CN106348515B - A kind of drinking device - Google Patents
A kind of drinking device Download PDFInfo
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- CN106348515B CN106348515B CN201611001448.0A CN201611001448A CN106348515B CN 106348515 B CN106348515 B CN 106348515B CN 201611001448 A CN201611001448 A CN 201611001448A CN 106348515 B CN106348515 B CN 106348515B
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- 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)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The present invention relates to a kind of drinking devices, by the setting to specific structure, can export boiled water, warm water and directly drink cold water.Pass through the setting of internal specific structure, so that temperature is transferred to part cold water in insulating process by hot water, it directly drinks to allow part cold water and part boiled water all to merge into warm water by heat exchange, is not exporting the occurrence of causing heat transmission to be lost in vain to air so as to cause heat in the time of boiled water so as to avoid drinking device.By improving to wherein purification system, so that clean-up effect is more obvious, the water after purifying can directly be drunk.
Description
Technical field
The invention belongs to purifier fields, and in particular to a kind of drinking device.
Background technique
With the raising of people's lives water product, the requirement for water quality etc. is gradually increased.Necessary not only for pure in life
Water purification needs the water of different temperatures also according to different demands, such as makes tea and need boiled water, and directly drinks and need warm water, steeps milk
Powder converts the warm water that fruit juice then needs temperature slightly higher, and summer day heat needs directly to drink cold water, how requirements numerous in this way accords with
Conjunction then needs the diversion equipment that can generate different temperatures, but existing diversion equipment often will appear multiple boiled repetition
The warm water that boiled boiled water and water is converted out needs to invent a kind of natural cooling or the temperature that heats naturally and does not repeat boiled
Boiled water and the drinking device of A grades of water quality can be provided simultaneously.
Summary of the invention
The present invention is by proposing a kind of drinking device.
It is realized especially by following technological means:
A kind of drinking device, including drinking-water component, heating element, heat-exchanging part and purification device.
The drinking-water component is including turning on the tap, high temperature temperature tap, low temperature warm water are leading, cold water faucet and boiled water store
Tank is detected, the first outlet for storing detection tank with the boiled water of turning on the tap is connected, and boiled water storage detects the of tank
Two outlets are connected with the heat-exchanging part, and the entrance of the boiled water storage detection tank is connected with the heating element；Boiled water storage
It deposits detection tank and is internally provided with temperature detection part, when threshold value of the temperature lower than setting, the valve of second outlet is opened, by institute
The water stated in boiled water storage detection tank is flowed into the heat-exchanging part.
There are three outlet, first outlet is connected with the heating element for the purification device setting, and second outlet and heat are handed over
It changes component to be connected, third outlet is connected with the cold water faucet.
The heating element is flowed into after boiling for heating the water that the purification device first outlet flows into
In the boiled water storage detection tank.
The heat-exchanging part includes the snake pipe of shell and interior of shell setting, and the heat-exchanging part is provided with two
A entrance and two outlets, first entrance is connected with the second outlet that the boiled water stores detection tank, and the boiled water is stored
The hot water of the second outlet outflow of detection tank is input in the snake pipe, and the snake pipe is connected with first outlet, institute
It states first outlet to be connected with the high temperature temperature tap, second entrance is connected with the second outlet of the purification device, and by institute
The purified water for stating the second outlet outflow of purification device is input in shell and carries out hot friendship with the hot water in the snake pipe
It changes, the water after heat exchange is connected by second outlet with the low temperature warm water faucet.
The purification device successively includes PP cotton processing component, the first active carbon processing component, Amorphous Alloy Grain processing
Component, reverse osmosis membrane component, wastewater discharge device and the second active carbon processing component.
Preferably, the PP cotton processing component includes positioned at the entrance of downside, multiple concatenated PP cotton filter elements and the
One outlet and second outlet, the entrance and water supply pipe and are pressurized water inlet line and connect, and the pressurized metal pipeline will be from
The water of the second outlet outflow of PP cotton processing component is passed through the entrance of PP cotton processing component again after pressurization, by threeway and
The opening and closing of low tension switch control pressurization water inlet line and water supply pipe, the multiple concatenated PP cotton filter element with snakelike arrangement,
It is provided with sewage flow pipeline outside filter core, is provided on sewage flow pipeline and deposits dirty chamber, the first outlet is set to PP
The top of cotton processing component.
The first outlet of the PP cotton processing component is entered by inlet water solenoid valve and the first active carbon processing component
Mouth connection.
The first active carbon processing component includes shell, entrance, active carbon treatment trough and outlet, the entrance and exit
It being arranged on shell, the active carbon treatment trough includes exocoel and inside groove, and the exocoel is fixed at the enclosure interior,
The exocoel is top end opening, and the cylindrical of bottom end closure is arranged, and the entrance is connect with the top of exocoel side, the outlet
It is connect with the bottom end of exocoel, inside groove setting is arranged for porous structure, is provided with active carbon in inside groove described outer intracavitary
Grain.
The Amorphous Alloy Grain processing component includes shell, entrance, amorphous particle processing board and outlet, the amorphous
Grain processing board be it is multiple, be vertically arranged inside the housing, be porous stainless steel plate outside the amorphous particle processing board, it is internal
It is provided with amorphous particle, the amorphous particle is Fe by atomic ratio69Ni12Sm0.2Tb0.8C3B6La3P6, 5 ~ 8mm of average grain diameter；
The outlet is connected with the entrance of the reverse osmosis membrane component.
The reverse osmosis membrane component includes shell, reverse osmosis membrane frame and reverse osmosis membrane, and the reverse osmosis membrane is arranged in institute
It states on reverse osmosis membrane frame, the reverse osmosis membrane successively includes water process non-woven fabrics base support layer, polysulfones is high-molecular porous holds
Hold in the palm layer, the ultra-thin dense separation layers of aromatic polyamides and graphite oxide ene coatings；The graphene oxide coating spraying is described
On the ultra-thin dense separation layers of aromatic polyamides；Two outlets, one outlet and the waste water is arranged in the reverse osmosis membrane component
Tapping equipment connection, another is connected by the high-voltage switch gear with the entrance of the second active carbon processing component.
The wastewater discharge device is for discharging the waste water that the reverse osmosis membrane component is discharged.
The second active carbon processing component includes the second active carbon treatment trough, setting in the second active carbon treatment trough
Active charcoal mixed processing agent particle, the component of the active carbon mixed processing agent particle is according to the mass fraction are as follows: active carbon: 11
~ 15 parts, starch: 11 ~ 12 parts, Sodium Polyacrylate: 1 ~ 3 part, sodium chloride: 1 ~ 2 part, phytone: 1 ~ 2 part, the active carbon
The average grain diameter of mixed processing agent particle is 0.6 ~ 1.0cm.
Preferably, the PP cotton filter element be 6, pore size filter be followed successively by 1.2 ~ 1.5 μm, 1.1 ~ 1.3 μm, 1.0 ~
1.2 μm, 0.9 ~ 1.1 μm, 0.8 ~ 1.0 μm and 0.9 ~ 1.1 μm.
Preferably, the active carbon mixed processing agent particle is porous particle.
Preferably, the average grain diameter of the amorphous particle is 6 ~ 8mm, further preferred 6.6mm.
Preferably, the high-molecular porous supporting layer of polysulfones with a thickness of 80 ~ 180nm, the aromatic polyamides are ultra-thin
The material of dense separation layers be equal benzene trimethamide, the graphite oxide ene coatings with a thickness of 50 ~ 130nm.
Preferably, the aperture of the high-molecular porous supporting layer of polysulfones is 0.0001 ~ 0.0002 μm.
Preferably, the threshold value of temperature detection part is set as 92 ~ 95 DEG C in the boiled water storage detection tank.
Effect of the invention is that:
1, detection tank is stored by setting boiled water, so that boiled water is kept the temperature wherein, it can if temperature is lower than threshold value
It is transmitted in heat-exchanger rig and exchanges heat with cold water, thus water here can both be carried out cooling down to realize that warm water exports,
Cold water can be heated again, realize the warm water output of another temperature, and water (hot water cold water mix can also be avoided
Formed warm water) situation appearance.And boiled water is stored in boiled water storage detection tank, water is avoided to repeat in heating device always
The boiled injury for leading to thousand boiling water for human body.
2, it is specifically improved by the layer structure to reverse osmosis membrane, so that osmosis filtration effect obtains significantly
Improve, reverse osmosis wastewater flow rate reaches minimum, to more adapt to the application of house or building for the purifier.
3, be configured by the specific component to purifier, the active carbon set-up mode that especially wherein mixes and
The specific setting of Amorphous Alloy Grain processing component, so that water purification efficiency is improved, integral arrangement mode guaranteeing only
In the case where water efficiency, overall volume is reduced, so that the occupied area of whole drinking device is guaranteed.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of drinking device of the present invention.
Fig. 2 is the structural schematic diagram of purification device in drinking device of the present invention.
Wherein: 11- turns on the tap, 12- high temperature temperature tap, 13- low temperature warm water faucet, 14- cold water faucet, 15- boiled water
Storage detection tank, 2- heating element, 3- purification device, 31-PP cotton processing component, 32- inlet water solenoid valve, the first active carbon of 33-
Processing component, 34- Amorphous Alloy Grain processing component, 35- booster pump, 36- reverse osmosis membrane component, 37- wastewater discharge device,
38- high-voltage switch gear, 39- the second active carbon processing component, 310- threeway, 311- are pressurized water inlet line, 312- water supply pipe, 4-
Heat-exchanging part.
Specific embodiment
Embodiment 1
A kind of drinking device, including drinking-water component, heating element, heat-exchanging part and purification device.
The drinking-water component is including turning on the tap, high temperature temperature tap, low temperature warm water are leading, cold water faucet and boiled water store
Tank is detected, the first outlet for storing detection tank with the boiled water of turning on the tap is connected, and boiled water storage detects the of tank
Two outlets are connected with the heat-exchanging part, and the entrance of the boiled water storage detection tank is connected with the heating element；Boiled water storage
It deposits detection tank and is internally provided with temperature detection part, when threshold value of the temperature lower than setting, the valve of second outlet is opened, by institute
The water stated in boiled water storage detection tank is flowed into the heat-exchanging part.
There are three outlet, first outlet is connected with the heating element for the purification device setting, and second outlet and heat are handed over
It changes component to be connected, third outlet is connected with the cold water faucet.
The heating element is flowed into after boiling for heating the water that the purification device first outlet flows into
In the boiled water storage detection tank.
The heat-exchanging part includes the snake pipe of shell and interior of shell setting, and the heat-exchanging part is provided with two
A entrance and two outlets, first entrance is connected with the second outlet that the boiled water stores detection tank, and the boiled water is stored
The hot water of the second outlet outflow of detection tank is input in the snake pipe, and the snake pipe is connected with first outlet, institute
It states first outlet to be connected with the high temperature temperature tap, second entrance is connected with the second outlet of the purification device, and by institute
The purified water for stating the second outlet outflow of purification device is input in shell and carries out hot friendship with the hot water in the snake pipe
It changes, the water after heat exchange is connected by second outlet with the low temperature warm water faucet.
The purification device successively includes PP cotton processing component, the first active carbon processing component, Amorphous Alloy Grain processing
Component, reverse osmosis membrane component, wastewater discharge device and the second active carbon processing component.
The PP cotton processing component includes entrance, multiple concatenated PP cotton filter elements and the first outlet and the positioned at downside
Two outlets, the entrance are connect with water supply pipe and pressurization water inlet line, and the pressurized metal pipeline will be from PP cotton processing unit
The water of the second outlet outflow of part is passed through the entrance of PP cotton processing component again after pressurization, passes through threeway and low tension switch control
The opening and closing of system pressurization water inlet line and water supply pipe, the multiple concatenated PP cotton filter element is with snakelike arrangement, outside filter core
It is provided with sewage flow pipeline, is provided on sewage flow pipeline and deposits dirty chamber, the first outlet is set to PP cotton processing component
Top.
The first outlet of the PP cotton processing component is entered by inlet water solenoid valve and the first active carbon processing component
Mouth connection.
The first active carbon processing component includes shell, entrance, active carbon treatment trough and outlet, the entrance and exit
It being arranged on shell, the active carbon treatment trough includes exocoel and inside groove, and the exocoel is fixed at the enclosure interior,
The exocoel is top end opening, and the cylindrical of bottom end closure is arranged, and the entrance is connect with the top of exocoel side, the outlet
It is connect with the bottom end of exocoel, inside groove setting is arranged for porous structure, is provided with active carbon in inside groove described outer intracavitary
Grain.
The Amorphous Alloy Grain processing component includes shell, entrance, amorphous particle processing board and outlet, the amorphous
Grain processing board be it is multiple, be vertically arranged inside the housing, be porous stainless steel plate outside the amorphous particle processing board, it is internal
It is provided with amorphous particle, the amorphous particle is Fe by atomic ratio69Ni12Sm0.2Tb0.8C3B6La3P6, average grain diameter 6mm；Institute
Outlet is stated to be connected with the entrance of the reverse osmosis membrane component.
The reverse osmosis membrane component includes shell, reverse osmosis membrane frame and reverse osmosis membrane, and the reverse osmosis membrane is arranged in institute
It states on reverse osmosis membrane frame, the reverse osmosis membrane successively includes water process non-woven fabrics base support layer, polysulfones is high-molecular porous holds
Hold in the palm layer, the ultra-thin dense separation layers of aromatic polyamides and graphite oxide ene coatings；The graphene oxide coating spraying is described
On the ultra-thin dense separation layers of aromatic polyamides；Two outlets, one outlet and the waste water is arranged in the reverse osmosis membrane component
Tapping equipment connection, another is connected by the high-voltage switch gear with the entrance of the second active carbon processing component.
The wastewater discharge device is for discharging the waste water that the reverse osmosis membrane component is discharged.
The second active carbon processing component includes the second active carbon treatment trough, setting in the second active carbon treatment trough
Active charcoal mixed processing agent particle, the component of the active carbon mixed processing agent particle is according to the mass fraction are as follows: active carbon: 12
Part, starch: 11.2 parts, Sodium Polyacrylate: 1.3 parts, sodium chloride: 1.2 parts, phytone: 1.2 parts, the active carbon mixing
The average grain diameter of inorganic agent particle is 0.9cm.
The PP cotton filter element be 6, pore size filter be followed successively by 1.3 μm, 1.15 μm, 1.02 μm, 0.98 μm, 0.9 μm with
And 1.01 μm.
The active carbon mixed processing agent particle is porous particle.
The average grain diameter of the amorphous particle is 6.8mm.
The high-molecular porous supporting layer of polysulfones with a thickness of 102nm, the ultra-thin dense separation layers of aromatic polyamides
Material be equal benzene trimethamide, the graphite oxide ene coatings with a thickness of 90nm.
The aperture of the high-molecular porous supporting layer of polysulfones is 0.00012 μm.
The threshold value of temperature detection part is set as 93 DEG C in the boiled water storage detection tank.
Embodiment 2
A kind of drinking device, including drinking-water component, heating element, heat-exchanging part and purification device.
The drinking-water component is including turning on the tap, high temperature temperature tap, low temperature warm water are leading, cold water faucet and boiled water store
Tank is detected, the first outlet for storing detection tank with the boiled water of turning on the tap is connected, and boiled water storage detects the of tank
Two outlets are connected with the heat-exchanging part, and the entrance of the boiled water storage detection tank is connected with the heating element；Boiled water storage
It deposits detection tank and is internally provided with temperature detection part, when threshold value of the temperature lower than setting, the valve of second outlet is opened, by institute
The water stated in boiled water storage detection tank is flowed into the heat-exchanging part.
There are three outlet, first outlet is connected with the heating element for the purification device setting, and second outlet and heat are handed over
It changes component to be connected, third outlet is connected with the cold water faucet.
The heating element is flowed into after boiling for heating the water that the purification device first outlet flows into
In the boiled water storage detection tank.
The heat-exchanging part includes the snake pipe of shell and interior of shell setting, and the heat-exchanging part is provided with two
A entrance and two outlets, first entrance is connected with the second outlet that the boiled water stores detection tank, and the boiled water is stored
The hot water of the second outlet outflow of detection tank is input in the snake pipe, and the snake pipe is connected with first outlet, institute
It states first outlet to be connected with the high temperature temperature tap, second entrance is connected with the second outlet of the purification device, and by institute
The purified water for stating the second outlet outflow of purification device is input in shell and carries out hot friendship with the hot water in the snake pipe
It changes, the water after heat exchange is connected by second outlet with the low temperature warm water faucet.
The purification device successively includes PP cotton processing component, the first active carbon processing component, Amorphous Alloy Grain processing
Component, reverse osmosis membrane component, wastewater discharge device and the second active carbon processing component.
Preferably, the PP cotton processing component includes positioned at the entrance of downside, multiple concatenated PP cotton filter elements and the
One outlet and second outlet, the entrance and water supply pipe and are pressurized water inlet line and connect, and the pressurized metal pipeline will be from
The water of the second outlet outflow of PP cotton processing component is passed through the entrance of PP cotton processing component again after pressurization, by threeway and
The opening and closing of low tension switch control pressurization water inlet line and water supply pipe, the multiple concatenated PP cotton filter element with snakelike arrangement,
It is provided with sewage flow pipeline outside filter core, is provided on sewage flow pipeline and deposits dirty chamber, the first outlet is set to PP
The top of cotton processing component.
The first outlet of the PP cotton processing component is entered by inlet water solenoid valve and the first active carbon processing component
Mouth connection.
The first active carbon processing component includes shell, entrance, active carbon treatment trough and outlet, the entrance and exit
It being arranged on shell, the active carbon treatment trough includes exocoel and inside groove, and the exocoel is fixed at the enclosure interior,
The exocoel is top end opening, and the cylindrical of bottom end closure is arranged, and the entrance is connect with the top of exocoel side, the outlet
It is connect with the bottom end of exocoel, inside groove setting is arranged for porous structure, is provided with active carbon in inside groove described outer intracavitary
Grain.
The Amorphous Alloy Grain processing component includes shell, entrance, amorphous particle processing board and outlet, the amorphous
Grain processing board be it is multiple, be vertically arranged inside the housing, be porous stainless steel plate outside the amorphous particle processing board, it is internal
It is provided with amorphous particle, the amorphous particle is Fe by atomic ratio69Ni12Sm0.2Tb0.8C3B6La3P6, average grain diameter 5.3mm；
The outlet is connected with the entrance of the reverse osmosis membrane component.
The reverse osmosis membrane component includes shell, reverse osmosis membrane frame and reverse osmosis membrane, and the reverse osmosis membrane is arranged in institute
It states on reverse osmosis membrane frame, the reverse osmosis membrane successively includes water process non-woven fabrics base support layer, polysulfones is high-molecular porous holds
Hold in the palm layer, the ultra-thin dense separation layers of aromatic polyamides and graphite oxide ene coatings；The graphene oxide coating spraying is described
On the ultra-thin dense separation layers of aromatic polyamides；Two outlets, one outlet and the waste water is arranged in the reverse osmosis membrane component
Tapping equipment connection, another is connected by the high-voltage switch gear with the entrance of the second active carbon processing component.
The wastewater discharge device is for discharging the waste water that the reverse osmosis membrane component is discharged.
The second active carbon processing component includes the second active carbon treatment trough, setting in the second active carbon treatment trough
Active charcoal mixed processing agent particle, the component of the active carbon mixed processing agent particle is according to the mass fraction are as follows: active carbon: 13
Part, starch: 12 parts, Sodium Polyacrylate: 2.2 parts, sodium chloride: 1 part, phytone: 2 parts, the active carbon mixed processing agent
The average grain diameter of particle is 0.8cm.
The PP cotton filter element be 6, pore size filter be followed successively by 1.21 μm, 1.2 μm, 1.1 μm, 1.0 μm, 0.9 μm and
1.0μm。
The active carbon mixed processing agent particle is porous particle.
The average grain diameter of the amorphous particle is 6.6mm.
The high-molecular porous supporting layer of polysulfones with a thickness of 96nm, the material of the ultra-thin dense separation layers of aromatic polyamides
Matter be equal benzene trimethamide, the graphite oxide ene coatings with a thickness of 80nm.
The aperture of the high-molecular porous supporting layer of polysulfones is 0.00019 μm.
The threshold value of temperature detection part is set as 92.2 DEG C in the boiled water storage detection tank.
Claims (5)
1. a kind of drinking device, which is characterized in that including drinking-water component, heating element, heat-exchanging part and purification device；
The drinking-water component is including turning on the tap, high temperature temperature tap, low temperature warm water are leading, cold water faucet and boiled water storage detect
Tank, the first outlet for storing detection tank with the boiled water of turning on the tap are connected, and the second of the boiled water storage detection tank goes out
Mouth is connected with the heat-exchanging part, and the entrance of the boiled water storage detection tank is connected with the heating element；Boiled water storage inspection
It surveys tank and is internally provided with temperature detection part, when threshold value of the temperature lower than setting, the valve of second outlet is opened, and is opened described
Water in water storage detection tank is flowed into the heat-exchanging part；
The purification device setting is there are three outlet, and first outlet is connected with the heating element, second outlet and heat exchange department
Part is connected, and third outlet is connected with the cold water faucet；
The heating element is flowed into described for heating the water that the purification device first outlet flows into after boiling
In boiled water storage detection tank；
The heat-exchanging part includes the snake pipe of shell and interior of shell setting, and there are two enter for the heat-exchanging part setting
Mouth and two outlets, first entrance are connected with the second outlet that the boiled water stores detection tank, and boiled water storage is detected
The hot water of the second outlet outflow of tank is input in the snake pipe, and the snake pipe is connected with first outlet, and described the
One outlet is connected with the high temperature temperature tap, and second entrance is connected with the second outlet of the purification device, and will be described net
The purified water for disguising the second outlet outflow set is input in shell and carries out heat exchange, heat with the hot water in the snake pipe
Water after exchange is connected by second outlet with the low temperature warm water faucet；
The purification device successively include PP cotton processing component, the first active carbon processing component, Amorphous Alloy Grain processing component,
Reverse osmosis membrane component, wastewater discharge device and the second active carbon processing component；
The PP cotton processing component includes that entrance, multiple concatenated PP cotton filter elements and the first outlet and second positioned at downside go out
Mouthful, it the entrance and water supply pipe and is pressurized water inlet line and connect, the pressurized metal pipeline will be from PP cotton processing component
The water of second outlet outflow is passed through the entrance of PP cotton processing component again after pressurization, is increased by threeway and low tension switch control
It is pressed into the opening and closing of waterpipe and water supply pipe, the multiple concatenated PP cotton filter element is arranged outside filter core with snakelike arrangement
There is sewage flow pipeline, be provided on sewage flow pipeline and deposit dirty chamber, the first outlet is set to the upper of PP cotton processing component
Portion；
The first outlet of the PP cotton processing component is connected by the entrance of inlet water solenoid valve and the first active carbon processing component
It is logical；
The first active carbon processing component includes shell, entrance, active carbon treatment trough and outlet, and the entrance and exit is all provided with
It sets on shell, the active carbon treatment trough includes exocoel and inside groove, and the exocoel is fixed at the enclosure interior, described
Exocoel is top end opening, and the cylindrical setting of bottom end closure, the entrance connect with the top of exocoel side, the outlet and outside
The bottom end of chamber connects, and the inside groove setting is arranged for porous structure, is provided with active carbon particle in inside groove described outer intracavitary；
The Amorphous Alloy Grain processing component includes shell, entrance, amorphous particle processing board and outlet, at the amorphous particle
Manage plate be it is multiple, be vertically arranged inside the housing, be porous stainless steel plate, inside setting outside the amorphous particle processing board
There is amorphous particle, the amorphous particle is Fe by atomic ratio69Ni12Sm0.2Tb0.8C3B6La3P6, 5 ~ 8mm of average grain diameter；It is described
Outlet is connected with the entrance of the reverse osmosis membrane component；
The reverse osmosis membrane component includes shell, reverse osmosis membrane frame and reverse osmosis membrane, and the reverse osmosis membrane setting is described anti-
On permeable membrane frame, the reverse osmosis membrane successively include water process non-woven fabrics base support layer, the high-molecular porous supporting layer of polysulfones,
The ultra-thin dense separation layers of aromatic polyamides and graphite oxide ene coatings；The graphene oxide coating spraying is poly- in the fragrance
On the ultra-thin dense separation layers of amide；Two outlets are arranged in the reverse osmosis membrane component, and one outlet and the discharge of wastewater fill
Connection is set, another is connected by high-voltage switch gear with the entrance of the second active carbon processing component；
The wastewater discharge device is for discharging the waste water that the reverse osmosis membrane component is discharged；
The second active carbon processing component includes the second active carbon treatment trough, is provided with work in the second active carbon treatment trough
Property charcoal mixed processing agent particle, the component of the active carbon mixed processing agent particle is according to the mass fraction are as follows: active carbon: 11 ~ 15
Part, starch: 11 ~ 12 parts, Sodium Polyacrylate: 1 ~ 3 part, sodium chloride: 1 ~ 2 part, phytone: 1 ~ 2 part, the active carbon mixing
The average grain diameter of inorganic agent particle is 0.6 ~ 1.0cm.
2. drinking device according to claim 1, which is characterized in that the PP cotton filter element is 6, and pore size filter is successively
It is 1.2 ~ 1.5 μm, 1.1 ~ 1.3 μm, 1.0 ~ 1.2 μm, 0.9 ~ 1.1 μm, 0.8 ~ 1.0 μm and 0.9 ~ 1.1 μm.
3. drinking device according to claim 1, which is characterized in that the active carbon mixed processing agent particle is porous
Grain.
4. drinking device according to claim 1, which is characterized in that the average grain diameter of the amorphous particle is 6 ~ 8mm.
5. drinking device according to claim 1, which is characterized in that temperature detection part in the boiled water storage detection tank
Threshold value be set as 92 ~ 95 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611001448.0A CN106348515B (en) | 2016-11-15 | 2016-11-15 | A kind of drinking device |
Applications Claiming Priority (1)
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6075389A (en) * | 1983-09-30 | 1985-04-27 | Mitsubishi Electric Corp | Apparatus for producing potable water |
| CN2457945Y (en) * | 2000-12-13 | 2001-11-07 | 关险峰 | Apparatus for making cold, warm and hot drinking water |
| DE102006009411B4 (en) * | 2006-03-01 | 2010-07-08 | Dünnleder, Werner, Dipl.-Ing. | Plant for heating drinking water and killing legionella and other germs |
| CN204071750U (en) * | 2014-08-28 | 2015-01-07 | 张付玲 | Electricity separation formula energy-saving drinking machine |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6075389A (en) * | 1983-09-30 | 1985-04-27 | Mitsubishi Electric Corp | Apparatus for producing potable water |
| CN2457945Y (en) * | 2000-12-13 | 2001-11-07 | 关险峰 | Apparatus for making cold, warm and hot drinking water |
| DE102006009411B4 (en) * | 2006-03-01 | 2010-07-08 | Dünnleder, Werner, Dipl.-Ing. | Plant for heating drinking water and killing legionella and other germs |
| CN204071750U (en) * | 2014-08-28 | 2015-01-07 | 张付玲 | Electricity separation formula energy-saving drinking machine |
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