CN203861021U - Distillation type water dispenser - Google Patents
Distillation type water dispenser Download PDFInfo
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- CN203861021U CN203861021U CN201420219024.1U CN201420219024U CN203861021U CN 203861021 U CN203861021 U CN 203861021U CN 201420219024 U CN201420219024 U CN 201420219024U CN 203861021 U CN203861021 U CN 203861021U
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Abstract
The utility model relates to a water processing device. A distillation type water dispenser comprises a rack, wherein the rack is provided with a water supply cavity with a water yielding tap, a water storage groove, a sand filter, an evaporation mechanism with an evaporation cavity, a mounting cavity, a heating mechanism, a middle water pipe, a condensing impeller arranged in the mounting cavity, an air pipe for vacuumizing the evaporation cavity, a distilled water circulating pump, a distilled water storage cavity and a T-branch pipe, wherein the water storage groove is located below the water yielding tap; the evaporation mechanism further comprises a heating cavity around the evaporation cavity; raw water after being filtered by the sand filter is evaporated by the evaporation device and then condensed by the condensing impeller to form purified water to be stored in the water supply cavity. The distillation type water dispenser provided by the utility model can recycle heat energy released during the vapor condensation to evaporate the raw water and enable the heat energy to be recycled between the evaporation and condensation, so that the problem that the existing water dispenser has poor removal effect on small particle impurities in the water is solved.
Description
Technical field
The utility model relates to water treatment facilities, relates in particular to a kind of distillation type water dispenser.
Background technology
The version of existing water dispenser has multiple.As disclosed a kind of water dispenser in the patent documentation that is on June 13rd, 2007 in China Patent No. ZL2005101304043, open day.Existing water dispenser adopts filtration method to purify water more, needs often to clean or change filter membrane, therefore not only uses inconvenience but also the poor removal effect to the granule impurity in water.
Utility model content
The utility model provides a kind of heat discharging during to steam-condensation to reclaim for former evaporation of water, make heat at the distillation type water dispenser recycling between evaporation and condensation, has solved the problem of the poor removal effect of existing water dispenser to the granule impurity in water.
Above technical problem solves by following technical proposal: a kind of distillation type water dispenser, comprise frame, and described frame is provided with sand filter and water chamber, and described water chamber is provided with depotition cock, and described frame is also provided with water chamber, be positioned at the aqua storage tank of depotition cock below, be provided with the installation cavity of vacuum orifice, heating arrangements, middle water pipe, distilled water circulating pump, distilled water storage chamber, three-way pipe, and be positioned at condensation impeller and the evaporation device of installation cavity, described evaporation device comprises evaporation cavity and be looped around the heating chamber outside evaporation cavity, and described condensation impeller comprises the condensation impeller shaft of synchronous rotation, condensation impeller blade, carry distilled water to the lip-deep feed pathway of condensation impeller blade and condensation impeller housing, between adjacent condensation impeller blade, form steam channel, condensation impeller housing is provided with air inlet, gas outlet and the liquid outlet channel aliging with the outer end of condensation impeller blade, air inlet docks with evaporation cavity, condensation impeller housing is with forming heat exchanging chamber between installation cavity, heat exchanging chamber is connected with distilled water storage chamber, middle water pipe is heat exchanger tube, and one end of middle water pipe links together with the port of export of sand filter, the other end is successively through being connected with evaporation cavity after heat exchanging chamber and distilled water storage chamber, and distilled water circulating pump is for being transported to heating chamber by the distilled water in distilled water storage chamber, and the first port of described three-way pipe links together with described heating chamber, the second port links together with described feed pathway, the 3rd port links together with described water chamber.When use, former water is transported in evaporation cavity and evaporates by middle water pipe after husky filter filters, former water in evaporation cavity absorbs the heat of the distilled water in heating chamber while evaporation, 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, the temperature of its temperature former water when just having entered installation cavity is high) part exports through the first distilled water discharging mouth as product water, another part arrives on the surface of condensation impeller blade after flowing into feed pathway, condensation impeller rotates the centrifugal force producing is continuously dispersed on the surface of condensation impeller blade the distilled water of the low temperature flowing into through feed pathway, vapor stream in evaporation cavity directly contacts and produces heat exchange and condensation with low temperature distillation water in the process of steam channel, low temperature distillation water on the distilled water of condensation gained and condensation impeller blade mixes formation hyperthermal distilled water, hyperthermal distilled water enters heat exchanging chamber from one end away from condensation impeller shaft (being outer end) of condensation impeller blade through liquid outlet channel, hyperthermal distilled water enters in the process of heat exchanging chamber and is shed on middle water pipe, former water to water pipe in the middle of flowing through carries out fountain heating, former water is forwarded in distilled water storage chamber in middle water pipe, hyperthermal distilled water converges to the part that in distilled water storage chamber, middle water pipe is positioned to distilled water storage chamber and floods under the effect of gravity, the former water of water pipe in the middle of flowing through is carried out to the temperature that impregnated is heated to the distilled water in same distilled water storage chamber to be equated, former water in the middle of last in water pipe enters into and in evaporation cavity, is evaporated formation steam, distilled water in distilled water storage chamber is distilled water-circulating pump and is transported in heating chamber, so far surround the cyclic process of a heat.Quoting water emits through depotition cock.
The utility model also comprises the storage barrel on the port of export that is arranged on middle water pipe, is provided with the CD-ROM drive motor that drives condensation impeller to use in storage barrel, and described distilled water circulating 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 circulating pump are all arranged in storage barrel, and the heat discharging 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 circulating pump.The heat energy that CD-ROM drive motor and distilled water circulating pump produce is recycled utilization, not only can reduce heat supplementary while evaporation, also lowers the temperature to CD-ROM drive motor and distilled water circulating pump without 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 conformation, 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, when Jiang Yuanshui is heated to the required temperature of evaporation, and by the distilled water heating in distilled water storage chamber, required heat when the distilled water that makes to enter heating chamber can provide former water evaporation.Can start fast evaporation process.
As preferably, evaporation device is unsettled to be arranged in installation cavity, and distilled water storage chamber is surrounded by outer wall and the installation cavity of evaporation device.The heat that can prevent the distilled water in heating chamber is lost, and 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 unlimited chamber, upper end, and condensation impeller vertically arranges, condensation impeller housing lower end is opened wide completely and is formed air inlet, and air inlet is docking together with the openend sealing of evaporation cavity.Compact conformation, the track route of steam and distilled water is short, is lost to heat outside installation cavity few, makes to need to supplement after device start to go the heat for evaporating few.Patency when vapor flow is good.
As preferably, between condensation impeller and evaporation cavity, be provided with guide grids.Make steam enter steam channel with the traffic direction vertically rising, condensation effect is good.
As preferably, the side surface of described evaporation cavity forms evaporating surface, in described evaporation cavity, be provided with and can form structure along the vacuum liquid film of the circumferential rotation of evaporation cavity, described vacuum liquid film forms structure and comprises the blade, concentrate adsorption tube and the combination film forming device that set gradually from front to back according to the rotation direction of vacuum liquid film formation structure, and described combination film forming device comprises the film forming bar of the some directions of level distribution along the vertical direction extensions and the sparge pipe to film forming bar by raw water.Vacuum liquid film forms structure in the process of evaporation cavity rotation, blade is removed evaporating surface, make evaporating surface non-scaling, is ensured that follow-up former water has clean evaporating surface, is convenient to the adhesion of liquid film and the transmission of heat on the one hand, steam rising in vane drive evaporation cavity simultaneously, makes steam immediately leave evaporating surface and forms a negative pressure band higher than the vacuum in vacuum tank at the rear of blade (with rotation direction orientation); The concentrate adsorption tube that is positioned at blade rear is walked the instant absorption of concentrate remaining on evaporating surface, can on evaporation cavity especially evaporating surface, not assemble concentrate, further ensures the clean of evaporating surface; While outflow in the film forming bar of former water from 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 not being evaporated is transported to the evaporating surface that is positioned at negative pressure band place, the thinner thickness of liquid film, liquid film one contacts evaporating surface and is fallen by flash evaporation.Now remain in the concentrate that is on evaporating surface, the concentrate adsorption tube that concentrate is arrived soon after in time absorption is walked.
As preferably, in described evaporation cavity, be provided with dope feeder, described dope feeder is with being provided with the concentrate recovery pump that the concentrate in dope feeder is transported to sand filter water inlet end between described sand filter.Can improve the utilization rate of water.
The utility model also comprises feet, and described feet can slide up and down to be connected in described frame.Can adjust height of the present utility model, the requirement for height while use to meet different spaces.
The utility model also comprises refueling device, described refueling device comprises oil storage tank, oil discharge passage, rupture of membranes bar and corrosive liquid storage bin, described oil discharge passage is for being transported to the lubricating oil of described oil storage tank the auxiliary section of described feet and frame, described oil storage tank comprises at least two sheathed and cavitys of being fixed together successively, the lower wall of described cavity is provided with oil-out, described oil-out is sealedly connected with diaphragm seal, described rupture of membranes bar vertically extends and is positioned at the below of oil storage tank, described rupture of membranes bar, and the oil-out of all cavitys is all positioned on same vertical curve, in described corrosive liquid storage bin, be provided with the saturating formula floating drum of regular corruption, the saturating formula floating drum of described regular corruption comprises the rotproofness shell of lower ending opening and is somely expended and set the dividing plate that corrodes brokenly of duration by the corrosive liquid that can be corroded in liquid storage bin, described shell is partitioned into some floating chambers by described dividing plate, the quantity of described floating chamber equates with the quantity of described cavity, described dividing plate distributes along the vertical direction, described oil storage tank floats on the corrosive liquid in described corrosive liquid storage bin by described floating drum, described in each, floating chamber can both float described oil storage tank independently, the broken floating chamber of the every corrosion of corrosive liquid in corrosive liquid storage bin and cause in process that oil storage tank declines once, described rupture of membranes bar only can poke a diaphragm seal on cavity.Regularly self-lubricate.
The utlity model has following advantage: husky filter is set, can be stopped up by bulky grain thing by dust evaporation device, distilled water by making low temperature with steam direct contact heat transfer to impel steam-condensation to form the distilled water of high temperature, therefore the heat discharging when condensation is stored in the distilled water of high temperature, then make the distilled water of high temperature carry out heat exchange with former water, make the temperature of former water reach evaporating temperature, and go evaporation cavity to heat by the distilled water of high temperature, needed heat when former water evaporation is provided, the temperature of the former water of the temperature that makes the distilled water of discharging when just having entered is lessly high, heat major part circulates between evaporation and condensation, therefore need the heat of external complement less when evaporation, reduce the energy consumption in purificating raw water process, heat when condensation has obtained effective recycling, aqua storage tank is set, and environment protecting is good.
Brief description of the drawings
Fig. 1 is schematic diagram of the present utility model.
Fig. 2 is the schematic diagram of A-A of Fig. 1 when analysing and observe and not drawing water chamber.
Fig. 3 is the local enlarged diagram 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.
Schematic diagram when Fig. 6 is the broken floating chamber of refueling device corrosion.
Schematic diagram when Fig. 7 is broken two floating chambers of refueling device corrosion.
In figure: installation cavity 1, distilled water storage chamber 11, heating arrangements 12, storage barrel 13, heat exchanging chamber 14, husky filter 15, husky filter 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, efferent duct 222, rotating disk 23, vacuum liquid film forms structure 24, blade 241, combination film forming device 242, sparge pipe 2421, film forming bar 2422, concentrate suction pipe 243, vacuum source 25, dope feeder 26, concentrate recovery pump 261, condensation impeller 3, condensation impeller shaft 31, liquid storage cylinder 311, condensation impeller blade 32, blade part inlet opening 321, flanging 322, the surface 323 of the front side that is positioned at condensation wheel rotation direction of condensation impeller blade, crack 324, condensation impeller housing 33, apocenosis passage 331, air inlet 332, gas outlet 333, steam channel 34, feed pathway 35, frame 4, water chamber 41, aqua storage tank 42, depotition cock 43, three-way pipe 45, CD-ROM drive motor 5, distilled water circulating pump 6, sparge pipe 7, guide grids 8, refueling device 9, oil storage tank 91, cavity 911, oil-out 912, diaphragm seal 913, oil discharge passage 92, oil-feed bucket 921, fuel filler neck 922, rupture of membranes bar 93, corrosive liquid storage bin 94, regularly rotten formula floating drum 95 thoroughly, shell 951, dividing plate 952, floating chamber 953, guide rod 96, corrosive liquid 97, connecting rod 98.
Detailed description of the invention
Below in conjunction with accompanying drawing and embodiment, the utility model is further described.
Embodiment mono-, referring to Fig. 1, distillation type water dispenser, comprises frame 4.Frame 4 is provided with water chamber 41, aqua storage tank 42 and three-way pipe 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.
In frame 4, be also provided with installation cavity 1, evaporation device 2 and condensation impeller 3.
The top of installation cavity 1 is provided with husky filter 15.Installation cavity 1 outside is provided with concentrate 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.In distilled water storage chamber 11, be provided with heating arrangements 12.Heating arrangements 12 is electrothermal tube.Storage barrel 13 is installed in distilled water storage chamber 11.In storage barrel 13, be provided with CD-ROM drive motor 5 and distilled water circulating pump 6.The import of distilled water circulating pump 6 is connected with distilled water storage chamber 11 by pipeline.
Evaporation device 2 comprises the unlimited evaporation cavity in upper end 21, is looped around heating chamber 22 and the rotating disk 23 of evaporation cavity outer 21.Rotating disk 23 drives by CD-ROM drive motor 5.In heating chamber 22, be provided with multiple nozzles 221.The import of nozzle 221 is connected with the outlet of distilled water circulating pump 6 by pipeline.The outlet of nozzle 221 is towards the periphery wall of evaporation cavity 21 (periphery wall refers to the wall that evaporation cavity 21 and heating chamber 22 are separated).Evaporation cavity 21 is ring channel structures.
The top of evaporation cavity 21 is provided with dope feeder 26.Concentrate in dope feeder 26 is input in husky filter by the entrance point of concentrate recovery pump 261 and husky filter 15.In evaporation cavity 21, be provided with vacuum liquid film and form structure 24.Vacuum liquid film forms structure 24 and is driving the circumferential rotation along evaporation cavity 21 by rotating disk 23.Vacuum liquid film forms structure 24 and comprises blade 241, concentrate suction pipe 243 and combination film forming device 242.Combination film forming device 242 comprises the film forming bar 2422 on sparge pipe 2421 that is connected to of sparge pipe 2421 and some distributions along the vertical direction.Film forming bar 2422 along continuous straight runs extend.Sparge pipe 2421 vertically extends.The upper end of sparge pipe 2421 is fixed on rotating disk 23.In rotating disk 23, be provided with the passage that is communicated with storage barrel 13 and sparge pipe 2421.On rotating disk 23, be provided with vacuum source 25.Concentrate suction pipe 243 extends along the vertical direction.The upper end of concentrate suction pipe 243 is that the port of export is docking together with the entrance point of vacuum source 44, and the outlet of vacuum source 25 is positioned at the top of dope feeder 26.
Condensation impeller 3 is positioned at installation cavity 1 and is positioned at the top of evaporation device 2.
Condensation impeller 3 comprises condensation impeller shaft 31, condensation impeller blade 32 and the condensation impeller housing 33 of synchronous rotation.Condensation impeller housing 33 and installation cavity 1 surround heat exchanging chamber 14.Condensation impeller shaft 31 drives by CD-ROM drive motor 5.
In condensation impeller shaft 31, be provided with liquid storage cylinder 311.The inner of condensation impeller blade 32 wears in liquid storage cylinder 311.In liquid storage cylinder 311, be equipped with the sparge pipe 7 extending along the vertical direction.Condensation impeller blade 32 and condensation impeller shaft 31 seal affixed linking together.Condensation impeller blade 32 and condensation impeller shaft 31 are sealed and are fixed together by the mode of welding.The inner of condensation impeller blade 32 is provided with multiple blade part inlet openings 321.Blade part inlet opening 321 is along the axial distribution of condensation impeller shaft 31.The outer end of condensation impeller blade 31 is welded on the inner surface of condensation impeller housing 33.Between adjacent condensation impeller blade 32, form the axially extended steam channel 34 along condensation impeller shaft.33 times both ends opens of condensation impeller housing and form air inlet 332, upper end and open wide and form gas port 333.Condensation impeller housing 33 is provided with apocenosis passage 331.Condensation impeller housing 33 is docking together with the lateral wall sealing of evaporation cavity 21.Condensation impeller housing 33 can rotate with respect to evaporation cavity 21.Between condensation impeller 3 and evaporation cavity 21, be provided with guide grids 8.
The first port of three-way pipe 45 with heating chamber 22 link together, the second port with sparge pipe 7 link together, the 3rd port links together with water chamber 41.
The roof of installation cavity 1 is provided with vacuum orifice 18.
In installation cavity 1, be also provided with some middle water pipes 17.Middle water pipe 17 is heat exchanger tube.The import of middle water pipe 17 links together with intake antrum 16.Intake antrum 16 links together with the port of export of husky filter 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 in frame 4.Refueling device 9 comprises oil storage tank 91, oil discharge passage 92 and corrosive liquid storage bin 94.
One end of oil discharge passage 92 is provided with the oil-feed bucket 921, the other end that are positioned at oil storage tank below and is provided with the oil outlet 922 of the auxiliary section alignment of same feet and casing.Oil storage tank 91 is higher than oil outlet 922.
Corrosive liquid storage bin 94 links together with frame 4.Corrosive liquid storage bin 94 and oil-feed bucket 921 are fixed together.
Referring to Fig. 2, condensation impeller blade 32 is along the circumferential distribution of condensation impeller shaft 31.The inner of condensation impeller blade 32 be provided with along condensation wheel rotation direction in figure D to the flanging 322 of bending forward.Condensation impeller housing 33 is fixed together with condensation impeller shaft 31 by condensation impeller blade 32.The surface 323 of the front side that is positioned at condensation wheel rotation direction of condensation impeller blade is with the entrance point alignment of apocenosis passage 331.Apocenosis passage 331 recedes along condensation wheel rotation direction.
Heat exchanging chamber 14 is annular, and middle water pipe 17 has 16.Middle water pipe 17 being circumferentially distributed in heat exchanging chamber 14 along condensation impeller housing 313.
Referring to Fig. 3, between flanging 322 and condensation impeller blade 32, form crack 324.Crack 324 and blade part inlet opening 321 form feed pathway 35.
Referring to Fig. 4, vacuum liquid film forms structure 24 four.Four vacuum liquid films form knot enough 24 and are symmetrically distributed in evaporation cavity 21.Evenly be arranged so that without counterweight the stationarity can ensure to rotate time.In blade 241, concentrate adsorption tube 243 and the combination film forming device 242 rotation direction figure when using, E is to setting gradually from front to back.Film forming bar 2422 is conical rod, and film forming bar 2422 is perpendicular to the sidewall of evaporation cavity 21 and be located in sparge pipe 421.Concentrate adsorption tube 243 is positioned on the outside of evaporation cavity 21.Nozzle 221 is circumferentially uniformly distributed along heating chamber 22.
Referring to Fig. 5, refueling device also comprises rupture of membranes bar 93, regularly corruption formula floating drum 95 and guide rod 96 thoroughly.
Oil storage tank 91 links together with the saturating formula floating drum 95 of regularly corruption by connecting rod 98.Connecting rod 98 and regularly corruption are detachably connected by bolt between formula floating drum 95 thoroughly.Oil storage tank 91 comprises at least two the present embodiment being 4 sheathed and cavitys 911 of being fixed together successively.Lubricating oil (not drawing in lubricating oil figure) is housed in cavity 911.The lower wall of cavity 911 is provided with oil-out 912.Oil-out 912 is sealedly connected with diaphragm seal 913.4 cavitys amount to 4 oil-outs 912 be positioned on the vertical straight line of same and be positioned at rupture of membranes bar 93 directly over.Distance between adjacent diaphragm seal equates.
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 oil storage tank 91.
Corrosive liquid storage bin 94 is positioned at the below of oil storage tank 91.
Regularly rotten formula floating drum 95 is thoroughly positioned at corrosive liquid storage bin 94.Regularly rotten formula floating drum 95 thoroughly comprises rotproofness shell 951 and four 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 953 that distribute along the vertical direction by dividing plate 952.Distance between adjacent dividing plate equates.Distance between adjacent dividing plate equals the distance between adjacent diaphragm seal.
Guide rod 96 vertically extends.One end of guide rod 96 is fixed together with oil storage tank 91.The other end of guide rod 96 is located in upper bolster 1 slidably.
Referring to Fig. 6, in the time will starting refueling device, corrosive liquid 97 is injected in corrosive liquid storage bin 94, corrosive liquid 97 floats saturating regular corruption formula floating drum 95 and realize out floating of fuel tank 91, stops adding corrosive liquid when fuel reserve tank 91 floats in the time that the distance between rupture of membranes bar 93 and the diaphragm seal in outermost layer cavity is less than the distance between adjacent diaphragm seal.The buoyancy that each floating chamber 953 produces can both float oil storage tank 91 independently.In the present embodiment, corrosive liquid 97 is sodium hydroxide solution.Concentration by controlling corrosive liquid 97 is or/and the thickness of dividing plate, makes dividing plate to set liquid 97 corrosion that are corroded in duration broken, and these data can be learnt by test.
Reach one and set when duration, in dividing plate 952, be positioned at the dividing plate of below and be corroded brokenly when pouring the time of corrosive liquid 97 into, corrosive liquid enters and in floating chamber 953, is arranged in the floating chamber of below, oil storage tank 91 drop to by floating chamber 953 from below to up second floating chamber of number float, the diaphragm seal 913-1 that is arranged in outermost layer cavity in decline process is flow to oil discharge passage 92 by the lubricating oil that rupture of membranes bar 93 is poked, cavity 911 is arranged in outermost cavity by corresponding oil-out and flows to feet and carry out self-oiling one time with the auxiliary section of frame.
Referring to Fig. 7, reach two and set when duration when pouring the time of corrosive liquid 97 into, in dividing plate 952, being positioned at time dividing plate of below is also corroded brokenly, corrosive liquid enters the floating chamber that is arranged in inferior below in floating chamber 953, float the 3rd floating chamber that oil storage tank 91 drops to by counting from below to up in floating chamber 953, the diaphragm seal that is arranged in time outer cavity in decline process is also poked by rupture of membranes bar 93, after the lubricating oil that is arranged in time outer field cavity in cavity 911 is flowed out by the oil-out of the oil-out on inferior outer cavity and outermost layer cavity, drop onto oil discharge passage 92 and flow to feet and carry out self-oiling again with the auxiliary section of frame, the like, in the present embodiment, can carry out four times self-oiling, then change automatic fuelling device and carry out again self-oiling.
When use, referring to Fig. 1: through vacuum orifice 18, evaporation cavity 21 is evacuated down to required vacuum by vaccum-pumping equipment, CD-ROM drive motor 5 drive condensation impeller 3 according to the D in Fig. 2 to rotation.Low temperature distillation water in sparge pipe 7 under the effect of centrifugal force through feed pathway 35(referring to Fig. 3) provide and deliver and spread the surperficial 323(in front that is positioned at condensation impeller blade rotation direction at condensation impeller blade out referring to Fig. 2) on.Steam in evaporation cavity 21 enters in steam channel 34, with directly contact and the condensation be mixed into the distilled water of high temperature of the low temperature distillation water on condensation impeller 3 surfaces, hyperthermal distilled water from the outer end of condensation impeller blade 32 in apocenosis passage 331 is shed heat exchanging chamber 14, hyperthermal distilled water plays the effect of fountain heating to middle water pipe 17, the former coolant-temperature gage in middle water pipe 17 rises.Under Action of Gravity Field, hyperthermal distilled water gathers in distilled water storage chamber 11 and middle water pipe 17 is flooded, former water in middle water pipe 17 and the distilled water heat exchange in distilled water storage chamber 11 equate to temperature, former water is again in storage barrel 13 enters evaporation cavity 21 and evaporate, the dope of evaporation gained is under the effect of adsorption pump 25 within concentrate suction pipe 243 gathers concentrate pinching groove 26, and the concentrate in concentrate pinching groove 26 is discharged to husky filter 15 through concentrate recovery pump 261.Distilled water in distilled water storage chamber 11 enters in heating chamber 22 under the effect of distilled water circulating pump 6, provide heat for the former water evaporation in evaporation cavity 21, the distilled water in heating chamber 22 declined by temperature after absorbing heat (temperature can higher than the temperature that just enters the former water of installation cavity 1 when interior).Distilled water in heating chamber 22 through three-way pipe 45 parts stretch out and be stored in water chamber 41, another part outputs to sparge pipe 7 and enters feed pathway 35(referring to Fig. 3) in.Whole process so circulates.After the water in water chamber 41 is full, stop water purifying.Former water in storage barrel 13 is that under the negative-pressure adsorption effect in installation cavity 1, the passage in rotating disk 23 enters sparge pipe 2421, under the effect of centrifugal force, spread out on film forming bar 2422 and flow on the lateral wall inner surface of evaporation cavity 21 with membranaceous, in this process, completing evaporation.Blade 241 plays the lateral wall inner surface of clean evaporation cavity 11 and forms lower subnormal ambient to accelerate to evaporate and reduce the effect of evaporating temperature.
For ease of read and comprehend, flow path to former water and distilled water is summarized as follows, the flow path of distilled water is: distilled water → heat exchanging chamber 14 → distilled water storage chamber 11 → distilled water circulating pump 6 → nozzle 221 → heating chamber 22 → three-way pipe 45, start walking along separate routes, a part of distilled water enters water chamber 41, another side divides distilled water → sparge pipe 7 → liquid storage cylinder 311 → blade part inlet opening 321 → crack 324 → condensation impeller blade 32 → heat exchanging chamber 14.The flow path of former water is: the lateral wall inner surface of former water → husky filter water inlet port 151 → husky filter 15 → intake antrum 16 → middle water pipe 17 → storage barrel 13 → rotating disk 23 → sparge pipe 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 vapour → condensation impeller blade 32, and another part forms concentrate → concentrate suction pipe 243 → dope feeder 26 → concentrate recovery pump 261 → husky filter water inlet port 151 → husky filter 15.When system has just driven, need to open heating arrangements 12 so that evaporation process drives, then judge whether to need additional heat to maintain evaporation process by the temperature that detects the former water in storage barrel 13, if the temperature of the former water in storage barrel is lower than the required temperature of evaporation, represent that heat number of dropouts is greater than the heat that pure liquid circulating pump 6 and CD-ROM drive motor 5 discharge, now by starting temperature that heating arrangements 12 improves the distilled water in former water and distilled water storage chamber 11 to meeting the requirements.
While needing water, grip water tumbler and make water tumbler be positioned at depotition cock 43 belows.Open depotition cock 43, the water in water chamber 41 flows to water tumbler through depotition cock 43.In the time that the water of depotition cock 43 poor sealings or water tumbler overflows, leak the water that overflows and be collected in aqua storage tank 42 and prevent that water clock is to ground.
Claims (10)
1. a distillation type water dispenser, comprises frame, and described frame is provided with sand filter and water chamber, and 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 of depotition cock below, be provided with the installation cavity of vacuum orifice, heating arrangements, middle water pipe, distilled water circulating pump, distilled water storage chamber, three-way pipe, and be positioned at condensation impeller and the evaporation device of installation cavity, described evaporation device comprises evaporation cavity and be looped around the heating chamber outside evaporation cavity, and described condensation impeller comprises the condensation impeller shaft of synchronous rotation, condensation impeller blade, carry distilled water to the lip-deep feed pathway of condensation impeller blade and condensation impeller housing, between adjacent condensation impeller blade, form steam channel, condensation impeller housing is provided with air inlet, gas outlet and the liquid outlet channel aliging with the outer end of condensation impeller blade, air inlet docks with evaporation cavity, condensation impeller housing is with forming heat exchanging chamber between installation cavity, heat exchanging chamber is connected with distilled water storage chamber, middle water pipe is heat exchanger tube, and one end of middle water pipe links together with the port of export of sand filter, the other end is successively through being connected with evaporation cavity after heat exchanging chamber and distilled water storage chamber, and distilled water circulating pump is for being transported to heating chamber by the distilled water in distilled water storage chamber, and the first port of described three-way pipe links together with described heating chamber, the second port links together with described feed pathway, the 3rd port links together with described water chamber.
2. distillation type water dispenser according to claim 1, it is characterized in that, also comprise the storage barrel on the port of export that is arranged on middle water pipe, in storage barrel, be provided with the CD-ROM drive motor that drives condensation impeller to use, described distilled water circulating pump is positioned at described storage barrel, and middle water pipe is connected with evaporation cavity by storage barrel.
3. distillation type water dispenser 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. distillation type water dispenser 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 outer wall and the installation cavity of evaporation device.
5. distillation type water dispenser 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 unlimited chamber, upper end, condensation impeller vertically arranges, condensation impeller housing lower end is opened wide completely and is formed air inlet, and air inlet is docking together with the openend sealing of evaporation cavity.
6. distillation type water dispenser according to claim 5, is characterized in that, between condensation impeller and evaporation cavity, is provided with guide grids.
7. according to the distillation type water dispenser described in claim 5 or 6, it is characterized in that, the side surface of described evaporation cavity forms evaporating surface, in described evaporation cavity, be provided with and can form structure along the vacuum liquid film of the circumferential rotation of evaporation cavity, described vacuum liquid film forms structure and comprises the blade, concentrate adsorption tube and the combination film forming device that set gradually from front to back according to the rotation direction of vacuum liquid film formation structure, and described combination film forming device comprises the film forming bar of the some directions of level distribution along the vertical direction extensions and the sparge pipe to film forming bar by raw water.
8. distillation type water dispenser according to claim 7, it is characterized in that, in described evaporation cavity, be provided with dope feeder, described dope feeder is with being provided with the concentrate recovery pump that the concentrate in dope feeder is transported to sand filter water inlet end between described sand filter.
9. according to the distillation type water dispenser described in claim 1 or 2 or 3 or 4 or 5 or 6, it is characterized in that, also comprise feet, described feet can slide up and down to be connected in described frame.
10. distillation type water dispenser according to claim 9, it is characterized in that, also comprise refueling device, described refueling device comprises oil storage tank, oil discharge passage, rupture of membranes bar and corrosive liquid storage bin, described oil discharge passage is for being transported to the lubricating oil of described oil storage tank the auxiliary section of described feet and frame, described oil storage tank comprises at least two sheathed and cavitys of being fixed together successively, the lower wall of described cavity is provided with oil-out, described oil-out is sealedly connected with diaphragm seal, described rupture of membranes bar vertically extends and is positioned at the below of oil storage tank, described rupture of membranes bar, and the oil-out of all cavitys is all positioned on same vertical curve, in described corrosive liquid storage bin, be provided with the saturating formula floating drum of regular corruption, the saturating formula floating drum of described regular corruption comprises the rotproofness shell of lower ending opening and is somely expended and set the dividing plate that corrodes brokenly of duration by the corrosive liquid that can be corroded in liquid storage bin, described shell is partitioned into some floating chambers by described dividing plate, the quantity of described floating chamber equates with the quantity of described cavity, described dividing plate distributes along the vertical direction, described oil storage tank floats on the corrosive liquid in described corrosive liquid storage bin by described floating drum, described in each, floating chamber can both float described oil storage tank independently, the broken floating chamber of the every corrosion of corrosive liquid in corrosive liquid storage bin and cause in process that oil storage tank declines once, described rupture of membranes bar only can poke a diaphragm seal on cavity.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420219024.1U CN203861021U (en) | 2014-05-02 | 2014-05-02 | Distillation type water dispenser |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420219024.1U CN203861021U (en) | 2014-05-02 | 2014-05-02 | Distillation type water dispenser |
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| CN203861021U true CN203861021U (en) | 2014-10-08 |
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| CN201420219024.1U Expired - Fee Related CN203861021U (en) | 2014-05-02 | 2014-05-02 | Distillation type water dispenser |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104433797A (en) * | 2014-11-10 | 2015-03-25 | 江苏创兰太阳能空调有限公司 | Water dispenser |
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2014
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104433797A (en) * | 2014-11-10 | 2015-03-25 | 江苏创兰太阳能空调有限公司 | Water dispenser |
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