CN106082373A - A kind of energy-saving water purification machine - Google Patents
A kind of energy-saving water purification machine Download PDFInfo
- Publication number
- CN106082373A CN106082373A CN201610694555.XA CN201610694555A CN106082373A CN 106082373 A CN106082373 A CN 106082373A CN 201610694555 A CN201610694555 A CN 201610694555A CN 106082373 A CN106082373 A CN 106082373A
- Authority
- CN
- China
- Prior art keywords
- water
- alembic
- hot
- electromagnetic valve
- vacuum pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 171
- 238000000746 purification Methods 0.000 title claims abstract description 14
- 239000008399 tap water Substances 0.000 claims abstract description 16
- 235000020679 tap water Nutrition 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract description 3
- 230000009467 reduction Effects 0.000 abstract description 3
- 230000008676 import Effects 0.000 abstract 1
- 230000001737 promoting effect Effects 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 15
- 230000008020 evaporation Effects 0.000 description 15
- 238000009835 boiling Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 10
- 230000000694 effects Effects 0.000 description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 238000004821 distillation Methods 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000005374 membrane filtration Methods 0.000 description 2
- 238000012946 outsourcing Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000003303 reheating Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011085 pressure filtration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention relates to purifier and manufacture the energy-saving water purification machine of one in field, including alembic, alembic arranges tap water access port and steam (vapor) outlet, arranges 1# electrothermal tube and heat exchanger inside alembic；Left and right sides at alembic, vacuum pump, hot-water cylinder and frozen water tank are set, 2# electrothermal tube is set inside hot-water cylinder, the inlet pipeline of vacuum pump passes through 1# electromagnetic valve, connect the steam (vapor) outlet of alembic, the outlet conduit of vacuum pump connects the inlet pipeline of heat exchanger, and the outlet conduit of heat exchanger upwardly extends along the inwall of alembic, and connects hot-water cylinder；Frozen water tank rear connects the import of vacuum pump by 3# electromagnetic valve；Frozen water tank is arranged above 4# electromagnetic valve, and frozen water tank passes on left 2# electromagnetic valve, and connection is arranged at the vertical pipe of hot-water cylinder inwall；The present invention uses reduction air pressure flashes vapor and water vapour to be cooled to liberated heat recycling during water, it is thus achieved that the electric energy of 1 kilogram of pure water needs is only 0.1 degree of electricity, energy-conserving and environment-protective, possesses promotional value.
Description
Technical field
The present invention relates to field of manufacture of water treatment equipment, specifically refer to use natural evaporation principle and the one developed is energy-conservation
Type water purification machine.
Background technology
Earth water pollutes the pollutant mainly produced by mankind's activity to be caused, including industrial pollution source, agricultural pollution source
With domestic pollution source three parts.Water pollutes and the living safety of the mankind is constituted significant threat, becomes human health and society
The major obstacles of development.
Domestic and international most of waterworks the most still uses the outmoded process of precipitation, filtration, chlorination, by rivers
Water or subsoil water are simply processed into drinkable water.In the face of substantial amounts of industrial or agricultural polluter pours in life water source, the kind of pollutant
More and more, waterworks is unable all removes all contaminants.Add tap water from water factory through water transfer pipe network and high level
Storage tank arrives the secondary pollution that drinking water terminal is brought, and the tap water arriving user has not met water hygiene
Standard.
The most ancient acquisition pure water processes is to use heating distillating method, steam obtain pure water after cooling down, and some is to pure
The laboratory that water purity requirement is high, the most still adopts in this way, and its energy consumption is high, does not possess practicality in addition to laboratory
It is worth.
Traditional water purification machine is to obtain pure water, owing to film is easily clogged, not easy care, replacement cost by the method for membrane filtration
In height, and membrane filtration processes, needing bigger pressure, the energy consumption of pressure filtration is the highest.Therefore citizen typically adopt outsourcing bucket
The method of dress pure water solves the demand of drinking water, but outsourcing drummed pure water is relatively costly, and the price of every 1 kg of water exceedes
1 yuan, and drummed pure water is difficult to manage due to supply and distribution channel, usually occurs that antibacterial exceeds standard and defective, more has illegal
Businessman uses undressed tap water, and personation pure water is sold, and seriously compromises civic healthy.
Summary of the invention
In order to solve the problem that above-mentioned prior art exists, the present invention provides a kind of energy-saving water purification machine.
The technical scheme that the present invention uses is as follows:
A kind of energy-saving water purification machine, including alembic, in the above and behind of alembic, is respectively provided with tap water access port and steaming
Vapor outlet, at alembic lower inside, arranges 1# electrothermal tube, above the internal 1# electrothermal tube of described alembic, arranges heat exchanger；
At the left and right sides of alembic, being respectively provided with vacuum pump and hot-water cylinder, the lower inside of hot-water cylinder arranges 2# electrothermal tube, hot-water cylinder
It is arranged over air vent；The inlet pipeline of described vacuum pump, by 1# electromagnetic valve, connects the steam (vapor) outlet at alembic rear, very
Empty delivery side of pump pipeline, connects the inlet pipeline of heat exchanger, and the outlet conduit of heat exchanger upwardly extends along the inwall of alembic,
Connection hot-water cylinder.
As improving and optimizating further, on the right side of described hot-water cylinder, being additionally provided with frozen water tank, frozen water tank rear arranges steam
Outlet, and by 3# electromagnetic valve, connect the inlet pipeline of vacuum pump；Frozen water tank is provided above air vent, and is provided with 4# electromagnetism
Valve；Frozen water tank passes on left 2# electromagnetic valve, and connection is arranged at the vertical pipe of hot-water cylinder inwall.
The Research idea of the present invention and beneficial effect:
1, at ambient pressure, water needs to reach 100 DEG C, could seethe with excitement, and is converted into steam in a large number.Reduce air pressure, such as low on plateau
Air pressure area, water just can seethe with excitement at about 80 DEG C and be converted into steam.So, in airtight container, artificial reduction water surface gas
Pressure, the boiling temperature of water can be reduced to 50 DEG C, even lower, is pressurizeed in exit by vacuum pump, makes under low pressure
The water vapour evaporated is condensed into the water of liquid at ambient pressure, and discharges substantial amounts of heat in condensation process, and these heats
Further through heat exchanger transmission back to the water in alembic, maintain the continuous evaporation that continues of the water in alembic.Produce hence with this technology
Pure water, only needs to carry water to certain temperature in equipment initial start stage, and midway only need to supplement a small amount of energy, i.e. can maintain
Continuous evaporation, continuously output pure water, i.e. need less heat just can obtain pure water；
2, we need pure water, are not water vapour, it is common practice to water vapour is cooled to water, then drinks, thus waste
Substantial amounts of heat.Using heat exchanger, the heat these slatterned is used for reheating tap water, produces more steaminess, energy-conservation
Efficiently, achieve many things at one stroke；
3, the electric energy that the present invention is consumed just corresponds to the water energy that (45-100 DEG C) is consumed when room temperature is heated to boiling,
Remaining institute's calorific requirement, is provided by heat exchanger, calculates according to reality, it is thus achieved that the electric energy required for 1 kilogram of pure water is only 0.1 degree
Electricity；
4, the effect using vacuum pump is to make in alembic and produce pressure reduction between air, thus obtains low-temperature evaporation and normal pressure is cold
Solidifying effect.Another effect of vacuum pump is to reduce alembic water surface air pressure and drain water vapour, improves evaporation efficiency, and
Frozen water is manufactured in frozen water tank；
5 if it is desired to obtain mineral water, it is only necessary in hot water outlet or frozen water exit, and connecting mineralized material can be (such as wheat meal
The useful mineralizer such as stone), even if pure water flows through the pipeline of built-in mineralized material, aquiform stool out contains mineral, becomes ore deposit
Spring water, it is true that the upper substantial amounts of mineral water factory of society produces mineral water, also uses such principle to manufacture.I.e. first
Mineralising after purification, first removes the impurity in water, remineralization；
6, it is by distillation due to the pure water of the present invention, effectively removes the harmful heavy metal ions that can not evaporate in water
With oxious components such as silt rust.So, all common than the great majority on the market mineral springs of the pure water of present invention production and mineral water
The non-distillage of water factory, superior in quality much cost is the highest, possesses application value, benefits masses.
Accompanying drawing explanation
Fig. 1 is a kind of energy-saving water purification machine schematic perspective view of the present invention.
Fig. 2 is a kind of energy-saving water purification machine internal structure schematic perspective view of the present invention.
Fig. 3 is Fig. 1 schematic rear view.
Fig. 4 is the relation table of height above sea level and atmospheric pressure.
Fig. 5 is the relation table of atmospheric pressure and evaporation of water temperature.
In figure, 1-vacuum pump, 2-alembic, 3-1# electromagnetic valve, 4-tap water access port, 5-air vent, 6-2#
Electromagnetic valve, 7-3# electromagnetic valve, 8-4# electromagnetic valve, 9-frozen water exports, 10-frozen water tank, 11-hot water outlet, 12-hot water
Tank, 13-outlet of sewer, 14-heat exchanger, 15-1# electrothermal tube, 16-2# electrothermal tube.
Detailed description of the invention
Fig. 1 and Fig. 2 is a kind of energy-saving water purification machine schematic perspective view of the present invention.In the above and behind of alembic, respectively
Tap water access port and steam (vapor) outlet are set, 1# electrothermal tube is set in inside, above 1# electrothermal tube, heat exchanger is set；Steaming
Evaporate the left and right sides of tank, be respectively provided with vacuum pump and hot-water cylinder, 2# electrothermal tube is set inside hot-water cylinder, is arranged over air vent.Very
The inlet pipeline of empty pump, by 1# electromagnetic valve, connects the steam (vapor) outlet at alembic rear, the outlet conduit of vacuum pump, connects heat exchange
The inlet pipeline of device, the outlet conduit connection hot-water cylinder of heat exchanger.On the right side of hot-water cylinder, it is provided with frozen water tank, frozen water tank rear
Steam (vapor) outlet is set, and is connected the inlet pipeline of vacuum pump by 3# electromagnetic valve；Frozen water tank is provided above air vent, and is provided with
4# electromagnetic valve；Frozen water tank passes on left 2# electromagnetic valve, and connection is arranged at the vertical pipe of hot-water cylinder inwall.
Work process of the present invention:
1, tap water is after tap water access port 4 enters alembic 2, closes access port 4, when in alembic, water temperature is less than 80 DEG C
Time, 1# electrothermal tube 15 starts heating, and when water temperature is higher than 95 DEG C, 1# adds heat pipe and stops heating；
2, after in alembic, water temperature is more than 80 DEG C, vacuum pump 1 starts, and 1# electromagnetic valve 3 is opened, and 2# electromagnetic valve 6 closes, due to vacuum
Effect, water seethes with excitement under conditions of less than 100 DEG C, and water vapour, after vacuum pump pressurizes, condenses in heat exchanger 14, becomes distillation
Water sends into hot-water cylinder storage, and the heat that heat exchanger obtains during condensed steam, for heating the tap water in alembic, is tieed up
Hold the tap water in alembic and continue evaporation, make present invention output pure water continuously；
3, the present invention only needs to be heated by 1# electric heater in initial start stage, and temperature liter is condensed obtained heat by steam after getting up
Heat, and heat without power consumption；Because vacuum pump pressurized water steam also can produce heat, these heats counteract water purification machine to
Outer radiator portion；
4, when the water yield in alembic is less than set amount, quitting work, discharge remaining sewage, sewage quantity accounts for total amount of water
10-20%, add new tap water, work on；
5, one electric heating tube 16 is set in hot-water cylinder, when water temperature is down to setting value lower limit, automatically starts, when water temperature rises to set
During the definite value upper limit, being automatically stopped, maintain the temperature of hot water, water temperature setting value can be set as 50-95 DEG C；
When 6, needing frozen water, open vacuum pump, simultaneously close off 1# electromagnetic valve and 4# electromagnetic valve, open 2# electromagnetic valve and 3# electromagnetism
Valve, the water in hot-water cylinder can be drawn into frozen water tank 10, after the water in frozen water tank reaches the water yield set, closes 2# electromagnetic valve,
Under vacuum action, the water in frozen water tank seethes with excitement under extremely low temperature, due to evaporation endothermic, and does not has thermal source in frozen water tank, the most whole
Water temperature in individual frozen water tank can persistently reduce, until it reaches the temperature of setting, can be to 0 DEG C.
Fig. 4 is the relation table of height above sea level and atmospheric pressure.In table visible, along with height above sea level raise, relatively large air pressure
Power declines, and relative air density reduces, absolute humidity (g/m3) and the boiling point (DEG C) of water also decline.
Fig. 5 is the relation table of atmospheric pressure and evaporation of water temperature.In table visible, when air is in an atmospheric pressure, phase
When in 0.1MPa, the boiling point of water is 99.63 DEG C, and the enthalpy of water vapour is 2675.7kJ/kg, and the water of i.e. 1 kilogram 99.63 DEG C steams
Vapour contains the heat of 2675.7 kilojoules.
If the atmospheric pressure on the water surface is reduced to 1/10th of conventional air pressure, i.e. during 0.01 MPa, the boiling point of water is
45.83 DEG C, the enthalpy of water vapour is 2584.4kJ/kg, and the water vapour of i.e. 1 kilogram 45.83 DEG C contains the heat of 2584.4 kilojoules.Instead
For crossing, when atmospheric pressure is 0.01 MPa, the boiling point of water is 45.83 DEG C, evaporates 1 kg of water and needs the heat of 2584.4 kilojoules
Amount.
It can also be seen that the boiling point of water can be from atmospheric pressure from Fig. 5 atmospheric pressure relation table with evaporation of water temperature
Being 6.982 DEG C during 0.001 MPa, until atmospheric pressure is 221.78 DEG C during 2.40MPa, span is very big, but, water vapour
The change of enthalpy is only 2513.8 kJ/kg to 2800.4 kJ/kg, and change is only tens percent, therefore, even if reducing on the water surface
Atmospheric pressure, can reduce the boiling point of water, accelerate evaporation rate, but the heat needed for evaporation, the amplitude of minimizing is little, i.e.
Energy-saving effect is little.If recycle-water steam is not cooled to liberated heat during water, the then present invention and introduction in background technology
Ancient heating distillating method produces pure water, and required energy consumption reduces few, do not reaches obvious energy-saving effect, simply improves
Evaporation of water efficiency.
Here it is the present invention needs to use heat exchanger to reclaim the true cause place of water vapour liberated heat.
Atmospheric pressure on the water surface in alembic can be reduced to 0.01-0.02MPa from 0.1MPa by the present invention, the boiling of water
Point is reduced to 45-60 DEG C, and is drained by water vapour in time, thus accelerates evaporation of water speed, uses heat exchanger simultaneously, returns
The heat receiving water vapour is used for reheating tap water, reaches energy-efficient purpose.
The electric energy that the present invention is consumed just corresponds to the water energy that (45-100 DEG C) is consumed when room temperature is heated to boiling
Amount, it is thus achieved that the process of distilled water does not the most consume extra electric energy, and therefore it is the most energy-conservation, it is thus achieved that needed for 1 kilogram of distilled water
The electric energy wanted is only 0.1 degree of electricity, and cost is less than 0.1 yuan.
Present configuration is simple, cheap, according to measuring and calculating, small-sized household type cost only about 1500 yuan, no material consumption, it is easy to
Safeguard, be unit and the ideal device of family's acquisition pure water.
The core of the present invention is that the heat using steam to condense institute's output continues to make tap water evaporation give birth to continuously
Produce distillation pure water.
Claims (2)
1. an energy-saving water purification machine, including alembic, in the above and behind of alembic, be respectively provided with tap water access port and
Steam (vapor) outlet, at alembic lower inside, arranges 1# electrothermal tube, it is characterised in that: on the internal 1# electrothermal tube of described alembic
Side, arranges heat exchanger；At the left and right sides of alembic, being respectively provided with vacuum pump and hot-water cylinder, the lower inside of hot-water cylinder arranges 2#
Electrothermal tube, hot-water cylinder be arranged over air vent；The inlet pipeline of described vacuum pump, by 1# electromagnetic valve, after connecting alembic
The steam (vapor) outlet of side, the outlet conduit of vacuum pump, connect the inlet pipeline of heat exchanger, the outlet conduit of heat exchanger is along alembic
Inwall upwardly extend, connect hot-water cylinder.
The energy-saving water purification machine of one the most according to claim 1, it is characterised in that: on the right side of described hot-water cylinder, also set
There are frozen water tank, frozen water tank rear that steam (vapor) outlet is set, and by 3# electromagnetic valve, connect the inlet pipeline of vacuum pump；On frozen water tank
Side arranges air vent, and is provided with 4# electromagnetic valve；Frozen water tank passes on left 2# electromagnetic valve, and connection is arranged at hanging down of hot-water cylinder inwall
Straight pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610694555.XA CN106082373A (en) | 2016-08-22 | 2016-08-22 | A kind of energy-saving water purification machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610694555.XA CN106082373A (en) | 2016-08-22 | 2016-08-22 | A kind of energy-saving water purification machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106082373A true CN106082373A (en) | 2016-11-09 |
Family
ID=58070247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610694555.XA Pending CN106082373A (en) | 2016-08-22 | 2016-08-22 | A kind of energy-saving water purification machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106082373A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018233547A1 (en) * | 2017-06-18 | 2018-12-27 | 易汉平 | Pure water preparation method and device |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4525243A (en) * | 1984-03-05 | 1985-06-25 | J. Stanley Miller Corporation | Apparatus for desalinating water |
| US4696718A (en) * | 1986-02-04 | 1987-09-29 | Lasater Henry C | Water purification device |
| CN102219270A (en) * | 2011-04-21 | 2011-10-19 | 唐福辉 | Multifunctional water distilling machine |
| CN102374698A (en) * | 2011-11-29 | 2012-03-14 | 林绍风 | Refrigerating system being opening-type refrigerating and heating device |
| CN103435116A (en) * | 2013-09-10 | 2013-12-11 | 苏州新区枫桥净化设备厂 | Evaporation and purification device |
| CN105540707A (en) * | 2015-03-25 | 2016-05-04 | 胡胜录 | Evaporation system for vacuum production of salt and purified water |
| CN205933290U (en) * | 2016-08-22 | 2017-02-08 | 王骏 | Energy -saving water purification machine |
-
2016
- 2016-08-22 CN CN201610694555.XA patent/CN106082373A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4525243A (en) * | 1984-03-05 | 1985-06-25 | J. Stanley Miller Corporation | Apparatus for desalinating water |
| US4696718A (en) * | 1986-02-04 | 1987-09-29 | Lasater Henry C | Water purification device |
| CN102219270A (en) * | 2011-04-21 | 2011-10-19 | 唐福辉 | Multifunctional water distilling machine |
| CN102374698A (en) * | 2011-11-29 | 2012-03-14 | 林绍风 | Refrigerating system being opening-type refrigerating and heating device |
| CN103435116A (en) * | 2013-09-10 | 2013-12-11 | 苏州新区枫桥净化设备厂 | Evaporation and purification device |
| CN105540707A (en) * | 2015-03-25 | 2016-05-04 | 胡胜录 | Evaporation system for vacuum production of salt and purified water |
| CN205933290U (en) * | 2016-08-22 | 2017-02-08 | 王骏 | Energy -saving water purification machine |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2018233547A1 (en) * | 2017-06-18 | 2018-12-27 | 易汉平 | Pure water preparation method and device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203662555U (en) | Waste water recovery energy-saving type cold-hot direct-drinking water dispenser | |
| CN104591327B (en) | Loop heat pipe formula cylinder type solar energy sea water desalination apparatus | |
| CN211595081U (en) | Sea water desalting device by liquid gravity distillation method | |
| CN205222728U (en) | Purifier and water purification machine of water purification machine | |
| CN104929190A (en) | Equipment for producing water through air | |
| CN105329962B (en) | Solar energy composite heat pump desalinization and confession domestic water system and method | |
| CN202457890U (en) | Non-container direct-heating nanometer electrothermal film heating unit water dispenser | |
| CN106082373A (en) | A kind of energy-saving water purification machine | |
| CN205933290U (en) | Energy -saving water purification machine | |
| CN205481836U (en) | Solar boiler | |
| CN201842667U (en) | Drinking water treatment equipment | |
| CN205873941U (en) | Wave power oscillating type solar -powered seawater desalination device | |
| CN203269609U (en) | Solar seawater desalination device | |
| CN202671242U (en) | Preheating energy-saving distillation apparatus | |
| CN205671939U (en) | The water of split type on-line cleaning adjusts valve water to adjust machine and hot water machine | |
| CN205367777U (en) | Sea water desalting device | |
| CN204301301U (en) | Heat pump direct-heating-type boiler | |
| CN202297191U (en) | Natural condensation type solar pure water production and water heating device | |
| CN203949354U (en) | Water boiler | |
| CN207501741U (en) | A kind of domestic hot-water recycles filter device | |
| CN206502626U (en) | A kind of pure water evaporation apparatus | |
| CN105174340B (en) | A kind of solar energy kettle steams formula sea water desalinating unit | |
| CN213454260U (en) | Hot pot type warm boiled water heating device | |
| CN201203245Y (en) | Heating system and drinking equipment using the same | |
| CN205014319U (en) | Steam condensate water heat recovery system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20210115 Address after: 311215 No. 117 Hongxing Road, Qiaonan Block, Xiaoshan Economic and Technological Development Zone, Xiaoshan District, Hangzhou City, Zhejiang Province Applicant after: HANGZHOU ANYONG ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: Zhiqiao company, No.40, cuixing Road, Duanzhou District, Zhaoqing City, Guangdong Province 526020 Applicant before: Wang Jun |
|
| TA01 | Transfer of patent application right | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161109 |
|
| WD01 | Invention patent application deemed withdrawn after publication |