CN203833657U - Household water processing mechanism - Google Patents
Household water processing mechanism Download PDFInfo
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- CN203833657U CN203833657U CN201420219012.9U CN201420219012U CN203833657U CN 203833657 U CN203833657 U CN 203833657U CN 201420219012 U CN201420219012 U CN 201420219012U CN 203833657 U CN203833657 U CN 203833657U
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Abstract
The utility model relates to water processing equipment, in particular to a household water processing mechanism. According to the household water processing mechanism, water is processed through a distilling method, water dropped from a faucet can be collected, and the collected water can not overflows. The household water processing mechanism comprises a machine frame provided with a water supply cavity, a water storage trough, an evaporation mechanism, an installation cavity, a heating mechanism, a raw water input pipe, a condensation impeller, an air pipe, a distilled water circulation pump, a distilled water storage cavity, a t-branch pipe and a ball float valve, wherein the water supply cavity is provided with a water outlet faucet, the evaporation mechanism is provided with an evaporation cavity, the condensation impeller is arranged in the installation cavity, the air pipe is used for vacuumizing the evaporation cavity, and the ball float valve is used for controlling opening and closing of the water outlet faucet and the water supply cavity, the water storage trough is located below the water outlet faucet, a floating ball of the ball float valve is located in the water storage trough, the evaporation mechanism further comprises a heating cavity surrounding the evaporation cavity, and raw water is evaporated by the evaporation device and condensed by the condensation impeller to form purified water and be stored in the water supply cavity. The household water processing mechanism solves the problems that as for an existing water processing mechanism, the removing effect of small-particle impurities in the water is low, and the dropped water can not be collected.
Description
Technical field
The utility model relates to water treating equipment, relates in particular to a kind of service water processing mechanism.
Background technology
The structure formation of existing service water processing mechanism has multiple.As China Patent No. ZL2005101304043, within open day, be June 13 in 2007 day, in being called the patent documentation of " a kind of method and apparatus that prevents domestic water purifier discharge water from generating secondary pollution ", a kind of service water processing mechanism is disclosed.Existing service water processing mechanism adopts filtration method to purify water more, needs often to clean or change filtering membrane, therefore not only uses inconvenience but also the poor removal effect to the small-particle impurity in water; When depotition cock produces water clock, water can trickle to ground.
Utility model content
The service water processing mechanism that the utility model provides a kind of method water that water is processed, that can collect depotition cock water clock by distillation and the water in aqua storage tank can not produce spillover, has solved existing service water processing mechanism to the poor removal effect of small-particle impurity in water, the water of water clock can trickle to ground problem.
Above technical problem solves by following technical proposal: a kind of service water processing mechanism, comprise frame, described frame is provided with water chamber, described water chamber is provided with the depotition cock of downward water outlet, described frame is also provided with aqua storage tank, the evaporation device with evaporation cavity, be provided with the installation cavity of vacuum orifice, heating arrangements, former water inlet pipe, be built in the condensation impeller of installation cavity, distilled water recycle pump, distilled water storage chamber, Y-tube, and the float(ing)valve of controlling the break-make of described depotition cock and described water chamber, described aqua storage tank is positioned at the below of described depotition cock, described float(ing)valve is normally open valve, described float(ing)valve comprises valve body, the ball float of spool and the folding of driving spool, described ball float is positioned at described aqua storage tank, described aqua storage tank is provided with limiting water level, when the water level in aqua storage tank reaches capacity water level, described float(ing)valve is in closing condition, described evaporation device also comprises the heating chamber being looped around outside evaporation cavity, described condensation impeller comprises the condensation impeller shaft of synchronous rotation, condensation impeller vane, carry distilled water to the lip-deep feed pathway of condensation impeller vane and condensation impeller housing, between adjacent condensation impeller blade, form vapour passage, condensation impeller housing is provided with inlet mouth, air outlet and the liquid outlet channel aliging with the outer end of condensation impeller vane, inlet mouth 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, former water inlet pipe is heat transfer tube, former water inlet pipe is successively through being connected with evaporation cavity after heat exchanging chamber and distilled water storage chamber, distilled water recycle pump is for being transported to heating chamber by the distilled water in distilled water storage chamber, the first port of described Y-tube links together with described heating chamber, the second port links together with described feed pathway, the 3rd port links together with described water chamber.During use, former water in evaporation cavity absorbs the heat of the distilled water in heating chamber while 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, 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 vane after flowing into feed pathway, the condensation impeller centrifugal force that rotation produces continuously makes to be dispersed on the surface of condensation impeller vane through the distilled water of the low temperature of feed pathway inflow, vapour stream in evaporation cavity directly contacts and produces heat exchange and condensation with low-temperature distillation water 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 (being outer end) of condensation impeller vane through liquid outlet channel, hyperthermal distilled water enters in the process of heat exchanging chamber and is shed on former water inlet pipe, former water to the former water inlet pipe of flowing through carries out spray-type heating, former water is forwarded in distilled water storage chamber in former water inlet pipe, hyperthermal distilled water converges to the part that in distilled water storage chamber, former water inlet pipe is positioned to distilled water storage chamber and floods under the effect of gravity, the former water of the former water inlet pipe 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 last former water inlet 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 working cycle of a heat.Quoting water emits depotition cock.Producing leading water clock water that go out or that water tumbler overflows is collected in aqua storage tank.When the water in aqua storage tank reaches capacity water level, ball float floats to float(ing)valve is closed, thereby makes the depotition cock can not water outlet, plays anti-sealing and spills into ground effect, environmental protection.
The utility model also comprises the storage barrel on the exit end that is arranged on former water inlet pipe, is provided with the CD-ROM drive motor that drives condensation impeller to use in storage barrel, and described distilled water recycle pump is positioned at described storage barrel, and former water inlet pipe is connected with evaporation cavity by storage barrel.CD-ROM drive motor and distilled water recycle 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 recycle pump.The heat energy that CD-ROM drive motor and distilled water recycle pump produce is recycled utilization, not only can reduce heat supplementary while evaporating, and also without additional mechanism providing additional operation, to CD-ROM drive motor and distilled water recycle pump, lowers the temperature.
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, 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 evaporative 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 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, and making needs the supplementary less calories for evaporating that goes after 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 rising, condensation effect is good.
As preferably, the side surface of described evaporation cavity forms generating 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 blade, concentrated solution adsorption tube and the combination film forming device setting gradually from front to back according to the turning 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 water distributing pipe to film forming bar by raw water.Vacuum liquid film forms structure in the process of evaporation cavity rotation, blade is removed generating surface, make water surface of evaporation non-scaling, is guaranteed that follow-up former water has clean water surface of evaporation, is convenient to the adhesion of liquid film and the transmission of heat on the one hand, steam rising in vane drive evaporation cavity, makes steam immediately leave generating surface and forms a negative pressure band higher than the vacuum tightness in vacuum vessel at the rear of blade (directed with turning direction) simultaneously; The concentrated solution adsorption tube that is positioned at blade rear is walked the instant absorption of concentrated solution remaining on generating surface, can on evaporation cavity especially generating surface, not assemble concentrated solution, further guarantees the clean of generating surface; While flowing out in the film forming bar of former water from combination film forming device, effect due to 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 generating surface that is positioned at negative pressure band place, the thinner thickness of liquid film, liquid film one contact generating surface is fallen by flash evaporation.Now remain in the concentrated solution that is on generating surface, the concentrated solution adsorption tube that concentrated solution is arrived soon after in time absorption is walked.
The utlity model has following advantage: the distilled water by making low temperature with steam direct contact heat transfer to impel vapor condensation to form the distilled water of high temperature, therefore the heat discharging during 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 vaporization 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 during evaporation, reduced the energy consumption in purificating raw water process, heat during condensation has obtained effective recycling, adopt the mode of distillation to carry out water purification, good purification, aqua storage tank is set, and environment protecting is good, float(ing)valve is set, and the water in aqua storage tank can not overflow, and has further improved environment protecting.
Accompanying drawing explanation
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.
In figure: installation cavity 1, distilled water storage chamber 11, heating arrangements 12, storage barrel 13, heat exchanging chamber 14, original water inlet 15, intake antrum 16, former water inlet 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 forms 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 discharge outlet 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 of the front side that is positioned at 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, depotition cock 43, Y-tube 45, CD-ROM drive motor 5, distilled water recycle pump 6, water distributing pipe 7, guide grids 8, ball valve 9, valve body 91, ball float 92, connecting rod 93.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the utility model is further described.
Embodiment mono-, and referring to Fig. 1, a kind of service water processing mechanism, comprises frame 4 and float(ing)valve 9.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 42 is positioned at the below of depotition cock 43.
Float(ing)valve 9 is normally open valve.Float(ing)valve 9 is for controlling the break-make of depotition cock 43 and water chamber 41.Float(ing)valve 9 comprises valve body 91, is positioned at spool and the ball float 92 of valve body.Ball float 92 links together with spool by connecting rod 93.Ball float 92 is positioned at aqua storage tank 42.Aqua storage tank is provided with limiting water level; When the water level in aqua storage tank reaches capacity water level, described float(ing)valve is in closing condition.
In frame 4, be also provided with installation cavity 1, evaporation device 2 and condensation impeller 3.
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 recycle pump 6.The import of distilled water recycle 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 a plurality of nozzles 221.By pipeline, the outlet with distilled water recycle pump 6 is connected in the import of nozzle 221.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 receiving tank 26.Dope receiving tank 26 is provided with the concentrated solution discharge outlet 261 that stretches out installation cavity 1.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, concentrated solution suction pipe 243 and combination film forming device 242.Combination film forming device 242 comprises the film forming bar 2422 on water distributing pipe 2421 that is connected to of water distributing pipe 2421 and some distributions along the vertical direction.Film forming bar 2422 along continuous straight runs extend.Water distributing pipe 2421 vertically extends.The upper end of water distributing 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 water distributing pipe 2421.On rotating disk 23, be provided with vacuum source 25.Concentrated solution suction pipe 243 extends along the vertical direction.To be exit end be docking together with the entrance end of vacuum source 44 in the upper end of concentrated solution suction pipe 243, 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 condensation impeller shaft 31, condensation impeller vane 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 vane 32 wears in liquid storage cylinder 311.In liquid storage cylinder 311, be equipped with the water distributing pipe 7 extending along the vertical direction.Condensation impeller vane 32 and affixed the linking together of condensation impeller shaft 31 sealing.Condensation impeller vane 32 and condensation impeller shaft 31 are sealed and are fixed together by the mode of welding.The inner of condensation impeller vane 32 is provided with a plurality of 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 vane 31 is welded on the internal surface of condensation impeller housing 33.Between adjacent condensation impeller blade 32, form the axially extended vapour passage 34 along condensation impeller shaft.33 times both ends opens of condensation impeller housing and form inlet mouth 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 outer side 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 Y-tube 45 with heating chamber 22 link together, the second port with water distributing 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 former water inlet pipes 17.Former water inlet pipe 17 is heat transfer tube.The import of former water inlet pipe 17 links together with intake antrum 16.By original water inlet 15, the outside with installation cavity 1 is connected intake antrum 16.Former water inlet pipe 17 is from top to bottom successively through heat exchanging chamber 14 and distilled water storage chamber 11.The outlet of former water inlet pipe 17 is connected with storage barrel 13.
Referring to Fig. 2, condensation impeller vane 32 is along the circumferential distribution of condensation impeller shaft 31.The inner of condensation impeller vane 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 vane 32.The surface 323 of the front side that is positioned at condensation wheel rotation direction of condensation impeller vane is with the entrance end alignment of apocenosis passage 331.Apocenosis passage 331 recedes along condensation wheel rotation direction.
Heat exchanging chamber 14 is annular, and former water inlet pipe 17 has 16.Former water inlet pipe 17 is circumferentially distributed in heat exchanging chamber 14 along condensation impeller housing 313.
Referring to 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.
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 in the time of can guaranteeing to rotate.In blade 241, concentrated solution adsorption tube 243 and the combination film forming device 242 turning 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 water distributing pipe 421.Concentrated solution adsorption tube 243 is positioned on the outside of evaporation cavity 21.Nozzle 221 is circumferentially uniformly distributed along heating chamber 22.
During use, referring to Fig. 1: by vaccum-pumping equipment, through 18 pairs of evaporation cavities 21 of vacuum orifice, be evacuated down to required vacuum tightness, CD-ROM drive motor 5 drive condensation impellers 3 according to the D in Fig. 2 to rotation.Low-temperature distillation water in water distributing pipe 7 under the effect of centrifugal force through feed pathway 35(referring to Fig. 3) provide and deliver and spread out at condensation impeller vane, be positioned at condensation impeller vane turning direction the surperficial 323(in the place ahead referring to Fig. 2) on.Steam in evaporation cavity 21 enters in vapour passage 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 vane 32 in apocenosis passage 331 is shed heat exchanging chamber 14, hyperthermal distilled water plays the effect of spray-type heating to former water inlet pipe 17, the former water temp in former water inlet pipe 17 rises.Under action of gravity, hyperthermal distilled water gathers in distilled water storage chamber 11 and former water inlet pipe 17 is flooded, former water in former water inlet 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 absorbent pump 25 within concentrated solution suction pipe 243 gathers concentrated solution pinching groove 26, and the concentrated solution in concentrated solution pinching groove 26 is discharged through concentrated solution discharge outlet 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, 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 Y-tube 45 parts stretch out and be stored in water chamber 41, another part outputs to water distributing pipe 7 and enters feed pathway 35(referring to Fig. 3) in.Whole process so circulates.Water in water chamber 41 after expiring stops water purifying.While needing water, water tumbler is shelved on the position that is positioned at depotition cock 43 belows on shelf 44, open depotition cock 43, water in water chamber 41 flow in water tumbler, when water tumbler water overflow or when depotition cock 43 produces weeping, the water of omitting out is collected in water storage cavity 42, play and prevent trickling to ground and affect sanitary effect.
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 water distributing pipe 2421, under the effect of centrifugal force, with membranaceous, spread out on film forming bar 2422 and flow on the outer side wall internal surface of evaporation cavity 21, in this process, completing evaporation.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, flowing-path to former water and distilled water is summarized as follows, the flowing-path of distilled water is: heat exchanging chamber 14 → distilled water storage chamber 11 → distilled water recycle pump 6 → nozzle 221 → heating chamber 22 → Y-tube 45, start walking along separate routes, a part is through entering water chamber 41, divide → water distributing pipe of the other side 7 → liquid storage cylinder 311 → blade part inlet opening 321 → crack 324 → condensation impeller impeller 32 → heat exchanging chamber 14.The flowing-path of former water is: the outer side wall internal surface evaporation of former water admission port 15 → intake antrum 16 → former water inlet pipe 17 → storage barrel 13 → rotating disk 23 → water jet standpipe 2422 → film forming bar 2421 → evaporation cavity 21.When system has just driven, need to open heating arrangements 12 so that evaporative process drives, then by detecting the temperature of the former water in storage barrel 13, judge whether to need additional heat to maintain evaporative process, 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 recycle 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, hand-held water tumbler makes water tumbler be positioned at depotition cock 43 belows.Open depotition cock 43, the water in water chamber 41 flows to water tumbler through float(ing)valve 9 and depotition cock 43 successively.When the water of depotition cock 43 poor sealings or water tumbler overflows, leak the water overflowing and be collected in aqua storage tank 42.Along with rising, the float 92 of the water level in aqua storage tank 42 floated gradually, the spool that float 92 drives in valve bodies 91 by connecting rod 93; Water level in aqua storage tank 4 reach capacity water level (" limiting water level " refer to setting can time the float(ing)valve water level of closing) time, float 92 drives float(ing)valve 9 to cut out, make whether no matter depotition cock 43 is opened, the water in water storage cavity 41 can not flow out through depotition cock 43, thereby further play the water preventing in aqua storage tank 4, overflow and trickle to ground effect.
Claims (7)
1. a service water processing mechanism, comprise frame, described frame is provided with water chamber, described water chamber is provided with the depotition cock of downward water outlet, it is characterized in that, described frame is also provided with aqua storage tank, the evaporation device with evaporation cavity, be provided with the installation cavity of vacuum orifice, heating arrangements, former water inlet pipe, be built in the condensation impeller of installation cavity, distilled water recycle pump, distilled water storage chamber, and Y-tube, and the float(ing)valve of controlling the break-make of described depotition cock and described water chamber, described aqua storage tank is positioned at the below of described depotition cock, described float(ing)valve is normally open valve, described float(ing)valve comprises valve body, the ball float of spool and the folding of driving spool, described ball float is positioned at described aqua storage tank, described aqua storage tank is provided with limiting water level, when the water level in aqua storage tank reaches capacity water level, described float(ing)valve is in closing condition, described evaporation device also comprises the heating chamber being looped around outside evaporation cavity, described condensation impeller comprises the condensation impeller shaft of synchronous rotation, condensation impeller vane, carry distilled water to the lip-deep feed pathway of condensation impeller vane and condensation impeller housing, between adjacent condensation impeller blade, form vapour passage, condensation impeller housing is provided with inlet mouth, air outlet and the liquid outlet channel aliging with the outer end of condensation impeller vane, inlet mouth 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, former water inlet pipe is heat transfer tube, former water inlet pipe is successively through being connected with evaporation cavity after heat exchanging chamber and distilled water storage chamber, distilled water recycle pump is for being transported to heating chamber by the distilled water in distilled water storage chamber, the first port of described Y-tube 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. service water processing mechanism according to claim 1, it is characterized in that, also comprise the storage barrel on the exit end that is arranged on former water inlet pipe, in storage barrel, be provided with the CD-ROM drive motor that drives condensation impeller to use, described distilled water recycle pump is positioned at described storage barrel, and former water inlet pipe is connected with evaporation cavity by storage barrel.
3. service water processing mechanism 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. service water processing mechanism 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. service water processing mechanism 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 inlet mouth, and inlet mouth is docking together with the opening end sealing of evaporation cavity.
6. service water processing mechanism according to claim 5, is characterized in that, between condensation impeller and evaporation cavity, is provided with guide grids.
7. according to the service water processing mechanism described in claim 5 or 6, it is characterized in that, the side surface of described evaporation cavity forms generating 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 blade, concentrated solution adsorption tube and the combination film forming device setting gradually from front to back according to the turning 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 water distributing pipe to film forming bar by raw water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420219012.9U CN203833657U (en) | 2014-05-02 | 2014-05-02 | Household water processing mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420219012.9U CN203833657U (en) | 2014-05-02 | 2014-05-02 | Household water processing mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203833657U true CN203833657U (en) | 2014-09-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420219012.9U Expired - Fee Related CN203833657U (en) | 2014-05-02 | 2014-05-02 | Household water processing mechanism |
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| CN (1) | CN203833657U (en) |
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2014
- 2014-05-02 CN CN201420219012.9U patent/CN203833657U/en not_active Expired - Fee Related
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