CN103277867B - A kind of High-enthalpy wind bathing device device - Google Patents
A kind of High-enthalpy wind bathing device device Download PDFInfo
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Abstract
A kind of High-enthalpy wind bathing device, including high air enthalpy subsystem, cool-down dehumidification oxygenation subsystem and air channel switching device.High air enthalpy subsystem in the present invention, toilet air is carried out the humidification that heats up, high-order air draught, low level air-out in toilet, can also low level air draught, high-order air-out, form the vertical warm moist air surrounding bather, reach to improve toilet bottom humiture, improve effect of toilet humiture field uniformity.Cool-down dehumidification oxygenation subsystem in the present invention, the pipeline of fin-tube type heat exchanger is flow through by low temperature tap water, heat exchange is carried out again with the hot and humid air of the toilet flowing through fin-tube type heat exchanger fin of centrifugal blower press-in, realize cool-down dehumidification, air themperature reduces, partial pressure of water vapor reduces, attract toilet extraneous air to supplement and enter toilet, so that toilet atmospheric density increases, oxygen partial pressure increases, namely realize oxygen supplement, thus effectively prevent bather from anoxia giddy phenomenon occurring.
Description
Technical field
The present invention relates to a kind of heating indoor damping device, particularly to one low level air draught high position air-out in toilet (or high-order air draught low level air-out) and the High-enthalpy wind bathing device device improving bathing thermal comfort and safety with cool-down dehumidification oxygen-supplying function.
Background technology
Toilet has become a reality most important unitary space in family life, and kinsfolk here carries out washing one's face and rinsing one's mouth, bathing, go to toilet, and completes the key link in family and Personal hygiene activity.But there is following point with bathing in winter between the domestic hygiene of reality:
1, toilet distribution capacity is little
In Residence Design, toilet distribution mainly considers super bath, washing machine, electric consumption on lighting demand, and wire such as copper core sectional area is generally 2.5mm2, rated load is < 3kw, and distribution capacity is little.
2, toilet thermal inertia is big
The product of our quality a material system and specific heat capacity, is called the thermal inertia of this system, and it reflects the complexity that this material system heats.The body of wall of current home toilet, top board, ground, the on-the-spot armored concrete of many employings is built, and later stage finishing again more in addition adopts ceramic tile veneer, causes the building enclosure being made up of body of wall, top board, ground etc. of air in toilet, quality is big, there are about about 10 tons, as a material system, the product of its quality and specific heat capacity, the namely thermal inertia of this system, very big, it is difficult to heat temperature raising, just as a heat " black hole ".As made the homogeneous temperature of toilet building enclosure raise 1 DEG C, it is necessary to heat energy 8.8 × 106J, amounts to electric work 2.44kw about h.
3, toilet specific surface area is big
We, the ratio of toilet internal surface area with toilet volume, are called the specific surface area of toilet, and the physical and chemical indexs such as air themperature humidity in toilet are affected intensity by its reflection toilet building enclosure (body of wall).Specific surface area is more little, affects more little；Specific surface area is more big, affects more big.In the toilet all rooms in house, specific surface area is maximum, say, that the power of influence of the humiture of toilet air etc. physical and chemical index is very huge by the humiture of toilet body of wall.
4, the heater power of current bathing in winter is little, comfortableness is poor
At present, the intensification heater in toilet, because the consideration of environment of paddling, relatively more employing ceiling type bathroom heaters or warm-air drier.
These electric heating products are widely used in toilet warming, there is following problem:
1. the serious super bath of electromagnetic radiation generally adopts high-power bulb or PTC heater element, and particularly head radiation dose is bigger than normal to human body to there is electromagnetic radiation, and the blue ray radiation in electromagnetic radiation is serious to the inpairment of vision of bather's particularly infant；
2. heat release power, toilet that specific surface area big big relative to thermal inertia less than normal, the heating power of 2～3kw is still less than normal；
3. air becomes the use of these heating equipments dry, to some extent solves toilet air heat temperature raising problem, but brings again the problem of another association, relative air humidity rapid decrease after namely heating up simultaneously.Such as by temperature to be 10 DEG C of relative humiditys be 60% air be heated to 30 DEG C, namely its relative humidity drops to 17.3%, air becomes very dry, cause the globule of bather's body surface, the evaporation power of moisture film is strengthened further, and globule moisture film is accelerated from the heat absorption vaporization of bather's body surface, though temperature is high, the hot water of spray also has a small amount of vaporization to make air slowly be humidified, but relative air humidity is still very low, and air enthalpy is low, the creeping chill of bather is still strong.The practical effect of these electric heating appliances is unsatisfactory.
The applicant application number be 201110255087.3, denomination of invention be a kind of heating indoor damping device disclosed in a kind of high-enthalpy bathing device.It includes a frame, described frame arranges a lagging casing, a generation heat and the accommodation space of transmission heat is formed in described lagging casing, this accommodation space can be respectively provided with an inlet scoop and exhaust outlet, self-priming air port starts, order arranges centrifugal blower, bellows chamber, homogenizing plate, fan nozzle, adapter cavity, finned electric hot plate group, until exhaust outlet；
Apparatus above is to adopt small-power accumulation and high-strength heat exothermic technology, as toilet heater, the peak power of its heat release sucks more than 2 times of electrical power up to it, to shorten the time of toilet preheating, and in the follow-up bathing stage, matching to the heat and mass of air with hot water in the process of heat water-spraying, forming relatively stable total heat release power, thus maintaining stablizing of toilet temperature field moisture field；Adopt ventilation heat release and feedwater atomization and vaporization heat release concurrent job technology, while promoting toilet air themperature, air absolute moisture content is significantly increased, stablizes or increase the relative humidity of air, the enthalpy of toilet air and gentle effect are greatly improved.
The applicant also finds in further R&D process, and following place can be improved:
Such as, how to improve the humiture of toilet bottom in the winter time, overcome toilet " hot bottom, top is cold " phenomenon, promote the spatially uniform of toilet humiture field further, to improve the thermal comfort of bathing；
For another example, when summer high temperature bathing or height air enthalpy in winter during bathing, if bather anoxia giddy sign occurs because of hot and humid, how to solve the cool-down dehumidification oxygen supplement problem of toilet air.
Summary of the invention
It is an object of the invention to provide a kind of High-enthalpy wind bathing device device, during to solve the bathing on the low side, hot and humid of toilet bottom humiture or the bathing in summer that exist in prior art domestic bathing in winter process, there is anoxia giddy sign etc. technical problem in bather.
A kind of High-enthalpy wind bathing device device, including high air enthalpy subsystem, air channel switching device and cool-down dehumidification oxygenation subsystem, wherein:
Described high air enthalpy subsystem at least includes the accommodation space forming a generation heat and transmission heat in lagging casing, this accommodation space can be respectively provided with an inlet scoop and exhaust outlet, self-priming air port starts, order arranges aspiration channel, centrifugal blower, bellows chamber, homogenizing plate, fan nozzle, adapter cavity, finned electric hot plate group, exhaust duct, until exhaust outlet；
Described High-enthalpy wind bathing device device adopts low level air draught, high-order air-out；The Hot wet air heating of High-enthalpy wind bathing device device, after toilet top (high position) sprays, moves from top to bottom, is sucked by the aspiration channel low level of High-enthalpy wind bathing device device at toilet bottom, again enters toilet after the humidification that heats up；This endless form can promote the homogenization of toilet humiture field, improves the humiture level of toilet bottom in winter；
Described cool-down dehumidification oxygenation subsystem includes the second air channel arranged separately after described centrifugal blower, the fin-tube type heat exchanger arranged in the second air channel, in the pipe of described fin-tube type heat exchanger, side is connected with tap water pipe line, fin-tube type heat exchanger fin side communicates with centrifugal fan air outlet, this subsystem shares aspiration channel, centrifugal blower with high air enthalpy subsystem, arranges described air channel switching device at centrifugal fan air outlet;When summer high temperature bathing or height air enthalpy in winter during bathing, then can start this subsystem by air channel switching device, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger, the hot and humid air in indoor of centrifugal blower press-in flows through fin-tube type heat exchanger fin side, Hot wet air heating releases heat by described fin-tube type heat exchanger to low temperature tap water, lower the temperature and dehumidify, original decrease in air pressure, thus promoting that the air outside Takd A Bath The Space enters toilet, it is achieved the increase of toilet air oxygen content;
Air channel switching device: for accepting the triggering of user, when bather carries out room air intensification humidification increasing enthalpy operation, is triggered and is closed in the air channel towards fin-tube type heat exchanger, opened in the air channel towards finned electric hot plate group simultaneously；When bather carries out cool-down dehumidification oxygen supplement operation, it is triggered and the air channel towards finned electric hot plate group is closed, the air channel towards fin-tube type heat exchanger is opened simultaneously.
High air enthalpy subsystem in the present invention and cool-down dehumidification oxygenation subsystem, high-order air draught, low level air-out in toilet, can also low level air draught, high-order air-out, form the vertical warm moist air surrounding bather, reach to improve toilet bottom humiture, improve effect of toilet humiture field uniformity.If bather is when summer high temperature bathing or height air enthalpy in winter during bathing, because toilet is hot and humid anoxia giddy sign occurs, then start cool-down dehumidification oxygenation subsystem of the present invention, now low temperature tap water flows through the pipeline of fin-tube type heat exchanger, the hot and humid air of toilet of centrifugal blower press-in flows through the fin of fin-tube type heat exchanger, Hot wet air heating releases heat by fin-tube type heat exchanger to low temperature tap water, realize cool-down dehumidification, become low temperature and low humidity air and again enter toilet.Operating through cool-down dehumidification, air themperature reduces, partial pressure of water vapor reduces, and toilet extraneous air will be attracted to supplement and enter toilet, so that toilet atmospheric density increases, oxygen partial pressure increases, namely realizes oxygen supplement.
Specifically, High-enthalpy wind bathing device device of the present invention has following 2 technological innovations:
This High-enthalpy wind bathing device device has the low level air-out (or low level air draught) of uniqueness, the big technological innovation of cool-down dehumidification oxygen supplement 2.
1, low level air-out (or low level air draught)
The cross section of exhaust duct is rectangle or circle, downwardly extends along wall.The function of exhaust duct is that Hot wet air heating is entered toilet bottom, forms zone of positive pressure at toilet bottom.Namely High-enthalpy wind bathing device device is from the air draught of toilet top, the exhaust duct then passed through under along wall realizes toilet low level air-out, negative pressuren zone is formed at sanitary and balneal room top, Hot wet air heating is entered toilet bottom, zone of positive pressure is formed at toilet bottom, promote that the hot and humid air of toilet bottom is to top movements, promotes the homogenization of toilet humiture field.
Owing to have employed low level air-out, top air draught, the humiture field of toilet air extremely uniform, bathing in winter thermal comfort improves more than 2 times (with toilet air enthalpy for benchmark)
The air outlet of High-enthalpy wind bathing device device and inlet scoop can also be exchanged by the present invention, change low level air draught into；Hot wet air heating, after top sprays, moves from top to bottom, is sucked by High-enthalpy wind bathing device device at toilet bottom, again enters toilet after the humidification that heats up；The homogenization of this endless form equally possible promotion toilet humiture field.
2, cool-down dehumidification oxygen supplement
When summer high temperature bathing or height air enthalpy in winter during bathing, dry if bathing terminates to need that toilet is carried out cool-down dehumidification afterwards, or there is anoxia giddy sign because of hot and humid in bather, then start cool-down dehumidification oxygenation subsystem, now low temperature tap water flows through the pipeline of fin-tube type heat exchanger, the hot and humid air of toilet of centrifugal blower press-in flows through the fin of fin-tube type heat exchanger, Hot wet air heating releases heat by fin-tube type heat exchanger to low temperature tap water, realize cool-down dehumidification, become low temperature and low humidity air and again enter toilet.Operating through cool-down dehumidification, air themperature reduces, partial pressure of water vapor reduces, decrease in air pressure, toilet extraneous air will be attracted to supplement and enter toilet, so that toilet atmospheric density increases, oxygen partial pressure increases, namely realizes oxygen supplement.
Accompanying drawing explanation
The schematic diagram of Fig. 1 High-enthalpy wind bathing device device one of the present invention example feedwater part；
Fig. 2 is the warm moist air schematic diagram of the high-order air draught low level air-out example of High-enthalpy wind bathing device device one of the present invention；
Fig. 3 is the schematic diagram of the high-order air draught low level air-out example host part of High-enthalpy wind bathing device device one of the present invention；
Fig. 4 is the machine system schematic diagram of the high-order air draught low level air-out example of High-enthalpy wind bathing device device one of the present invention；
Fig. 5 is the warm moist air schematic diagram of High-enthalpy wind bathing device device one low level air draught high-low-position air-out of the present invention；
Fig. 6 is the main frame internal air channel schematic diagram of High-enthalpy wind bathing device device one low level air draught high position air-out of the present invention；
Fig. 7 is the machine system schematic diagram of High-enthalpy wind bathing device device one low level air draught high position air-out of the present invention.
Detailed description of the invention
Embodiment one
Refer to Fig. 1 to Fig. 7, a kind of High-enthalpy wind bathing device device, including high air enthalpy subsystem 2, air channel switching device 11 and cool-down dehumidification oxygenation subsystem 1, wherein:
High air enthalpy subsystem 2 can adopt application number to be the subsystem disclosed in 201110255087.3, carries out the switching between high air enthalpy subsystem and cool-down dehumidification oxygenation subsystem 1 by air channel switching device 11.
Such as, high air enthalpy subsystem 2 at least includes the accommodation space forming a generation heat and transmission heat in lagging casing, this accommodation space can be respectively provided with an inlet scoop and exhaust outlet, self-priming air port starts, order arranges centrifugal blower, bellows chamber, homogenizing plate 5, fan nozzle 6, adapter cavity, finned electric hot plate group 8, exhaust duct, until exhaust outlet.Bellows chamber, homogenizing plate 5, fan nozzle 6, adapter cavity, finned electric hot plate group 8 are all provided in the accommodation space of lagging casing.
Centrifugal blower 3, centrifugal blower 3 is arranged on the inlet scoop place of frame, flows through the fin of bellows chamber, homogenizing plate 5, adapter cavity, finned electric hot plate group 8 after the air blower fan 3 by centrifugation boosting that inlet scoop sucks, and heat absorption enters indoor from exhaust outlet 37 after becoming hot blast；The present invention, adopts pressure wind formula structure to make blower fan be operated in low-temperature space, is conducive to effectively protecting the electrical system of centrifugal blower 3, bearing arrangement and preventing impeller deformation, get stuck.Inlet scoop can be connected with high enthalpy controller air inlet pipeline 15
Bellows chamber, bellows chamber is enclosed by lagging casing and homogenizing plate 5 and forms, and is connected with the air outlet of centrifugal blower 3, forms a positive pressure air container.
Homogenizing plate 5, homogenizing plate 5 is fixedly installed on insulation crust, and homogenizing plate 5 erects and arranges.Homogenizing plate 5 includes a metallic plate, and metallic plate arranges some apertures, and the effect of these apertures is to make from the wind of centrifugal blower 3 blowout with in identical speed punching to adapter cavity.The diameter of the aperture on homogenizing plate 5 and the distribution of eyelet be in that suitably to raise be positioned at centrifugal blower 3 after, the pressure of bellows chamber air before homogenizing plate 5, and make air uniformly through homogenizing plate 5, enter the adapter cavity before finned electric hot plate group 8.Namely the aperture of these a little apertures is different, and the closer to centrifugal blower 3, aperture is more big.
Fan nozzle, fan nozzle is arranged on homogenizing plate 5, and pass lagging casing and be connected with water pipe, the expansion angle of fan nozzle is big, and under appropriate pressures, water ejects into fan-shaped vaporific in fan nozzle and injection subtended angle is big, after tiny mist pearl pours in the passage of finned electric hot plate group 8 in company with air, absorb heat carburation by evaporation on fin, forms hot and humid high enthalpy damp-heat air and is expelled to indoor, to increase indoor temperature and humidity.Fan nozzle is connected on tap water pipe line, pipeline there is the first electromagnetic valve 22 control opening and closing, after the first electromagnetic valve 22 receives the pulse signal of unlatching, valve is opened, band pressure tap water sprays through fan nozzle 6, form the water smoke of folding fan shape that subtended angle is about 110 °, under the carrying of the air that water smoke is sent at homogenizing plate 5, march on towards finned electric hot plate group 8 through adapter cavity.In the present embodiment, fan nozzle 6 adopts and is horizontally disposed with, and is perpendicular to homogenizing plate 5 and is arranged on homogenizing plate 5, and the opening of fan nozzle 6 faces toward the diamond shaped air passage of finned electric hot plate group 8.
Adapter cavity, the space between homogenizing plate 5 and finned electric hot plate group 8 is adapter cavity.
The running of high air enthalpy subsystem 2 is as follows: first, and user selects the regenerator temperature of high-enthalpy bathing device, generally has high, medium and low regenerator temperature gear to select for user, then starts power supply, and finned electric hot plate group 8 enters heat storage state；The heat that electrothermal tube sends accumulates on electric hot plate body (present invention is metallic plate) and fin, after reaching the regenerator temperature set, electrothermal tube continues energising work, meanwhile, centrifugal blower 3 starts, and sucks air pressure in toilet to bellows chamber, air in bellows chamber is after homogenizing plate 5 air distribution, uniformly flowing to the finned electric hot plate group 8 that have accumulated heat, air is blown into indoor through exhaust outlet 4 after forming high temperature air from fin absorption heat.Because of finned electric hot plate group 8 regenerator temperature is higher and ventilate beginning time indoor air temperature relatively low, cause fin that the heat transfer temperature difference of room air is bigger, heat release power is big, can reach electrothermal tube power more than 2 times on electric hot plate, it is achieved small-power accumulation of heat, high intensity heat release.The pulse signal that electromagnetic valve in water lines is sent by computer chip controls opening and closing, by regulating length and the cycle of pulse signal, can control the confluent of atomization and vaporization, thus controlling absolute moisture content and the relative humidity of the air of toilet.It is specially, after first electromagnetic valve 22 receives the pulse signal of unlatching, valve is opened, band pressure tap water sprays through fan nozzle, forms the water smoke of the folding fan shape of subtended angle about 110 °, with the air of centrifugal blower 3 press-in, the diamond passages group of electric hot plate fin composition is flowed into after mixing, heat absorption vaporization, heat temperature raising, the hot and humid air becoming high enthalpy injects toilet.
It should be noted that cool-down dehumidification oxygenation subsystem and air channel switching device 11 are this programme one preferably implementations, the high position air-out of low level air draught in the present invention (or high-order air draught low level air-out) is the important inventive point of the present invention.
Namely, a kind of High-enthalpy wind bathing device device, including high air enthalpy subsystem, wherein said high air enthalpy subsystem at least includes the accommodation space forming a generation heat and transmission heat in lagging casing, can being respectively provided with an inlet scoop and exhaust outlet on this accommodation space, self-priming air port starts, and order arranges aspiration channel, centrifugal blower, bellows chamber, homogenizing plate, fan nozzle, adapter cavity, finned electric hot plate group, exhaust duct, until exhaust outlet
Hot wet air heating is entered space bottom by exhaust outlet, zone of positive pressure is formed in space bottom, promote that the hot and humid air of toilet bottom is to top movements, form the vertical warm moist air surrounding bather, to promote the homogenization of toilet humiture field: described air outlet and inlet scoop are separately positioned on low level and a high position, high-order air draught, Hot wet air heating sprays from bottom, sucked by inlet scoop, top, form circulation, High-enthalpy wind bathing device device is from the air draught of toilet top, and the air exhaust passage then passed through under along wall realizes toilet low level air-out；
Or, described aspiration channel downwardly extends setting along wall, and toilet bottom air is sucked by aspiration channel, intensification through high air enthalpy subsystem humidifies, become high enthalpy air, discharge from high-order air outlet, move from toilet top down, form the vertical warm moist air surrounding bather, described air outlet and inlet scoop are separately positioned on a high position and low level, low level air draught, and Hot wet air heating sprays from top, sucked by inlet scoop, bottom, form circulation
Hereinafter have a talk low level air draught high position air-out (or high-order air draught low level air-out) and cool-down dehumidification oxygenation subsystem.
One, high-order air draught low level air-out
High-order air draught low level air exhausting structure, forms the vertical warm moist air surrounding bather, reaches to improve toilet bottom humiture, improve effect of toilet humiture field uniformity.
The cross section of described exhaust duct 20 is rectangle or circle, downwardly extends along wall.Exhaust duct 20 can be arranged to rectangular-shaped, can as air exhaust passage in pipe.The main part of High-enthalpy wind bathing device device can be arranged on the top of exhaust duct 20, and can be provided with the interface installing handware on exhaust duct 20, this with regard to conveniently making integrated by High-enthalpy wind bathing device device, introduces it in detail below and realizes process.
The function of exhaust duct 20 is, Hot wet air heating is entered toilet bottom, forms zone of positive pressure at toilet bottom, promote that the hot and humid air of toilet bottom is to top movements, form the vertical warm moist air surrounding bather, to promote the homogenization of toilet humiture field.Namely, High-enthalpy wind bathing device device is from the air draught of toilet top, the exhaust duct then passed through under along wall realizes toilet low level air-out, negative pressuren zone is formed at sanitary and balneal room top, form zone of positive pressure in bottom, from the air draught of toilet top, the air exhaust passage then passed through under along wall realizes toilet low level air-out, thus forming one " warm moist air cover " around bather, the humiture of the air ambient of Takd A Bath The Space and thermal comfort are all very good.
Described cool-down dehumidification oxygenation subsystem further includes at the second air channel 52 arranged separately after described centrifugal blower 3, the fin-tube type heat exchanger 12 arranged in the second air channel 52, the side of fin-tube type heat exchanger 12 is connected with tap water pipe line, fin-tube type heat exchanger 12 fin side communicates with centrifugal blower 3 air outlet, this subsystem shares aspiration channel, centrifugal blower 3 with high air enthalpy subsystem, arranges air channel switching device 11 at centrifugal blower 3 air outlet;When summer high temperature bathing or height air enthalpy in winter during bathing, then can pass through air channel switching device 11 and start this subsystem, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger 12, the hot and humid air in indoor of centrifugal blower 3 press-in flows through fin-tube type heat exchanger fin 12 side, Hot wet air heating releases heat by described fin-tube type heat exchanger 12 to low temperature tap water, cool-down dehumidification oxygen supplement, becomes low temperature and low humidity oxygen-enriched air and again enters indoor;
Air channel switching device 11: for accepting the triggering of user, when bather carries out room air intensification humidification increasing enthalpy operation, is triggered and is closed in the second air channel 52 towards fin-tube type heat exchanger 12, opened in the first air channel 51 towards finned electric hot plate group 8 simultaneously；When bather carries out cool-down dehumidification oxygen supplement operation, it is triggered and the first air channel 51 towards finned electric hot plate group 12 is closed, the second air channel 52 towards fin-tube type heat exchanger 8 is opened simultaneously.
Second air channel 52, fin-tube type heat exchanger 12, air channel switching device 11 are generally all disposed within accommodation space, namely in the main part of High-enthalpy wind bathing device device.High-enthalpy wind bathing device device, except main part, also includes low portion.This low portion includes the exhaust duct 20 downwardly extending setting along wall, some intensive uniform high enthalpy controller exhaust vents 18 are offered in the bottom of exhaust duct 20, size that exhaust vent 18 is offered and how many not clear and definite regulation, it is usually and can offer the intensive exhaust vent of a few row 18 in the lower end of its exhaust duct, so as to be easier to form one warm moist air by those exhaust vents 18.And the top of exhaust duct 20 can also arrange cool-down dehumidification oxygen supplement air inlet pipeline, high enthalpy controller air inlet pipeline 15, supply line 36 and high enthalpy controller air outlet pipeline 37.In general, air outlet pipeline 37 connects with the wind path of exhaust duct 20, warm moist air is also discharged by the multiple exhaust vents 18 on exhaust duct 20, forms the vertical warm moist air surrounding bather, reaches to improve toilet bottom humiture, improve effect of toilet humiture field uniformity.The main part of High-enthalpy wind bathing device device is arranged on indoor suspended ceiling, downwardly extend along wall and the air draft tube wall of setting arranges the five metals object including faucet 32, gondola water faucet 31, further, the water supply system of five metals object shares with the water supply system 36 of described high air enthalpy subsystem.In toilet, attached wall is installed, integration is carried out with the bathroom hardware object such as faucet, gondola water faucet, form the domestic bathing system of integration, solve the support problem of a small amount of fixing and gondola water faucet not evaporating back water emission problem, faucet of the fan nozzle water of High-enthalpy wind bathing device device, tap water overvoltage formation simultaneously.
Two, low level air draught high position air-out
The air outlet of High-enthalpy wind bathing device device and inlet scoop can also be exchanged by the present invention, change low level air draught high position air-out into.
When adopting low level air draught high position air-out mode, Hot wet air heating, after toilet top air outlet sprays, moves from top to bottom, is sucked by High-enthalpy wind bathing device device at toilet bottom, again enters toilet after the humidification that heats up；The homogenization of this endless form equally possible promotion toilet humiture field.Namely air outlet and inlet scoop are separately positioned on a high position and low level, low level air draught, and Hot wet air heating sprays from top, and bottom is sucked by inlet scoop, form circulation.
The air outlet of High-enthalpy wind bathing device device and inlet scoop are exchanged, namely realize toilet low level air draught by the air channel under along wall, by the air-out of toilet top, equally possible one " warm moist air cover " of formation around bather, the humiture and the thermal comfort that reach the air ambient of bathing are all very good.And be technically easier to realize.
Specifically referring to Fig. 5 to Fig. 7, downwardly extend along wall and arrange air-suction duct 41, and arrange uniform multiple inlet scoop 42 on aspiration channel 41, it is as fresh air inlet and cool-down dehumidification oxygen supplement air inlet pipe road junction.nullAfter this fresh air inlet and cool-down dehumidification oxygen supplement air inlet pipe road junction air intake，Along air-suction duct 41 upwards air-out，Then through the high enthalpy controller intake stack 45 being positioned at above pipeline、46,Dehumidifying oxygen supplement admission line 44 enters the main part of High-enthalpy wind bathing device device，The principle of its realization is substantially similar with the above-mentioned principle mentioned: arrange the first air outlet 51 and the second air outlet 52 after centrifugal blower 3,First air outlet 52 side arranges homogenizing plate 5、Nozzle 6、Finned electric hot plate group 8 etc.，And the fin-tube type heat exchanger 12 arranged in the second air outlet 51，The side of fin-tube type heat exchanger 12 is connected with tap water pipe line，Fin-tube type heat exchanger 12 fin side communicates with centrifugal blower 3 air outlet，This subsystem shares aspiration channel with high air enthalpy subsystem、Centrifugal blower 3，At centrifugal blower 3 air outlet, air channel switching device 11 is set.Air door conversion equipment 11 can realize the switching of the first air outlet 51 and the second air outlet 52 by a guide rail 53.
It addition, the high enthalpy controller air outlet pipeline 43 of pipeline 41 upper end can be passed through during air-out, cool-down dehumidification oxygen supplement outlet pipe 47 carries out air-out.By the air-out of toilet top, equally possible one " warm moist air cover " of formation around bather, the humiture and the thermal comfort that reach the air ambient of bathing are all very good.
Air channel switching device is air-flow threeway mechanism 21, is controlled by a motor, connects the first electromagnetic valve 22 and the second electromagnetic valve 23, open the first electromagnetic valve 22, then start high air enthalpy subsystem, open the second electromagnetic valve 23, then start cool-down dehumidification oxygenation subsystem.
The running of High-enthalpy wind bathing device device is illustrated below as follows with a kind of scheme:
First, user selects the regenerator temperature of High-enthalpy wind bathing device device, generally has high, medium and low regenerator temperature gear to select for user, then starts power supply, and finned electric hot plate group enters heat storage state；The heat that electrothermal tube sends accumulates on electric hot plate body (present invention is metallic plate) and fin, after reaching the regenerator temperature (such as 300 DEG C) set, electrothermal tube continues energising work, simultaneously, centrifugal blower starts, suck the air pressure at toilet top to bellows chamber, air in bellows chamber is after homogenizing plate air distribution, uniformly flow to the finned electric hot plate group that have accumulated heat, after air forms high temperature air from fin absorption heat, exhaust duct to low level exhaust outlet under along wall is blown into indoor, rising is spread around bather below gondola water faucet, again sucked by High-enthalpy wind bathing device device after rising to ceiling.Because of finned electric hot plate group regenerator temperature is higher and ventilate beginning time indoor air temperature relatively low, cause fin that the heat transfer temperature difference of room air is relatively big, heat release power is big, it is achieved small-power accumulation of heat, high intensity heat release.
Secondly, the pulse signal that electromagnetic valve in water lines is sent by computer chip controls opening and closing, by regulating length and the cycle of pulse signal, can control fan nozzle discharge for the water smoke amount in finned electric hot plate group surface evaporation, thus controlling absolute moisture content and the relative humidity of the air of toilet.It is specially, after electromagnetic valve receives the pulse signal of unlatching, valve is opened, band pressure tap water sprays through fan nozzle, form the water smoke of the folding fan shape of subtended angle about 110 °, air with centrifugal blower press-in, the diamond passages group of electric hot plate fin composition is flowed into after mixing, in fin surface heat absorption vaporization, heat temperature raising, becomes hot and humid high enthalpy air, and the exhaust duct under through suitable wall is to low level exhaust outlet flood chamber, below gondola water faucet, spread rising around bather, again sucked by High-enthalpy wind bathing device device after rising to ceiling.
Again, when summer high temperature bathing or height air enthalpy in winter during bathing, if there is anoxia giddy sign because of hot and humid in bather, then start cool-down dehumidification oxygenation subsystem, now low temperature tap water flows through the pipeline of fin-tube type heat exchanger, and the hot and humid air of toilet of centrifugal blower press-in flows through the fin of fin-tube type heat exchanger, and Hot wet air heating releases heat by heat exchanger to low temperature tap water, realize cool-down dehumidification, become low temperature and low humidity air and again enter toilet.Operating through cool-down dehumidification, air themperature reduces, partial pressure of water vapor reduces, and toilet extraneous air will be promoted to supplement and enter toilet, and cause toilet atmospheric density to increase, and oxygen partial pressure increases, namely oxygen supplement.
When High-enthalpy wind bathing device device ventilates with feedwater atomization and vaporization parallel heat release, peak heat release power is up to 4 times of 12kw(electrothermal tube power) more than, heat up extremely quick；The vapour content of High-enthalpy wind bathing device device air outlet reaches 140(g water vapour/kg dry air), it is more than 10 times of PTC warm-air drier, completely eliminates and cause bather's body surface globule water film evaporation thus producing the dry-heat air of " creeping chill "；Air enthalpy (i.e. air energy density) is high, up to more than 3 times of common warm-air drier；Owing to have employed low level air-out, top air draught, the humiture field of toilet air extremely uniform, bathing in winter thermal comfort improves more than 2 times (with toilet air energy density for benchmark)
Implement the feedwater atomization and vaporization heat release parallel with ventilation heat release, improve absolute moisture content and the enthalpy of air in toilet, the energy density of air in toilet is made substantially to increase, be conducive to the skin of gentle bath person, improve the pliability of bath person's limbs, promote blood circulation and body surface microcirculation in bath person's body, accelerate the discharge of bath person's vivotoxin, regulate emotion and the pressure of bath person, make bath person enter physiology and the kilter of psychology.
High-enthalpy wind bathing device device of the present invention have thermal comfort good, significantly energy-conservation, safety good, thermal disinfection, generally be suitable for five big advantages:
1, thermal comfort is good
The damp-heat air of High-enthalpy wind bathing device device brushes, and the heated dry air overcoming tradition electrical heating method generation causes the evaporation of bather's body surface moisture film globule to produce " creeping chill " problem, and space humiture field uniformity is good.
The vapour content of High-enthalpy wind bathing device device air-out reaches 140(g water vapour/kg dry air), it is more than 10 times of PTC warm-air drier, completely eliminates and cause bather's body surface globule water film evaporation thus producing the dry-heat air of creeping chill；Air enthalpy (i.e. air energy density) is high, up to more than 3 times of common warm-air drier；Aerial temperature and humidity field uniformity is good, and bathing in winter thermal comfort improves more than 2 times；
Due to the intensification humidification capability that High-enthalpy wind bathing device device is remarkable so that toilet air is while heating up, and absolute humidity quickly increases, up to 20(g water vapour/kg dry air) more than, peak value is up to 40(g water vapour/kg dry air).
The low level air discharge structure of original creation, High-enthalpy wind bathing device device is from the air draught of toilet top, the exhaust duct then passed through under along wall realizes toilet low level air-out, negative pressuren zone is formed at sanitary and balneal room top, zone of positive pressure is formed in bottom, promote the motion to top of the toilet bottom Hot wet air heating, made toilet top uniform with the humiture of bottom, solve the problem uneven in temperature that toilet humiture field gradient is big, hot bottom, top is cold that conventional heating methods causes at all.
Meanwhile, due also to High-enthalpy wind bathing device device is to the lasting heat effect containing humid air, thus preventing water vapor in air condensation mist formation, it is ensured that toilet air is not only gentle but also become clear.
2, significantly energy-conservation
Winter domestic bathing, the gross energy input intensity in bathroom, at about 20kw, wherein produces the energy expenditure accounting about 85% of hot water, heating energy consumption accounting about 14%, illumination ventilation etc. power consumption accounting about 1%.
The thermal inertia of air, only the 1/4000 of same volume tap water, improve the humiture of air to reduce health hot water consumption, is the energy-conservation main direction of bathing in winter.
High-enthalpy wind bathing device device emission capacity is very big, and peak value reaches more than electrothermal tube power 4 times (12kw)；Heat up extremely quick, up to 20 DEG C/min, preheating time is greatly shortened, decreases the heat waste in warm；The particularly important is, High-enthalpy wind bathing device device adopts low level air-out, toilet bottom temperature and humidity conditions improves at all, reduce the dependence that heat water-spraying is kept out the cold by bather, hot water consumption is greatly decreased, the heating power of water heater can from 10L(17.4kw) more than be reduced to 5L(8.7kw), synthesis energy saving more than 40%;
3, efficient thermal disinfection
High-enthalpy wind bathing device device passes through the circulating-heating to toilet air and humidification, between its electric hot plate fin, air can be made to reach higher temperature, and the absolute moisture content in air is greatly improved, up to 20(g water vapour/kg dry air) more than, peak value is up to 40(g water vapour/kg dry air), become high-temperature hot humid air.
Energy density height, the good fluidity of high-temperature hot humid air, permeability is strong, heat transfer coefficient is big, by modes such as conduction of heat, thermal convection current, heat radiation and condensation heat releases, high level heat is passed to the mycete in air, antibacterial, virus, make its protein oxidation, degeneration, carbonization and electrolyte modified, thus killing the microorganisms such as mycete, antibacterial, virus.
The high-temperature hot of High-enthalpy wind bathing device device wets sterilization method, thoroughly solve existing room air physical disinfection method (such as ultraviolet) or the middle sterilization existed of chemical disinfection method (such as ozone) is thorough, have the technical problem such as drug residue, toxic side effect, it it is the method for high-efficiency broad spectrum the most, solve the such a darkness of toilet, humidity at all, be suitable to again the efficient exterminating bacterium problem in the spatial environments of mycete, antibacterial, virus, growth of microorganism, make toilet real " health ".
4, high security
The accumulation of heat exothermic parts of High-enthalpy wind bathing device device, adopt the " three high " aluminium-based rare-earth alloy foundry goods of elevated operating temperature, high specific heat capacity, high thermal conductivity coefficient, operating temperature includes regenerator temperature < 350 DEG C, is significantly less than the fusing point of alloy material, is operated in safe warm area.
In the warm and humid parallel exotherm of High-enthalpy wind bathing device device, feedwater atomization and vaporization heat release accounts for leading, reduces the leaving air temp of air outlet.
High-enthalpy wind bathing device device adopts has high intelligence, high reliability, man machine interface close friend and the control system with fail safe function.Casting temperature measuring probe adopts thermocouple element, and certainty of measurement is at ± 5 DEG C；High-enthalpy wind bathing device 2 temperature probes of device inner shell arranged outside, arrange 2 temperature detect switch (TDS)s inside shell, point 5 intense excess syndrome execute security protection.Control system can carry out oneself's detection of probe and mainboard, takes fail safe control when controlling thrashing.
High-enthalpy wind bathing device device adopts 50Hz civil power as energy source, it does not have high frequency electromagnetic radiation, it does not have the inpairment of vision that head burn feeling and shortwave blue light produced by bulb-type super bath intense radiation cause；The skin of bather, brain, auditory visual system will not be produced any negative effect.
High-enthalpy wind bathing device device also adopts the by-pass air duct technology of aero-engine, outside air runner is set outside the inner fin type electric hot plate of lagging casing, the part guiding transition region flows through from this runner containing humid gas, the outer surface of cooling fins formula electric hot plate, reduce the skin temperature of High-enthalpy wind bathing device device, under nominal situation, skin temperature < 60 DEG C, further increase the safety of use.
5, universality is good
High-enthalpy wind bathing device device adopts " low suction height is put ", can adapt with the distribution line of average family.
Because the intensification humidification of cold conditions toilet, need in the short time (several minutes), to discharge a large amount of heat energy (million burnt levels), namely high intensity heat release is realized, heat release power to reach more than 10kW, this is excessive with the inhabitation of reality instantly and commercial power condition drop, thus causing directly-heated type electrical heating method to be difficult to apply or actual effect is bad after application reluctantly.For demanding side of the electrical power net number in dispersion user necessarily, there is the powerful thermal load demands such as dry, the heating of short time, intensification humidification.The heavy load power of even moment this short time, is the terminal transformer, switch cubicle, the several times of capacity of distribution line or even the decades of times that design by general power load of user.If to including power transformer, switch cubicle, distribution line carry out capacity-increasing transformation, both bring the increase of investment in fixed assets to user, also result in the more idle operation in the electric power system more time outside short time heavy load simultaneously.
High-enthalpy wind bathing device device adopts " low suction height is put " technology, fill up the wide gap between this energy supply and demand, intensity is changed with the time, realize " small-power accumulation and high-strength heat heat release ", both the above heavy load demand of short time 10kw that toilet in winter cold conditions intensification humidification is required had been solved, make again electrothermal tube suck power < 3kw, adapt with the distribution condition of present average family.
High-enthalpy wind bathing device device implements the strongly exothermic pattern that " ventilation heat release " is parallel with " feedwater atomization and vaporization heat release ".The water smoke that evaporation heat release uses is provided by nozzle.The operating pressure of nozzle nominal situation, at about 2atm, matches with present piped water pressure.
Second embodiment
The present invention can also only include cool-down dehumidification oxygenation subsystem.
A kind of High-enthalpy wind bathing device device, including cool-down dehumidification oxygenation subsystem, wherein:
Described cool-down dehumidification oxygenation subsystem further includes at inlet scoop, centrifugal blower, air channel, the fin-tube type heat exchanger arranged in air channel, the side of described fin-tube type heat exchanger is connected with tap water pipe line, fin-tube type heat exchanger fin side communicates with centrifugal fan air outlet, when summer high temperature bathing or height air enthalpy in winter during bathing, then can start this subsystem, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger, the hot and humid air in indoor of centrifugal blower press-in flows through fin-tube type heat exchanger fin side, Hot wet air heating releases heat by described fin-tube type heat exchanger to low temperature tap water, cool-down dehumidification oxygen supplement, become low temperature and low humidity oxygen-enriched air and again enter indoor.
Described exhaust duct downwardly extends setting along wall, and hot warm air enters the bottom of indoor by exhaust duct, forms zone of positive pressure bottom it, and the hot and humid air in indoor bottom is to top movements.High-enthalpy wind bathing device device is from the air draught of toilet top, and the air channel then passed through under along wall realizes toilet low level air-out, thus forming one " warm moist air cover " around bather, the humiture of the air ambient of Takd A Bath The Space and thermal comfort are all very good.
Or, the air outlet of High-enthalpy wind bathing device device and inlet scoop are exchanged, namely realize toilet low level air draught by the air channel under along wall, by the air-out of toilet top, equally possible one " warm moist air cover " of formation around bather, the humiture and the thermal comfort that reach the air ambient of bathing are all very good.And be technically easier to realize.
The preferred embodiment of the present invention is only intended to help to set forth the present invention.Preferred embodiment does not have all of details of detailed descriptionthe, is not intended to the detailed description of the invention that this invention is only described yet.Obviously, the content according to this specification, can make many modifications and variations.These embodiments are chosen and specifically described to this specification, is to explain principles of the invention and practical application better, so that skilled artisan can utilize the present invention well.The present invention is limited only by the restriction of claims and four corner thereof and equivalent.
Claims (8)
- null1. a High-enthalpy wind bathing device device，It is characterized in that，Including high air enthalpy subsystem，Wherein said high air enthalpy subsystem at least includes the accommodation space forming a generation heat and transmission heat in lagging casing，This accommodation space connects an inlet scoop and an exhaust outlet respectively，Self-priming air port starts，Order arranges aspiration channel、Centrifugal blower、Bellows chamber、Homogenizing plate、Fan nozzle、Adapter cavity、Finned electric hot plate group、Exhaust duct，Until exhaust outlet，Hot wet air heating is entered space bottom by exhaust outlet，High-enthalpy wind bathing device device is from the air draught of toilet top，The exhaust duct then passed through under along wall realizes toilet low level air-out，Negative pressuren zone is formed at sanitary and balneal room top，Zone of positive pressure is formed in bottom，Promote that the hot and humid air of toilet bottom is to top movements，Form the vertical warm moist air surrounding bather，To promote the homogenization of toilet humiture field；Also include air channel switching device and cool-down dehumidification oxygenation subsystem, wherein:Described cool-down dehumidification oxygenation subsystem includes the second air channel arranged separately after described centrifugal blower, the fin-tube type heat exchanger arranged in the second air channel, in the pipe of described fin-tube type heat exchanger, side is connected with tap water pipe line, the fin side of fin-tube type heat exchanger communicates with centrifugal fan air outlet, this subsystem shares aspiration channel, centrifugal blower, exhaust duct with high air enthalpy subsystem, arranges described air channel switching device at centrifugal fan air outlet;When summer high temperature bathing or height air enthalpy in winter during bathing, then start this subsystem by air channel switching device, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger, the hot and humid air in indoor of centrifugal blower press-in flows through fin-tube type heat exchanger fin side, Hot wet air heating releases heat by described fin-tube type heat exchanger to low temperature tap water, lower the temperature and dehumidify, original partial pressure of water vapor reduces, decrease in air pressure, thus promoting that the air outside Takd A Bath The Space enters toilet, realize the pressure of toilet air, the increase of oxygen partial pressure, thus realizing the increase of air oxygen content；Air channel switching device: for accepting the triggering of user, when bather carries out room air intensification humidification increasing enthalpy operation, is triggered and is closed in the air channel towards fin-tube type heat exchanger, opened in the air channel towards finned electric hot plate group simultaneously；When bather carries out cool-down dehumidification oxygen supplement operation, it is triggered and the air channel towards finned electric hot plate group is closed, the air channel towards fin-tube type heat exchanger is opened simultaneously.
- 2. High-enthalpy wind bathing device device as claimed in claim 1, it is characterised in that described air channel switching device is air-flow threeway mechanism, is controlled by a motor.
- 3. High-enthalpy wind bathing device device as claimed in claim 1, it is characterised in that the main part of described High-enthalpy wind bathing device device is arranged on indoor suspended ceiling, downwardly extends along wall and arranges exhaust duct；Exhaust duct tube wall arranges the five metals object including faucet, gondola water faucet, and, the water supply system of five metals object is shared with the water supply system of described high air enthalpy subsystem.
- 4. a High-enthalpy wind bathing device device, it is characterised in that include high air enthalpy subsystem, air channel switching device and cool-down dehumidification oxygenation subsystem, wherein:Described high air enthalpy subsystem at least includes the accommodation space forming a generation heat and transmission heat in lagging casing, this accommodation space is respectively provided with an inlet scoop and exhaust outlet, self-priming air port starts, order arranges aspiration channel, centrifugal blower, bellows chamber, homogenizing plate, fan nozzle, adapter cavity, finned electric hot plate group, exhaust duct, until exhaust outlet；High-enthalpy wind bathing device device realizes from toilet bottom air draught by the air-suction duct arranged along wall, it is heated into after hot and humid air in the air draft of toilet top, so, zone of positive pressure is formed at sanitary and balneal room top, negative pressuren zone is formed in bottom, promote that the hot and humid air in toilet top moves to bottom, form the vertical warm moist air surrounding bather, to promote the homogenization of toilet humiture field；Wherein:Described cool-down dehumidification oxygenation subsystem includes the second air channel arranged separately after described centrifugal blower, the fin-tube type heat exchanger arranged in the second air channel, in the pipe of described fin-tube type heat exchanger, side is connected with tap water pipe line, the fin side of fin-tube type heat exchanger communicates with centrifugal fan air outlet, this subsystem shares aspiration channel, centrifugal blower, exhaust duct with high air enthalpy subsystem, arranges described air channel switching device at centrifugal fan air outlet;When summer high temperature bathing or height air enthalpy in winter during bathing, then start this subsystem by air channel switching device, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger, the hot and humid air in indoor of centrifugal blower press-in flows through fin-tube type heat exchanger fin side, Hot wet air heating releases heat by described fin-tube type heat exchanger to low temperature tap water, lower the temperature and dehumidify, original partial pressure of water vapor reduces, decrease in air pressure, thus promoting that the air outside Takd A Bath The Space enters toilet, realize the pressure of toilet air, the increase of oxygen partial pressure, thus realizing the increase of air oxygen content;Air channel switching device: for accepting the triggering of user, when bather carries out room air intensification humidification increasing enthalpy operation, is triggered and is closed in the air channel towards fin-tube type heat exchanger, opened in the air channel towards finned electric hot plate group simultaneously；When bather carries out cool-down dehumidification oxygen supplement operation, it is triggered and the air channel towards finned electric hot plate group is closed, the air channel towards fin-tube type heat exchanger is opened simultaneously.
- 5. High-enthalpy wind bathing device device as claimed in claim 4, it is characterized in that, described aspiration channel downwardly extends setting along wall, toilet bottom air is sucked by aspiration channel, intensification through high air enthalpy subsystem humidifies, become high enthalpy air, discharge from high-order air outlet, moving from toilet top down, form the vertical warm moist air surrounding bather, described air outlet and inlet scoop are separately positioned on a high position and low level, low level air draught, Hot wet air heating sprays from top, is sucked by inlet scoop, bottom, forms circulation.
- 6. a High-enthalpy wind bathing device device, it is characterised in that include high air enthalpy subsystem, air channel switching device and cool-down dehumidification oxygenation subsystem, wherein:Described high air enthalpy subsystem at least includes the accommodation space forming a generation heat and transmission heat in lagging casing, this accommodation space is respectively provided with an inlet scoop and exhaust outlet, self-priming air port starts, order arranges aspiration channel, centrifugal blower, bellows chamber, homogenizing plate, fan nozzle, adapter cavity, finned electric hot plate group, exhaust duct, until exhaust outlet；Described cool-down dehumidification oxygenation subsystem includes the second air channel arranged separately after described centrifugal blower, the fin-tube type heat exchanger arranged in the second air channel, in the pipe of described fin-tube type heat exchanger, side is connected with tap water pipe line, the fin side of fin-tube type heat exchanger communicates with centrifugal fan air outlet, this subsystem shares aspiration channel, centrifugal blower, exhaust duct with high air enthalpy subsystem, arranges described air channel switching device at centrifugal fan air outlet;When summer high temperature bathing or height air enthalpy in winter during bathing, then start this subsystem by air channel switching device, now low temperature tap water flows through side in the pipe of fin-tube type heat exchanger, the hot and humid air in indoor of centrifugal blower press-in flows through fin-tube type heat exchanger fin side, Hot wet air heating releases heat by described fin-tube type heat exchanger to low temperature tap water, lower the temperature and dehumidify, original partial pressure of water vapor reduces, decrease in air pressure, thus promoting that the air outside Takd A Bath The Space enters toilet, realize the pressure of toilet air, the increase of oxygen partial pressure, thus realizing the increase of air oxygen content；Air channel switching device: for accepting the triggering of user, when bather carries out room air intensification humidification increasing enthalpy operation, is triggered and is closed in the air channel towards fin-tube type heat exchanger, opened in the air channel towards finned electric hot plate group simultaneously；When bather carries out cool-down dehumidification oxygen supplement operation, it is triggered and the air channel towards finned electric hot plate group is closed, the air channel towards fin-tube type heat exchanger is opened simultaneously.
- 7. High-enthalpy wind bathing device device as claimed in claim 6, it is characterized in that, described exhaust duct downwardly extends setting along wall, and Hot wet air heating enters the bottom of indoor by exhaust duct, zone of positive pressure is formed bottom it, the hot and humid air in indoor bottom, to top movements, forms the vertical warm moist air surrounding bather, and described air outlet and inlet scoop are separately positioned on low level and a high position, high-order air draught, Hot wet air heating sprays from bottom, is sucked by inlet scoop, top, forms circulation.
- 8. High-enthalpy wind bathing device device as claimed in claim 6, it is characterized in that, described aspiration channel downwardly extends setting along wall, toilet bottom air is sucked by aspiration channel, intensification through high air enthalpy subsystem humidifies, become high enthalpy air, discharge from high-order air outlet, moving from toilet top down, form the vertical warm moist air surrounding bather, described air outlet and inlet scoop are separately positioned on a high position and low level, low level air draught, Hot wet air heating sprays from top, is sucked by inlet scoop, bottom, forms circulation.
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| CN2013200714568 | 2013-02-07 | ||
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203518116U (en) * | 2013-02-07 | 2014-04-02 | 上海伯涵热能科技有限公司 | Wind bathing device with high enthalpy |
| CN104534540B (en) * | 2014-11-30 | 2017-03-22 | 嘉兴鸿亮光电科技有限公司 | Safe and efficient integrated ceiling bath heater |
| CN105318402B (en) * | 2015-05-26 | 2018-01-02 | 高乃鑫 | Pipeline heating Multifunctional air heater for bathroom |
| CN105318403B (en) * | 2015-07-28 | 2017-12-08 | 高乃鑫 | Lower heating super bath and lower heating type separate body bath warmer |
| CN105466277A (en) * | 2015-08-17 | 2016-04-06 | 浙江鼎美电器有限公司 | Device and method for removing water scale of high-enthalpy bathroom heater through thermal shock |
| CN110332645B (en) * | 2019-07-31 | 2023-12-26 | 宁波东大空调设备有限公司 | Kitchen total heat recovery new fan |
| CN112833543A (en) * | 2020-03-18 | 2021-05-25 | 青岛海尔新能源电器有限公司 | Air energy water heater control method and air energy water heater |
| CN111397092A (en) * | 2020-03-27 | 2020-07-10 | 广东美的制冷设备有限公司 | Air conditioner cleaning control method, air conditioner, storage medium and device |
| CN114110885A (en) * | 2021-12-02 | 2022-03-01 | 重庆科技学院 | Intelligent high-efficiency ventilation system for bathroom space |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2852902Y (en) * | 2005-12-26 | 2007-01-03 | 周慕明 | Domestic bathroom |
| CN201028928Y (en) * | 2007-01-09 | 2008-02-27 | 阮立昂 | Indoor dehumidifier |
| US7900371B1 (en) * | 2008-07-14 | 2011-03-08 | Bullard B Wade | Personal dryer apparatus |
| CN102305438A (en) * | 2011-08-31 | 2012-01-04 | 上海伯涵热能科技有限公司 | High-enthalpy bathing device |
| CN203518116U (en) * | 2013-02-07 | 2014-04-02 | 上海伯涵热能科技有限公司 | Wind bathing device with high enthalpy |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20090109634A (en) * | 2008-04-16 | 2009-10-21 | 한선영 | Stand-type body dry equipment |
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- 2013-05-21 CN CN201310190873.9A patent/CN103277867B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2852902Y (en) * | 2005-12-26 | 2007-01-03 | 周慕明 | Domestic bathroom |
| CN201028928Y (en) * | 2007-01-09 | 2008-02-27 | 阮立昂 | Indoor dehumidifier |
| US7900371B1 (en) * | 2008-07-14 | 2011-03-08 | Bullard B Wade | Personal dryer apparatus |
| CN102305438A (en) * | 2011-08-31 | 2012-01-04 | 上海伯涵热能科技有限公司 | High-enthalpy bathing device |
| CN203518116U (en) * | 2013-02-07 | 2014-04-02 | 上海伯涵热能科技有限公司 | Wind bathing device with high enthalpy |
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| CN103277867A (en) | 2013-09-04 |
| CN203518116U (en) | 2014-04-02 |
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