CN2839249Y - Energy-saving distilled water machine - Google Patents
Energy-saving distilled water machine Download PDFInfo
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- CN2839249Y CN2839249Y CN 200520065537 CN200520065537U CN2839249Y CN 2839249 Y CN2839249 Y CN 2839249Y CN 200520065537 CN200520065537 CN 200520065537 CN 200520065537 U CN200520065537 U CN 200520065537U CN 2839249 Y CN2839249 Y CN 2839249Y
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Abstract
The utility model relates to the technical field of water purification equipment, particularly an energy-saving distilled water machine having the advantages of high heat utilization efficiency and convenient operation. The distilled water machine at least comprises a water supply tank, an evaporation chamber, and a distilled water collecting container which is communicated with the evaporation chamber, wherein a heat energy converter used for heating current entering the evaporation chamber and reducing the temperature of water steam discharged from the evaporation chamber is arranged between the water supply tank and the evaporation chamber. The distilled water machine also comprises a second evaporation chamber which is communicated with a water discharge outlet of the evaporation chamber; a water discharge outlet of the second evaporation chamber is communicated with the distilled water collecting container. The utility model adopts a mode that water is purified by a distillation method and adopts a heat conversion structure; the utility model can convert the heat discharged when the water steam is coagulated into liquid water into the liquid water waiting for evaporation to enable the heat to be circularly utilized and reduce the energy consumption, and meanwhile, the utility model is designed into a secondary evaporation structure to enable the heat utilization efficiency to be increased further and the purification efficiency to be increased. Because the energy consumption is reduced, the purification cost is reduced.
Description
Technical field:
The present invention relates to the water correction plant technical field, refer in particular to a kind of heat utilization efficiency height, energy-saving distilling water machine easy to use.
Background technology:
Be accompanied by constantly advancing of industrial civilization, more and more countries or area are faced with the crisis that water resources lacks.China is as a populous nation, and the situation that water resources lacks is also more and more serious.At present most common be to drink the drummed pure water of buying per capita through purifying, but buy pure water and not only need to spend certain expense, and because employed bucket of drummed pure water and water dispenser are repeated use, so it is difficult to guarantee whether the pure water of being drunk reaches standard for drinking fully.In addition, in some occasion or area, be provided with the direct drinking water pipe that can supply people directly to drink, setting up of these water pipes greatly facilitates people, but we also can see, need spend the great amount of manpower financial resources owing to lay the direct drinking water pipe, be in developing country for one we can't popularize comprehensively.
Another aspect, people never stopped for the research of water purification aspect, and along with the problem of present water resources crisis is more and more outstanding, increasing people adds this research field.Traditional method for purifying water mainly contains two kinds: distillation method and filtration method, be usually used in the refining plant of high throughput by filtering the method for purifying waste water, but the objectionable impurities that this method is difficult to be dissolved in the water is removed.Can obtain purified distilled water and water is carried out purifying treatment for the distillation mode, but there is following deficiency in this mode: at first be that speed is slow, because mostly it is by water is heated, and makes it produce a large amount of water vapors, the current after will condensing then compile.Whole process complexity, treatment capacity is very little; Secondly, energy expenditure is big, because liquid water need absorb a large amount of heat when becoming water vapor, it heats with regard to the outer bound pair of needs for this, but when water recovery becomes the water of liquid state, needs to discharge a large amount of heat again, these heat directly are discharged in the air usually, cause waste in vain.
The applicant is after process studies for a long period of time, and (number of patent application is: 200410051162.4) reach two Chinese invention patent applications of " module that is used for the water purification " (number of patent application is 200410028043.7) once to have proposed to cross " water-purification plant ".It reuses heat by heat exchange method in the process that water is distilled, purifies, and reduces energy expenditure, improves the efficient that water purifies.
Summary of the invention:
Technical problem to be solved by this invention is exactly that present product is further improved, and provides a kind of energy-saving efficiency higher energy-saving distilling water machine.
For solving the problems of the technologies described above, the present invention has adopted following technical scheme: this distillation machine comprises supply tank, evaporator room, the distilled water collection container that is communicated with evaporator room at least, is provided with one between described supply tank and the evaporator room and is used for entering that current in the evaporator room are heated and heat converter to being lowered the temperature by the water vapor of discharging in the evaporator room.
This distillation machine also comprises one second evaporator room, and this second evaporator room is communicated with the water port of evaporator room, and the water port of this second evaporator room is communicated with collection container.
Described second evaporator room comprises chamber, the cambered surface condenser that is arranged at chamber roof that constitutes the second evaporator room main body, the water receptacle that is positioned at the condenser edge, the spraying gun that is communicated with the evaporator room water port and the bubble generator that is positioned at chamber.
The water port of the chamber of described second evaporator room is communicated with supply tank, so that unnecessary water can be discharged in the supply tank.
The pipeline that is communicated with between described supply tank and the evaporator room is provided with water pump, by water pump the water in the supply tank is pumped into evaporator room.
Described collection container is communicated with accumulator through water pump, by water pump the water of collecting in the collection container is pumped in the accumulator, uses for the user.
The present invention adopts is still the mode that distillation method is purified waste water, but has adopted the thermal conversion structure, the heat that it is discharged in the time of water recovery can being become liquid water, and liquid water to be evaporated is given in conversion, makes these heats be able to recycle, reduces the consumption of energy.The present invention simultaneously also designs the double evaporation-cooling structure, and heat utilization efficiency is further promoted, and improves purification efficiency, and owing to reduced the consumption of energy, causes to purify the cost reduction.
Description of drawings:
Fig. 1 is a perspective view of the present invention;
Fig. 2 is a three-dimensional exploded view of the present invention;
Fig. 3 is a fundamental diagram of the present invention.
Embodiment:
The following stated only is specific embodiments of the invention, does not therefore limit protection scope of the present invention.
See Fig. 3, the present invention includes supply tank 1, heat converter 2, evaporator room 3, second evaporator room 4, collection container 5 and accumulator 6.The raw water of packing in the supply tank 1, this water enters evaporator room 3 through the heat tunnel of heat converter 2 and finishes evaporation for the first time.Water vapour after the evaporation enters in the distilled water collection container 5 through the heat release passage of heat converter 2 more for the first time, pumps in the accumulator 6 through water pump 51.The user can directly use the arrangement water in the accumulator 6.
Supply tank 1 generally is positioned at the below of whole distillation machine, and it passes through pipe connection with the heat converter 2 that is positioned at the top.Certainly, for the ease of the water in the supply tank 1 is injected in the heat converter 2, pipeline is provided with water pump 11.
Heat converter 2 adopts the applicant's design in the past, and (see that number of patent application is: 200410051162.4,200410028043.7 two Chinese invention patent application specifications), this heat converter 2 mainly is made of two passages: heat tunnel and heat release passage.Current to be clean are entered the heat tunnel of heat converter 2 by supply tank 1 by water pump 11, enter in the evaporator room 3 through behind the heat tunnel, the bottom of evaporator room 3 chambers is provided with an electricradiator 31, current in entering evaporator room 3 reach a certain height after (is lowest water level to cover electricradiator 31), electricradiator 31 is started working, and water is heated.Water after the heating begins to produce Evaporation Phenomenon, and the water vapour of its generation will be entered the heat release passage of heat converter 2 by steam-pipe 32.A heat exchange membranes at interval only between the heating of heat converter 2, the heat release passage, water vapour in the heat release passage will condense on cryogenic conduit wall, and the heat of its release is delivered to again in the heat tunnel of heat exchange membranes one side timely, and the cold water to be clean that enters in the heat tunnel is carried out preheating.Along with the current of water recovery continuously outflow along the heat release passage, its heat also constantly scatters and disappears, and the water that flow at last in the collection container 5 have dropped to the normal temperature state.Because constantly work in the evaporator room, the heat of its generation also will constantly make the water temperature in the heat tunnel raise.And the water in the passage of heat release is simultaneously also constantly heating the water in the heat tunnel, makes that the water in the heat tunnel can rise to certain altitude very soon.Electricradiator 31 only needs to produce less heat and can keep the lasting pure water that produces of whole module at this moment.So, make these heats be able to recycle, reduce the consumption of energy, not only can improve purification efficiency, and owing to reduced the consumption of energy, thereby the current consumption of electricradiator 31 reduced.
In order further to promote the heat utilization efficiency of product, this distillation machine also comprises one second evaporator room 4, and this second evaporator room 4 is communicated with the water port of evaporator room 3, and the water port of this second evaporator room 4 is communicated with collection container 5.Concrete structure is: this second evaporator room 4 comprises chamber 40, the cambered surface condenser 41 that is arranged at chamber 40 tops, the water receptacle 42 that is positioned at condenser 41 edges, the spraying gun 43 that is communicated with evaporator room 3 water port and the bubble generator 44 that is positioned at chamber 40 that constitutes second evaporator room, 4 main bodys.Second evaporator room 4 is that unnecessary hot water in the evaporator room 3 is collected, and utilizes the heat of these hot water itself that it is carried out double evaporation-cooling, improves vaporization efficiency of the present invention, improves heat utilization efficiency simultaneously.
The principle of work of second evaporator room 4 is: unnecessary hot water will enter in the chamber 40 of second evaporator room 4 by water port and spraying gun 43 in the evaporator room 3, and it is hot water atomized that spraying gun 43 will enter.The effect of atomizing is the steam output that can improve hot water.The bubble that the bubble generator of chamber 40 bottoms produces also is the effect that is used to improve steam output.The water vapour of evaporation condenses into liquid water on condenser 41, and along in the cambered surface inflow water receptacle 42 of himself, and water receptacle 42 is communicated with distilled water collection container 5, so the agglomerative liquid waters will flow in the collection container 5 in the water receptacle 42.
In addition, the chamber 40 of described second evaporator room 4 also is provided with a water port, and this water port is communicated with supply tank 1.This water port can be back to unnecessary water in the chamber 40 in the supply tank 1, to treat to enter the recycle system next time, reduces the waste at water source.
In conjunction with Fig. 1,2, the present invention can be provided with an electronic control box 8 according to present automatic water-drinking machine design in fuselage, push button 7 is set, to control working order of the present invention on fuselage cover.Wherein accumulator 6 just can directly adopt the bucket of present drummed pure water.Described collection container 5 is communicated with accumulator 6 through water pump 51, promptly pumps in the accumulator 6 distilled water that compiles in the collection container 5 for people to use by water pump 51.In order to guarantee safety, the water level that pumps in the accumulator 6 should not expired very much, and an inlet channel 61 can be set in accumulator 6.About 80% the height that the residing height of the water outlet of this inlet channel 61 roughly is positioned at whole accumulator 6 water levels gets final product.In addition, also be provided with a water level detector 62 at inlet channel 61 tops, when the water level in entering accumulator 6 rose to the height of this water level detector 62, water level detector 62 was triggered, and cut off the work of water pump 52 this moment.
In addition, in collection container 5, be provided with water level detector 52 and hygrosensor 53.Water level in collection container 5 reaches the height of water level detector 52, and water level detector 52 is triggered, and electronic control box 8 will cut off the circuit of whole device, break-off of the present invention.Hygrosensor 53 is the temperature that are used to survey by effusive water of condensation in the heat converter 2.Because along with the continuous work of heat converter 2, the temperature in its inner water back and the heat release pipeline all will rise, the last water of condensation of discharging of order can't drop to assigned temperature, even steam does not have condensation directly to discharge.Hygrosensor 53 is triggered in this case, electronic control box 8 produces instruction, make water pump 11 work, water in the supply tank 1 is constantly pumped into the water back of heat converter 2, water port by evaporator room 3 flows to second evaporator room 4, is back in the supply tank 1 at last again, and through circulation after a while, the heat of heat converter 2 water backs will reduce greatly, heat converter 2 is works better again, and water pump 11 stops to continue pump water.
The embodiment of the above, only be the present invention's preferred embodiments, be not to limit the scope of the present invention, so all do variation or modification according to the described shape of the present patent application claim, structure, feature and spiritual principle all should be included in the present patent application claim.
Claims (6)
1, energy-saving distilling water machine, this distillation machine comprises supply tank (1), evaporator room (3), the distilled water collection container (5) that is communicated with evaporator room (3) at least, it is characterized in that: be provided with one between described supply tank (1) and the evaporator room (3) and be used for entering that current in the evaporator room (3) are heated and heat converter (2) to being lowered the temperature by the water vapor of discharging in the evaporator room (3).
2, energy-saving distilling water machine according to claim 1, it is characterized in that: this distillation machine also comprises one second evaporator room (4), this second evaporator room (4) is communicated with the water port of evaporator room (3), and the water port of this second evaporator room (4) is communicated with collection container (5).
3, energy-saving distilling water machine according to claim 2 is characterized in that: described second evaporator room (4) comprises chamber (40), the cambered surface condenser (41) that is arranged at chamber (40) top, the water receptacle (42) that is positioned at condenser (41) edge, the spraying gun (43) that is communicated with evaporator room (3) water port and the bubble generator (44) that is positioned at chamber (40) that constitutes second evaporator room (4) main body.
4, energy-saving distilling water machine according to claim 3 is characterized in that: the water port of the chamber (40) of described second evaporator room (4) is communicated with supply tank (1).
5, energy-saving distilling water machine according to claim 1 is characterized in that: the pipeline that is communicated with between described supply tank (1) and the evaporator room (3) is provided with water pump (11).
6, according to any described energy-saving distilling water machine in the claim 1～5, it is characterized in that: described collection container (5) is communicated with accumulator (6) through water pump (51).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520065537 CN2839249Y (en) | 2005-10-12 | 2005-10-12 | Energy-saving distilled water machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520065537 CN2839249Y (en) | 2005-10-12 | 2005-10-12 | Energy-saving distilled water machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2839249Y true CN2839249Y (en) | 2006-11-22 |
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ID=37427234
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520065537 Expired - Fee Related CN2839249Y (en) | 2005-10-12 | 2005-10-12 | Energy-saving distilled water machine |
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| Country | Link |
|---|---|
| CN (1) | CN2839249Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102232791A (en) * | 2010-04-28 | 2011-11-09 | 上海安立霸电器有限公司 | Distillation type drinking water device |
| CN102344176A (en) * | 2010-07-30 | 2012-02-08 | 上海安立霸电器有限公司 | Distillation type water drinking device and energy-saving heating unit |
| TWI411754B (en) * | 2010-07-15 | 2013-10-11 | Shanghai Ariba Electric Co Ltd | Vaporizer |
| CN110372140A (en) * | 2019-06-17 | 2019-10-25 | 南京颐维环保科技有限公司 | A kind of low-temperature evaporation processing unit |
-
2005
- 2005-10-12 CN CN 200520065537 patent/CN2839249Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102232791A (en) * | 2010-04-28 | 2011-11-09 | 上海安立霸电器有限公司 | Distillation type drinking water device |
| CN102232791B (en) * | 2010-04-28 | 2015-02-18 | 上海安立霸电器有限公司 | Distillation type drinking water device |
| TWI411754B (en) * | 2010-07-15 | 2013-10-11 | Shanghai Ariba Electric Co Ltd | Vaporizer |
| CN102344176A (en) * | 2010-07-30 | 2012-02-08 | 上海安立霸电器有限公司 | Distillation type water drinking device and energy-saving heating unit |
| CN102344176B (en) * | 2010-07-30 | 2013-03-06 | 上海安立霸电器有限公司 | Distillation type water drinking device and energy-saving heating unit |
| CN110372140A (en) * | 2019-06-17 | 2019-10-25 | 南京颐维环保科技有限公司 | A kind of low-temperature evaporation processing unit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061122 Termination date: 20111012 |