storage tank, described rupture of membranes bar, and the oil outlet of all cavitys is all positioned on same vertical curve, regularly rotten formula floating drum is thoroughly provided with in described corrosive fluid bin, described regular corruption saturating formula floating drum comprises the rotproofness shell of lower ending opening and some corrosive fluids be corroded in liquid bin expend the broken dividing plate of setting duration corrosion, described shell divide is gone out some floating chambers by described dividing plate, the quantity of described floating chamber is equal with the quantity of described cavity, described dividing plate distributes along the vertical direction, described storage tank floats on the corrosive fluid in described corrosive fluid bin by described floating drum, described storage tank can both float by floating chamber independently described in each, corrosive fluid in corrosive fluid bin often corrode brokenly a floating chamber and cause that storage tank declines in process once, described rupture of membranes bar only can poke sealing membrane on a cavity.Can regularly self-lubrication.
As preferably, described aqua storage tank is stamped shelf.Accessibility during use can be improved.
As preferably, the sidewall of described aqua storage tank is provided with some brace rods, and described shelf links together with described aqua storage tank by being shelved on described brace rod, and described brace rod extends along the vertical direction.Fast and easy during installing/dismounting shelf; Brace rod can improve the structural strength of birth groove, makes aqua storage tank can be designed to thin-wall construction to improve volume.
As preferably, the upper surface of described shelf is provided with protective layer.Security is good.
The present invention has following advantage: arrange husky strainer, can be blocked by macrobead thing by dust evaporation device, by the distilled water making the distilled water of low temperature form high temperature to impel vapor condensation with steam direct contact heat transfer, therefore the heat storage discharged during condensation is in the distilled water of high temperature, then the distilled water of high temperature is made to carry out heat exchange with former water, the temperature of former water is made to reach vaporization temperature, and go to heat evaporation cavity by the distilled water of high temperature, heat required when providing former water to evaporate, make the temperature of the distilled water of discharging lessly higher than the temperature of former water when just entering, heat major part circulates between evaporation and condensation, therefore need the heat of external complement less during evaporation, reduce the energy consumption in purificating raw water process, heat during condensation obtains effective recycling, arrange aqua storage tank, environment protecting is good.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention.
Fig. 2 is the schematic diagram of the A-A of Fig. 1 when analysing and observe and do not draw water chamber.
Fig. 3 is the close-up schematic view that the B of Fig. 2 goes out.
Fig. 4 is C-C cross-sectional schematic of Fig. 1.
Fig. 5 is the enlarged diagram of refueling device.
Fig. 6 is the schematic diagram that refueling device corrodes when breaking a floating chamber.
Fig. 7 is the schematic diagram that refueling device corrodes when breaking two floating chambers.
In figure: installation cavity 1, distilled water storage chamber 11, heating arrangements 12, storage barrel 13, heat exchanging chamber 14, husky strainer 15, husky strainer water inlet port 151, intake antrum 16, middle water pipe 17, vacuum orifice 18, evaporation device 2, evaporation cavity 21, heating chamber 22, nozzle 221, output tube 222, rotating disk 23, vacuum liquid film forming structure 24, blade 241, combination film forming device 242, water distributing pipe 2421, film forming bar 2422, concentrated solution suction pipe 243, vacuum source 25, dope receiving tank 26, concentrated solution recovery pump 261, condensation impeller 3, condensation impeller shaft 31, liquid storage cylinder 311, condensation impeller vane 32, blade part inlet opening 321, flanging 322, the surface 323 being positioned at the front side in condensation wheel rotation direction of condensation impeller vane, crack 324, condensation impeller housing 33, apocenosis passage 331, inlet mouth 332, air outlet 333, vapour passage 34, feed pathway 35, frame 4, water chamber 41, aqua storage tank 42, brace rod 421, depotition cock 43, shelf 44, Y-tube 45, CD-ROM drive motor 5, distilled water recycle pump 6, water distributing pipe 7, guide grids 8, refueling device 9, storage tank 91, cavity 911, oil outlet 912, sealing membrane 913, oil discharge passage 92, oil-feed bucket 921, zerk 922, rupture of membranes bar 93, corrosive fluid bin 94, the saturating formula floating drum 95 of regular corruption, shell 951, dividing plate 952, floating chamber 953, guide rod 96, corrosive fluid 97, union lever 98.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the present invention is further illustrated.
Embodiment one, see Fig. 1, a kind of novel water treatment purifier, comprises frame 4.Frame 4 is provided with water chamber 41, aqua storage tank 42 and Y-tube 45.Water chamber 41 is provided with the depotition cock 43 of downward water outlet.Aqua storage tank 43 is positioned at the below of depotition cock 43.Aqua storage tank 42 is stamped shelf 44.The sidewall of aqua storage tank 42 is provided with some brace rods 421.Brace rod 421 extends along the vertical direction.Shelf 44 links together with aqua storage tank 42 by being shelved on brace rod 421.The upper surface of shelf 44 is provided with non-skid finish.
Frame 4 is also provided with installation cavity 1, evaporation device 2 and condensation impeller 3.
The top of installation cavity 1 is provided with husky strainer 15.Installation cavity 1 outside is provided with concentrated solution recovery pump 261.Evaporation device 2 is suspended in installation cavity 1.The outer wall of installation cavity 1 and evaporation device 2 surrounds distilled water storage chamber 11.Heating arrangements 12 is provided with in distilled water storage chamber 11.Heating arrangements 12 is electrothermal tube.Storage barrel 13 is installed in distilled water storage chamber 11.CD-ROM drive motor 5 and distilled water recycle pump 6 is provided with in storage barrel 13.The import of distilled water recycle pump 6 is connected with distilled water storage chamber 11 by pipeline.
Evaporation device 2 comprises the evaporation cavity 21 of open upper end, the heating chamber 22 being looped around evaporation cavity outer 21 and rotating disk 23.Rotating disk 23 is driven by CD-ROM drive motor 5.Multiple nozzle 221 is provided with in heating chamber 22.The import of nozzle 221 is connected by the outlet of pipeline with distilled water recycle pump 6.The outlet of nozzle 221 is towards the periphery wall (periphery wall refers to wall evaporation cavity 21 and heating chamber 22 separated) of evaporation cavity 21.Evaporation cavity 21 is ring channel structures.
The top of evaporation cavity 21 is provided with dope receiving tank 26.Concentrated solution in dope receiving tank 26 is input in husky strainer by the entrance end of concentrated solution recovery pump 261 and husky strainer 15.Vacuum liquid film forming structure 24 is provided with in evaporation cavity 21.The circumference that vacuum liquid film forming structure 24 is drive along evaporation cavity 21 by rotating disk 23 is rotated.Vacuum liquid film forming structure 24 comprises blade 241, concentrated solution suction pipe 243 and combination film forming device 242.Combination film forming device 242 comprises water distributing pipe 2421 and some film forming bars 2422 be connected on water distributing pipe 2421 distributed along the vertical direction.Film forming bar 2422 extends in the horizontal direction.Water distributing pipe 2421 vertically extends.The upper end of water distributing pipe 2421 is fixed on rotating disk 23.The passage being communicated with storage barrel 13 and water distributing pipe 2421 is provided with in rotating disk 23.Rotating disk 23 is provided with vacuum source 25.Concentrated solution suction pipe 243 extends along the vertical direction.The upper end of concentrated solution suction pipe 243 and exit end are docking together with the entrance end of vacuum source 44, and the outlet of vacuum source 25 is positioned at the top of dope receiving tank 26.
Condensation impeller 3 is positioned at installation cavity 1 and is positioned at the top of evaporation device 2.
Condensation impeller 3 comprises the condensation impeller shaft 31 of synchronous axial system, condensation impeller vane 32 and condensation impeller housing 33.Condensation impeller housing 33 and installation cavity 1 surround heat exchanging chamber 14.Condensation impeller shaft 31 is driven by CD-ROM drive motor 5.
Liquid storage cylinder 311 is provided with in condensation impeller shaft 31.The inner of condensation impeller vane 32 wears in liquid storage cylinder 311.The water distributing pipe 7 extended along the vertical direction is equipped with in liquid storage cylinder 311.Condensation impeller vane 32 and condensation impeller shaft 31 seal affixed linking together.Condensation impeller vane 32 and condensation impeller shaft 31 are sealed by the mode of welding and are fixed together.The inner of condensation impeller vane 32 is provided with multiple blade part inlet opening 321.Blade part inlet opening 321 is along the axial distribution of condensation impeller shaft 31.The outer end of condensation impeller vane 31 is welded on the internal surface of condensation impeller housing 33.The axially extended vapour passage 34 along condensation impeller shaft is formed between adjacent condensation impeller vane 32.Condensation impeller housing 33 times both ends opens and form inlet mouth 332, open upper end and form air outlet 333.Condensation impeller housing 33 is provided with apocenosis passage 331.Condensation impeller housing 33 is docking together with the outer side wall sealing of evaporation cavity 21.Condensation impeller housing 33 can rotate relative to evaporation cavity 21.Guide grids 8 is provided with between condensation impeller 3 and evaporation cavity 21.
First port of Y-tube 45 links together with heating chamber 22, the second port links together with water distributing pipe 7, the 3rd port links together with water chamber 41.
The roof of installation cavity 1 is provided with vacuum orifice 18.
Some middle water pipes 17 are also provided with in installation cavity 1.Middle water pipe 17 is heat transfer tube.The import of middle water pipe 17 links together with intake antrum 16.Intake antrum 16 links together with the exit end of husky strainer 15.Middle water pipe 17 is from top to bottom successively through heat exchanging chamber 14 and distilled water storage chamber 11.The outlet of middle water pipe 17 is connected with storage barrel 13.
Frame 4 is also provided with feet 46 and refueling device 9.Feet 46 can slide up and down to be connected to frame 4.Refueling device 9 comprises storage tank 91, oil discharge passage 92 and corrosive fluid bin 94.
One end of oil discharge passage 92 be provided be positioned at oil-feed bucket 921 below storage tank, the oil outlet 922 of matching part alignment that the other end is provided with same feet and casing.Storage tank 91 is higher than oil outlet 922.
Corrosive fluid bin 94 links together with frame 4.Corrosive fluid bin 94 and oil-feed bucket 921 are fixed together.
See Fig. 2, condensation impeller vane 32 distributes along the circumference of condensation impeller shaft 31.The inner of condensation impeller vane 32 is provided with along D in condensation wheel rotation direction and figure to the flanging 322 of forward fold.Condensation impeller housing 33 is fixed together with condensation impeller shaft 31 by condensation impeller vane 32.Align with the entrance end of apocenosis passage 331 in the surface 323 being positioned at the front side in condensation wheel rotation direction of condensation impeller vane.Apocenosis passage 331 tilts backwards along condensation wheel rotation direction.
Heat exchanging chamber 14 is annular, and middle water pipe 17 has 16.Middle water pipe 17 is distributed in heat exchanging chamber 14 along the circumference of condensation impeller housing 313.
See Fig. 3, between flanging 322 and condensation impeller vane 32, form crack 324.Crack 324 and blade part inlet opening 321 form feed pathway 35.
See Fig. 4, vacuum liquid film forming structure 24 has four.Four vacuum liquid film forming knots enough 24 are symmetrically distributed in evaporation cavity 21.Evenly be arranged so that without the need to counterweight, stationarity when rotating can be ensured.Blade 241, concentrated solution adsorption tube 243 and combination film forming device 242 according to use time turning direction and figure in E to setting gradually from front to back.Film forming bar 2422 is conical rod, film forming bar 2422 perpendicular to evaporation cavity 21 sidewall and be located in water distributing pipe 421.Concentrated solution adsorption tube 243 is positioned on the outside of evaporation cavity 21.Nozzle 221 is uniformly distributed along the circumference of heating chamber 22.
See Fig. 5, refueling device also comprises rupture of membranes bar 93, regularly rotten formula floating drum 95 and guide rod 96 thoroughly.
Storage tank 91 is linked together with the saturating formula floating drum 95 of regularly corruption by union lever 98.Union lever 98 and regularly corruption are detachably connected by bolt between formula floating drum 95 thoroughly.It is 4 sheathed successively and cavitys 911 be fixed together that storage tank 91 comprises at least two the present embodiment.Lubricating oil (not drawing in lubricating oil figure) is housed in cavity 911.The lower wall of cavity 911 is provided with oil outlet 912.Oil outlet 912 is sealedly connected with sealing membrane 913.4 oil outlets 912 of amounting to of 4 cavitys to be positioned on the vertical straight line of same and to be positioned at directly over rupture of membranes bar 93.Distance between adjacent sealing membrane is equal.
Rupture of membranes bar 93 vertically extends.The lower end of rupture of membranes bar 93 is connected in oil-feed bucket 921.Rupture of membranes bar 93 is positioned at the below of storage tank 91.
Corrosive fluid bin 94 is positioned at the below of storage tank 91.
The saturating formula floating drum 95 of regular corruption is positioned at corrosive fluid bin 94.The saturating formula floating drum 95 of regular corruption comprises rotproofness shell 951 and four pieces of dividing plates 952 of lower ending opening.Dividing plate 952 is aluminium sheet.Dividing plate 952 distributes along the vertical direction.Shell 951 is divided into 4 floating chambers distributed along the vertical direction 953 by dividing plate 952.Distance between adjacent dividing plate is equal.Distance between adjacent dividing plate equals the distance between adjacent sealing membrane.
Guide rod 96 vertically extends.One end of guide rod 96 is fixed together with storage tank 91.The other end of guide rod 96 is located in upper bolster 1 slidably.
See Fig. 6, when refueling device will be started, corrosive fluid 97 is injected in corrosive fluid bin 94, regular rotten formula floating drum 95 thoroughly floats and realizes out floating of fuel tank 91 by corrosive fluid 97, stops adding corrosive fluid when fuel reserve tank 91 floats the distance being less than between adjacent sealing membrane to the distance between rupture of membranes bar 93 and the sealing membrane in outermost layer cavity.Storage tank 91 can both float by buoyancy that each floating chamber 953 produces independently.In the present embodiment, corrosive fluid 97 is sodium hydroxide solution.By the concentration of control corrosion rate liquid 97 or/and the thickness of dividing plate, make the dividing plate liquid 97 that is corroded in setting duration corrode broken, these data can be learnt by test.
When the time of pouring corrosive fluid 97 into reaches a setting duration, the dividing plate that is positioned at bottom in dividing plate 952 is corroded brokenly, corrosive fluid enters the floating chamber being arranged in bottom in floating chamber 953, storage tank 91 drop to by floating chamber 953 from below to up second floating chamber of number float, the lubricating oil that the sealing membrane 913-1 being arranged in outermost layer cavity in decline process is poked by rupture of membranes bar 93, cavity 911 is arranged in outermost cavity flows to oil discharge passage 92 by the oil outlet of correspondence and flows to feet and carry out a self-oiling with the matching part of frame.
See Fig. 7, when the time of pouring corrosive fluid 97 into reaches two setting durations, be positioned at time dividing plate of below in dividing plate 952 to be also corroded brokenly, corrosive fluid enters in floating chamber 953 and is arranged in time floating chamber of below, the 3rd floating chamber that storage tank 91 drops to by counting from below to up in floating chamber 953 floats, the sealing membrane being arranged in time outer cavity in decline process is also poked by rupture of membranes bar 93, the lubricating oil being arranged in time outer field cavity in cavity 911 drops onto oil discharge passage 92 after being flowed out by the oil outlet of the oil outlet on secondary outer cavity and outermost layer cavity and flows to feet with the matching part of frame and carry out self-oiling again, the like, four self-oilings can be carried out in the present embodiment, then change automatic fuelling device and carry out self-oiling again.
During use, see Fig. 1: be evacuated down to required vacuum tightness by vaccum-pumping equipment through vacuum orifice 18 pairs of evaporation cavities 21, CD-ROM drive motor 5 drives condensation impeller 3 according to the D in Fig. 2 to rotation.Low-temperature distillation water in water distributing pipe 7 under the influence of centrifugal force through feed pathway 35(see Fig. 3) providing and delivering and spreading out is positioned at the surperficial 323(in the front of condensation impeller vane turning direction see Fig. 2 at condensation impeller vane) on.Steam in evaporation cavity 21 enters in vapour passage 34, directly contact with the low-temperature distillation water on condensation impeller 3 surface and condensation be mixed into the distilled water of high temperature, hyperthermal distilled water is shed in heat exchanging chamber 14 from the outer end of condensation impeller vane 32 through apocenosis passage 331, hyperthermal distilled water plays the effect of spray-type heating to middle water pipe 17, and the former water temp in middle water pipe 17 rises.Under gravity, hyperthermal distilled water gathers in distilled water storage chamber 11 and is flooded by middle water pipe 17, former water in middle water pipe 17 is equal to temperature with the distilled water heat exchange in distilled water storage chamber 11, former water enters in evaporation cavity 21 through storage barrel 13 and evaporates, the dope of evaporation gained gathers in concentrated solution pinching groove 26 through concentrated solution suction pipe 243 under the effect of absorbent pump 25, and the concentrated solution in concentrated solution pinching groove 26 is discharged to husky strainer 15 through concentrated solution recovery pump 261.Distilled water in distilled water storage chamber 11 enters in heating chamber 22 under the effect of distilled water recycle pump 6, provide heat for the former water evaporation in evaporation cavity 21, and after the distilled water in heating chamber 22 is absorbed heat, temperature declines (temperature can higher than the temperature of former water when just entering in installation cavity 1).Distilled water in heating chamber 22 through Y-tube 45 part stretch out and be stored in water chamber 41, another part outputs to water distributing pipe 7 and enters feed pathway 35(see Fig. 3) in.Whole process so circulates.Then stop purifying water after the water in water chamber 41 is full.Former water in storage barrel 13 is that the passage under the negative-pressure adsorption effect in installation cavity 1 in rotating disk 23 enters water distributing pipe 2421, to spread out on film forming bar 2422 with membranaceous and flow on the outer side wall internal surface of evaporation cavity 21 under the influence of centrifugal force, completing evaporation in the process.Blade 241 plays the outer side wall internal surface of clean evaporation cavity 11 and forms lower subnormal ambient to accelerate to evaporate and reduce the effect of vaporization temperature.
For ease of read and comprehend, the flowing-path of former water and distilled water is summarized as follows, the flowing-path of distilled water is: distilled water → heat exchanging chamber 14 → distilled water storage chamber 11 → distilled water recycle pump 6 → nozzle 221 → heating chamber 22 → Y-tube 45, starting walking along separate routes, a part of distilled water enters water chamber 41, the other side divides distilled water → water distributing pipe 7 → liquid storage cylinder 311 → blade part inlet opening 321 → crack 324 → condensation impeller vane 32 → heat exchanging chamber 14.The flowing-path of former water is: the outer side wall internal surface of former water → husky strainer water inlet port 151 → husky strainer 15 → intake antrum 16 → middle water pipe 17 → storage barrel 13 → rotating disk 23 → water jet standpipe 2422 → film forming bar 2421 → evaporation cavity 21, start walking along separate routes, one step is condensed into distilled water after dividing former water to be evaporated to water vapor → condensation impeller vane 32, and another part forms concentrated solution → concentrated solution suction pipe 243 → dope receiving tank 26 → concentrated solution recovery pump 261 → husky strainer water inlet port 151 → husky strainer 15.When system just drives, need to open heating arrangements 12 to drive to make evaporative process, then the temperature by detecting the former water in storage barrel 13 judges whether to need additional heat to maintain evaporative process, if the temperature of the former water in storage barrel is lower than the temperature needed for evaporation, represent and now improve the temperature of the distilled water in former water and distilled water storage chamber 11 to meeting the requirements by starting heating arrangements 12 by the heat that heat losses amount is greater than pure liquid recycle pump 6 and CD-ROM drive motor 5 and discharges.
When needing to use water, on the position that water tumbler being shelved on perpendicular configuration state shelf 44 is positioned at below depotition cock 43.Open depotition cock 43, the water in water chamber 41 flows to water tumbler through depotition cock 43.When the water of depotition cock 43 poor sealing or water tumbler overflows, leak the water overflowed and be collected in aqua storage tank 42 and prevent water clock on ground.
Claims (7)
1. a novel water treatment purifier, comprise frame, described frame is provided with sand filter and water chamber, described water chamber is provided with depotition cock, it is characterized in that, also comprise feet and refueling device, described frame is also provided with water chamber, be positioned at the aqua storage tank below depotition cock, be provided with the installation cavity of vacuum orifice, heating arrangements, middle water pipe, distilled water recycle pump, distilled water storage chamber, Y-tube, and be positioned at condensation impeller and the evaporation device of installation cavity, described evaporation device comprises evaporation cavity and is looped around the heating chamber outside evaporation cavity, described condensation impeller comprises the condensation impeller shaft of synchronous axial system, condensation impeller vane, conveying distilled water is to the feed pathway on condensation impeller vane surface and condensation impeller housing, vapour passage is formed between adjacent condensation impeller vane, condensation impeller housing is provided with inlet mouth, air outlet and the liquid outlet channel alignd with the outer end of condensation impeller vane, inlet mouth docks with evaporation cavity, condensation impeller housing forms heat exchanging chamber with between installation cavity, heat exchanging chamber is connected with distilled water storage chamber, middle water pipe is heat transfer tube, one end of middle water pipe links together with the exit end of sand filter, the other end is connected with evaporation cavity with after distilled water storage chamber through heat exchanging chamber successively, distilled water recycle pump is used for the distilled water in distilled water storage chamber to be transported to heating chamber, first port of described Y-tube links together with described heating chamber, second port links together with described feed pathway, 3rd port links together with described water chamber, described feet can slide up and down to be connected to described frame, described refueling device comprises storage tank, oil discharge passage, rupture of membranes bar and corrosive fluid bin, described oil discharge passage is used for the matching part lubricating oil in described storage tank being transported to described feet and frame, described storage tank comprises at least two sheathed successively and cavitys be fixed together, the lower wall of described cavity is provided with oil outlet, described oil outlet is sealedly connected with sealing membrane, described rupture of membranes bar vertically extends and is positioned at the below of storage tank, described rupture of membranes bar, and the oil outlet of all cavitys is all positioned on same vertical curve, regularly rotten formula floating drum is thoroughly provided with in described corrosive fluid bin, described regular corruption saturating formula floating drum comprises the rotproofness shell of lower ending opening and some corrosive fluids be corroded in liquid bin expend the broken dividing plate of setting duration corrosion, described shell divide is gone out some floating chambers by described dividing plate, the quantity of described floating chamber is equal with the quantity of described cavity, described dividing plate distributes along the vertical direction, described storage tank floats on the corrosive fluid in described corrosive fluid bin by described floating drum, described storage tank can both float by floating chamber independently described in each, corrosive fluid in corrosive fluid bin often corrode brokenly a floating chamber and cause that storage tank declines in process once, described rupture of membranes bar only can poke sealing membrane on a cavity.
2. the novel water treatment purifier of one according to claim 1, it is characterized in that, also comprise the storage barrel on the exit end being arranged on middle water pipe, the CD-ROM drive motor driving condensation impeller is provided with in storage barrel, described distilled water recycle pump is positioned at described storage barrel, and middle water pipe is connected with evaporation cavity by storage barrel.
3. the novel water treatment purifier of one according to claim 2, is characterized in that, storage barrel is positioned at distilled water storage chamber, and heating arrangements is arranged in distilled water storage chamber.
4. the novel water treatment purifier of one according to claim 3, is characterized in that, evaporation device is unsettled to be arranged in installation cavity, and distilled water storage chamber is surrounded by the outer wall of evaporation device and installation cavity.
5. the novel water treatment purifier of one according to claim 4, it is characterized in that, described condensation impeller is positioned at the top of described evaporation device, described evaporation cavity is the chamber of open upper end, condensation impeller is vertically arranged, condensation impeller housing lower end is opened wide completely and forms inlet mouth, and inlet mouth is docking together with the opening end sealing of evaporation cavity.
6. the novel water treatment purifier of one according to claim 5, is characterized in that, is provided with guide grids between condensation impeller and evaporation cavity.
7. the novel water treatment purifier of the one according to claim 5 or 6, it is characterized in that, the side surface of described evaporation cavity forms generating surface, the vacuum liquid film forming structure can rotated along the circumference of evaporation cavity is provided with in described evaporation cavity, described vacuum liquid film forming structure comprise set gradually from front to back according to the turning direction of vacuum liquid film forming structure blade, concentrated solution adsorption tube and combination film forming device, described combination film forming device comprise some directions of level distribution along the vertical direction extend film forming bar and by raw water to the water distributing pipe of film forming bar.
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| CN201410184079.8A CN104163461B (en) | 2014-05-05 | 2014-05-05 | A kind of novel water treatment purifier |
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| CN104761035A (en) * | 2015-03-20 | 2015-07-08 | 毛方生 | Sewage processing equipment with water quality monitoring function and usage method thereof |
| CN106693418B (en) * | 2016-12-22 | 2018-10-16 | 重庆淼森环保工程有限公司 | Strong brine high dispersive dehydration equipment |
| CN117643259B (en) * | 2024-01-30 | 2024-04-09 | 云南朗乾农副产品有限公司 | Automatic irrigation equipment of plant |
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| JP2013071057A (en) * | 2011-09-28 | 2013-04-22 | Toshiba Corp | Water treatment equipment |
| CN102580333B (en) * | 2012-02-15 | 2014-04-30 | 傅利江 | Evaporation system for pressure reduction and film formation through vacuum rotation |
| CN102659194B (en) * | 2012-04-01 | 2014-03-12 | 傅利江 | Distillation-type seawater desalinization device |
| CN202558663U (en) * | 2012-04-01 | 2012-11-28 | 傅利江 | Distillation type seawater desalting equipment |
| CN103387270B (en) * | 2013-07-18 | 2014-06-25 | 海南大学 | A vacuum vapor compression distillation sea water desalination device |
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