CN104163461A - Novel water treatment purifier - Google Patents
Novel water treatment purifier Download PDFInfo
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- CN104163461A CN104163461A CN201410184079.8A CN201410184079A CN104163461A CN 104163461 A CN104163461 A CN 104163461A CN 201410184079 A CN201410184079 A CN 201410184079A CN 104163461 A CN104163461 A CN 104163461A
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Abstract
本发明涉及水处理设备。一种新型水处理净化器，包括机架，机架设有具有出水龙头的供水腔、储水槽、沙过滤器、具有蒸发腔的蒸发机构、安装腔、加热机构、中间水管、内置于安装腔的冷凝叶轮、给蒸发腔抽真空用的气管、蒸馏水循环泵、蒸馏水储存腔和三通管，储水槽位于出水龙头的下方，蒸发机构还包括环绕在蒸发腔外的加热腔，原水经沙过滤器过滤后被蒸发装置蒸发、再被冷凝叶轮冷凝后形成净化水而储存在供水腔中。本发明提供了一种对蒸汽冷凝时所释放出的热量进行回收以用于原水的蒸发、使得热量在蒸发与冷凝之间进行循环利用的新型水处理净化器，解决了现有的水处理净化器使用不便且对水中的小颗粒杂质的去除效果差的问题。
The present invention relates to water treatment equipment. A new type of water treatment purifier, including a frame, the frame is equipped with a water supply chamber with a water outlet, a water storage tank, a sand filter, an evaporation mechanism with an evaporation chamber, an installation chamber, a heating mechanism, an intermediate water pipe, and a built-in installation chamber. Condensing impeller, air pipe for vacuuming the evaporation chamber, distilled water circulation pump, distilled water storage chamber and tee pipe, the water storage tank is located under the water outlet tap, the evaporation mechanism also includes a heating chamber surrounding the evaporation chamber, and the raw water passes through the sand filter After being filtered, it is evaporated by the evaporating device, condensed by the condensing impeller, and then purified water is formed and stored in the water supply chamber. The present invention provides a new type of water treatment purifier that recovers the heat released during steam condensation to be used for the evaporation of raw water, so that the heat can be recycled between evaporation and condensation, and solves the problem of existing water treatment and purification. The problem is that the device is inconvenient to use and the removal effect of small particles of impurities in water is poor.
Description
Technical field
The present invention relates to water treating equipment, relate in particular 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 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 discharge water from generating secondary pollution ", a kind of novel water treatment purifier is disclosed.Existing a kind of novel water treatment purifier 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.
Summary of the invention
The invention provides a kind of heat discharging during to vapor condensation and reclaim for former evaporation of water, a kind of novel water treatment purifier that makes heat carry out recycle between evaporation and condensation, solved existing a kind of novel water treatment purifier and used inconvenience and the problem to the poor removal effect of the small-particle impurity in water.
Above technical problem solves 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 of depotition cock below, 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 the condensation impeller and the evaporation device that are positioned at 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 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, 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 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 is transported in evaporation cavity and evaporates by middle water pipe after husky strainer filters, 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 middle water pipe, former water to water pipe in the middle of flowing through carries out spray-type 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 working cycle of a heat.Quoting water emits through depotition cock.
The present invention also comprises the storage barrel on the exit end 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 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, 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.
As preferably, in described evaporation cavity, be provided with dope receiving tank, described dope receiving tank with between described sand filter, be provided with by dope receiving tank from concentrated solution described in to the concentrated solution recovery pump of sand filter feed-water end.Can improve the utilization ratio of water.
The present invention also comprises feet, and described feet can slide up and down to be connected in described frame.Can adjust height of the present invention, the requirement for height while using to meet different spaces.
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 for being transported to the lubricating oil of described storage tank the matching part of described feet and frame, described storage tank comprises at least two sheathed and cavitys of being fixed together successively, 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, in described corrosive fluid 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 somely by the corrosive fluid in the liquid bin that can be corroded, is expended and set the dividing plate that duration corrodes brokenly, described dividing plate is partitioned into some floating chambers by described shell, the quantity of described floating chamber equates 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 in each, floating chamber can both float described storage tank independently, corrosive fluid in corrosive fluid bin every corrosion Po Yige floating chamber and cause in process that storage tank declines once, described rupture of membranes bar only can poke a sealing membrane on cavity.Regularly self-lubrication.
As preferably, on described aqua storage tank, be stamped shelf.Can improve the accessibility while using.
As preferably, the sidewall of described aqua storage tank is provided with some brace rods, and described shelf is by being shelved on described brace rod and link together with described aqua storage tank, 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: husky strainer is set, can by macrobead thing, be stopped up by dust evaporation device, 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, aqua storage tank is set, and environment protecting is good.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention.
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 refueling device corrosion Po Yige floating chamber.
Schematic diagram when Fig. 7 is refueling device corrosion Po Erge floating chamber.
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 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 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 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, 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, regularly corruption is formula floating drum 95 thoroughly, 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 mono-, and referring to 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.On aqua storage tank 42, be 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 is by being shelved on brace rod 421 and link together with aqua storage tank 42.The upper surface of shelf 44 is provided with non-skid finish.
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 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.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.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.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 middle water pipes 17.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 in 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 is provided with the oil outlet 922 that the oil-feed bucket 921, the other end that are positioned at storage tank below are provided with the matching part alignment of 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.
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 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 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.
Referring to Fig. 5, refueling device also comprises rupture of membranes bar 93, regularly corruption formula floating drum 95 and guide rod 96 thoroughly.
Storage tank 91 links 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.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 outlet 912.Oil outlet 912 is sealedly connected with sealing membrane 913.4 cavitys amount to 4 oil outlets 912 be positioned on the vertical straight line of same and be positioned at rupture of membranes bar 93 directly over.Distance between adjacent sealing membrane 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 storage tank 91.
Corrosive fluid bin 94 is positioned at the below of storage tank 91.
Regularly rotten formula floating drum 95 is thoroughly positioned at corrosive fluid 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.Dividing plate 952 is divided into 4 floating chambers 953 that distribute along the vertical direction by shell 951.Distance between adjacent dividing plate equates.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.
Referring to Fig. 6, in the time will starting refueling device, corrosive fluid 97 is injected in corrosive fluid bin 94, corrosive fluid 97 floats the saturating formula floating drum 95 of regular corruption and realize out floating of fuel tank 91, when fuel reserve tank 91 floats, stops adding corrosive fluid when the distance between rupture of membranes bar 93 and the sealing membrane in outermost layer cavity is less than the distance between adjacent sealing membrane.The buoyancy that each floating chamber 953 produces can both float storage tank 91 independently.In the present embodiment, corrosive fluid 97 is sodium hydroxide solution.Concentration by controlling corrosive fluid 97 is or/and the thickness of dividing plate, makes dividing plate liquid 97 corrosion that are corroded in setting duration broken, and these data can be learnt by test.
When pouring the time of corrosive fluid 97 into, reach one while setting duration, in dividing plate 952, be positioned at the dividing plate of below and be corroded brokenly, corrosive fluid enters and in floating chamber 953, is arranged in the floating chamber of below, storage tank 91 drop to by floating chamber 953 from below to up second floating chamber of number float, the sealing membrane 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 outlet and flows to feet and carry out self-oiling one time with the matching part of frame.
Referring to Fig. 7, when pouring the time of corrosive fluid 97 into, reach two while setting duration, in dividing plate 952, being positioned at time dividing plate of below is also corroded brokenly, corrosive fluid enters the floating chamber that is arranged in inferior below in floating chamber 953, storage tank 91 drop to by floating chamber 953 from below to up several San Ge floating chamber float, the sealing membrane that is arranged in time outer cavity in decline process is also poked by rupture of membranes bar 93, after the oil outlet of the oil outlet of the lubricating oil that is arranged in time outer field cavity in cavity 911 on inferior outer cavity and outermost layer cavity flows out, drop onto oil discharge passage 92 and flow to feet and carry out self-oiling again with the matching part 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.
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 middle water pipe 17, the former water temp in middle water pipe 17 rises.Under action of gravity, hyperthermal distilled water gathers in distilled water storage chamber 11 and middle water pipe 17 is flooded, former water and the distilled water heat exchange in distilled water storage chamber 11 in middle water pipe 17 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 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, 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.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: distilled water → 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 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 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, water tumbler is also shelved on the position that is positioned at depotition cock 43 belows on shelf 44 to erect configuration state.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 sealings or water tumbler overflows, leak the water overflow and be collected in aqua storage tank 42 and prevent that water clock is to ground.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410184079.8A CN104163461B (en) | 2014-05-05 | 2014-05-05 | A new type of water treatment purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410184079.8A CN104163461B (en) | 2014-05-05 | 2014-05-05 | A new type of water treatment purifier |
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| Publication Number | Publication Date |
|---|---|
| CN104163461A true CN104163461A (en) | 2014-11-26 |
| CN104163461B CN104163461B (en) | 2015-10-21 |
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| CN201410184079.8A Active CN104163461B (en) | 2014-05-05 | 2014-05-05 | A new type of water treatment purifier |
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Cited By (3)
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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 |
| CN106693418A (en) * | 2016-12-22 | 2017-05-24 | 重庆淼森环保工程有限公司 | Strong brine high dispersion and dehydration equipment |
| CN117643259A (en) * | 2024-01-30 | 2024-03-05 | 云南朗乾农副产品有限公司 | Automatic irrigation equipment of plant |
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| CN102580333A (en) * | 2012-02-15 | 2012-07-18 | 傅利江 | Evaporation system for pressure reduction and film formation through vacuum rotation |
| CN102659194A (en) * | 2012-04-01 | 2012-09-12 | 傅利江 | Distillation-type seawater desalinization device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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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 |
| CN106693418A (en) * | 2016-12-22 | 2017-05-24 | 重庆淼森环保工程有限公司 | Strong brine high dispersion and dehydration equipment |
| 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 |
| CN117643259A (en) * | 2024-01-30 | 2024-03-05 | 云南朗乾农副产品有限公司 | Automatic irrigation equipment of plant |
| 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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| CN104163461B (en) | 2015-10-21 |
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