Summary of the invention
The technical issues that need to address of the present invention are to provide a kind of healthy comfortable economical air conditioner, the temperature of this kind of air conditioner air-out and humidity can independently control, comprise and accomplish significantly to reduce air humidity when reducing room temperature hardly by single-cooling type air-conditioner, use in the air conditioning mode of " dehumidifying; cooling is auxiliary ", process out that humidity is slightly low, moderate temperature, good for health and comfortable air, and environmental protection and energy saving more.
Present invention also offers a kind of processing method to air.
The present invention is healthy, and comfortable economical air conditioner can take following technical scheme:
A kind of healthy comfortable economical air conditioner, comprises combined evaporimeter, demist chamber, water smoke intercepts net, discharge outlet, can provide the heat exchange circulating device of heat exchange medium; It is characterized in that: its inside of described combined evaporimeter is provided with multiple spaced inlet channel adjacent one another are and return gas channel, the top of described inlet channel and the top of return gas channel are provided with air inlet and return air outlet accordingly, and the below of inlet channel and the below of return gas channel are provided with gas entry outlet and return air inlet accordingly; Dehumidifying heat pipe runs through the below of inlet channel and the below of return gas channel, and air outlet heat pipe runs through the top of inlet channel and the top of return gas channel; Dehumidifying heat pipe, air outlet heat pipe are respectively linked in its heat exchange circulation loop of heat exchange circulating device respectively; Described combined evaporimeter is provided with the demist chamber being communicated with gas entry outlet and return air inlet below it, and its inside, demist chamber is provided with the water smoke preventing gas entry outlet and return air inlet to be directly communicated with and intercepts net, discharge outlet connection demist chamber.
The present invention deals with problems and can also take following corrective measure further:
Described air inlet and return air outlet are correspondingly arranged on the top of inlet channel, return gas channel respectively, or are correspondingly arranged on the side at close top place of inlet channel, return gas channel respectively; Described gas entry outlet and return air inlet are correspondingly arranged on the bottom of inlet channel, return gas channel respectively, or are correspondingly arranged on inlet channel, the side of return gas channel near bottom respectively.
The described central point of each its air inlet of inlet channel and the central point line of gas entry outlet are the first line, the central point of the return air inlet of the adjacent return gas channel of this inlet channel and the central point line of return air outlet are the second line, first line produces orthographic projection on the vertical plane crossing the second line, and this orthographic projection is crossing with the second line.
Described air inlet outside is provided with air intake cover, and its inner chamber of air intake cover communicates with all air inlet; Described return air outlet outside is provided with outlet housing, and its inner chamber of outlet housing communicates with all return air outlet.
Described water smoke intercepts net and is at least one or more, and water smoke intercepts net and is located between gas entry outlet in its chamber, demist chamber and return air inlet.
Described inlet channel and return gas channel are separated by the fin being positioned at its main body of combined evaporimeter and form, and the spacing of fin is between 1 millimeter to 9 millimeters.
Described air outlet heat pipe its arrange near return air outlet.
Described discharge outlet is arranged on the extreme lower position in demist chamber.
Its heat exchange circulation loop of described heat exchange circulating device is made up of heat exchange circulation major loop and heat exchange circulation branch road, dehumidifying heat pipe belongs to heat exchange circulation major loop, air outlet heat pipe belongs to heat exchange circulation branch road, dehumidifying heat pipe is linked in heat exchange circulation major loop, and air outlet heat pipe is linked in heat exchange circulation branch road.
The processing method of the present invention to air takes following technical scheme:
The comfortable economical air conditioner of health, to a processing method for air, is characterized in that: comprise the following steps, 1) air entered from the external world is carried out precooling; 2) air setting after precooling is separated out water droplet; 3) air after condensation water droplet is intercepted net separation water smoke wherein by water smoke; 4) again the air backheating being intercepted net by water smoke; 5) going out extraneous air conditioning to temperature required rear outflow.
The comfortable economical air conditioner of health, to a processing method for air, is characterized in that: comprise the following steps, 1) the air entered from the external world by inlet channel precooling; 2) air after precooling is passed through dehumidifying heat pipe peripheral region condensation water droplet; 3) air after condensation water droplet is intercepted net separation water smoke wherein by water smoke; 4) again being intercepted the air of net by water smoke by return gas channel backheat; 5) again by air outlet heat pipe going out extraneous air conditioning to temperature required rear outflow.
Technique scheme has such technique effect:
1, the heat pipe that independently dehumidifies is adopted to be responsible for air dewetting, and increase the heat exchange path of air and fin, inlet channel adds the precooling link of air, evaporimeter can make air obtain lower dew point under equal evaporating temperature, separate out more juicy, when solving megathermal climate dehumidifying, leaving air temp is higher causes the not enough problem that dehumidifies.
When 2, setting up water smoke obstruct net effective prevention air inflow return gas channel, dew and the water smoke be suspended in air are brought into, improves effect on moisture extraction further.
3, return gas channel adds the backheat link of air, the too low problem of leaving air temp after dehumidifying when solving microthermal climate, air after dehumidifying backheat is adjusted to most suitable leaving air temp finally by air outlet heat pipe, air-out air humidity and temperature can independently control flexibly, solve dehumidifying condensation temperature and the problem that mutually pins down of leaving air temp.
4, intensive adjacent inlet channel and return gas channel in combined evaporimeter, the line of centres of respective air access ports intersects at the projection line of fin place plane, the convection current of turnover air-flow large area intersection is made to realize efficient heat exchange, realize the sensible heat fast transfer between turnover air, when not needing to provide energy from outside, the air entering in combined evaporimeter and go out is made to obtain pre-cold-peace backheat respectively, reduce when dehumidifying because air sensible changes the energy consumed, reduce refrigeration compressor load, save air-conditioner power consumption.
5, air outlet heat pipe independently can belong to different heat exchange circulation loops separately respectively from dehumidifying heat pipe, air-out heat pipe can be lowered the temperature to air-out or heat, and by controlling the flow of heat exchange medium, realizing air dewetting cooling, simple dehumidifying respectively, dehumidify the comprehensive function of heating, heating merely.
6, structure of the present invention is simple, makes easily, widely applicable, easy to use.
7, the present invention changes into the handling process of existing " air intake-cooling is along band dehumidifying-air-out " handling process of " air intake-precooling-independent dehumidification by condensation-aerosol isolation-backheat-independent temperature adjustment-air-out ", since traditional air conditioner technology is consistent, " dehumidifying dew point must from leaving air temp " changes into the refrigerated dehumidification pattern of " dehumidifying dew point is not from leaving air temp ", the temperature of air conditioner air-out and humidity can independently control, and comprise and accomplish significantly to reduce air humidity when reducing room temperature hardly by single-cooling type air-conditioner.The present invention uses in the air conditioning mode of " dehumidifying, cooling is auxiliary ", and humidity is slightly low, moderate temperature to provide one to process out, more good for health and comfortable air and the air-conditioner of environmental protection and energy saving more.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is specifically described.
Embodiment: as shown in Figures 1 to 6, healthy comfortable economical air conditioner, comprises combined evaporimeter 4, demist chamber 7, water smoke intercepts net 8, discharge outlet 9, can provide the heat exchange circulating device of heat exchange medium; Its inside of described combined evaporimeter is provided with multiple inlet channel 14 adjacent one another are and return gas channel 15, the top of described inlet channel 14 and the top of return gas channel 15 are provided with air inlet 17 and return air outlet 20 accordingly, and the below of inlet channel 14 and the below of return gas channel 15 are provided with gas entry outlet 19 and return air inlet 21 accordingly; Multistage dehumidifying heat pipe 10 runs through the below of inlet channel 14 and the below of return gas channel 15, and multistage air outlet heat pipe 13 runs through the top of inlet channel 14 and the top of return gas channel 15; Dehumidifying heat pipe 10, air outlet heat pipe 13 are respectively connected with its heat exchange circulation loop of heat exchange circulating device respectively; Described combined evaporimeter is provided with the demist chamber 7 being communicated with gas entry outlet 19 and return air inlet 21 below it, and its inside, demist chamber 7 is provided with the water smoke preventing gas entry outlet 19 and return air inlet 21 to be directly communicated with and intercepts net 8, and discharge outlet 9 is communicated with demist chamber 7.Heat exchange circulating device in this example is made up of refrigeration compressor 1, condenser 2, choke valve 3, room temperature control valve 11, by-passing valve 12, the outlet of refrigeration compressor 1 and condenser 2, choke valve 3, the heat pipe 10 that dehumidifies, by-passing valve 12 are sequentially connected in series, the outlet of by-passing valve 12 is connected with refrigeration compressor 1 entrance, and refrigeration compressor 1, condenser 2, choke valve 3, dehumidifying heat pipe 10, by-passing valve 12 form heat exchange circulation major loop; Room temperature control valve 11 and air outlet heat pipe 13 are connected in series and form heat exchange circulation branch road, and the entrance of room temperature control valve 11 is communicated with the entrance of by-passing valve 12, the outlet of air outlet heat pipe 13 and by-passing valve 12 outlet.
Described inlet channel 14 and return gas channel 15 are separated by the fin 16 being positioned at its main body of combined evaporimeter and form; Its dehumidifying heat pipe 10 of combined evaporimeter 4 paramountly roundaboutly upwards to extend from low, and its each horizontally disposed horizontal pipeline section is each passed through the fin 16 of combined evaporimeter 4 inferior portion; Air outlet heat pipe 13 paramountly roundaboutly upwards to extend from low, and its each horizontally disposed horizontal pipeline section is each passed through the fin 16 of combined evaporimeter 4 upper section.
As shown in Figure 2, Figure 3, Figure 4, described air inlet 17 is arranged on the top of inlet channel 14 or the side by top, return air outlet 20 is arranged at the top of return gas channel 15 or the side by top, and described gas entry outlet 19 and return air inlet 21 are correspondingly arranged on inlet channel, the bottom of return gas channel or the side by bottom respectively.
The described central point of its air inlet 17 of each inlet channel and the central point line of gas entry outlet 19 are the first line, the central point of the return air inlet 21 of the adjacent return gas channel of this inlet channel and the central point line of return air outlet 20 are the second line, first line produces orthographic projection on the vertical plane crossing the second line, and this orthographic projection is crossing with the second line.Gas flowing main road line and the gas through return gas channel through the inlet channel main road line that flows can be made so interlaced, be beneficial to when gas runs in inlet channel and return gas channel and there is the longest route, the heat exchange of gas and inlet channel or its wall of return gas channel can be made to carry out more thorough, heat exchange is more abundant, can improve heat exchanger effectiveness.
The formation of described air inlet, gas entry outlet, return air inlet, return air outlet can be implemented the appropriate section of closed inlet channel or return gas channel upper and lower end aperture position by tamper 18 and be formed.
Described air inlet 17 outside is provided with air intake cover 5, and its inner chamber of air intake cover 5 communicates with all air inlet 17; Described return air outlet 20 outside is provided with outlet housing 6, and its inner chamber of outlet housing 6 communicates with all return air outlet 20; All air inlet 17 are communicated to total air inlet 22 by air intake cover 5, and all return air outlet 20 are communicated to total air outlet 23 by outlet housing 6.
Described water smoke intercepts net 8, and to be at least one also can be multiple, and water smoke intercepts net 8 and is located between gas entry outlet 19 in its chamber, demist chamber 7 and return air inlet 21.
Described air outlet heat pipe 13 its arrange near return air outlet 20.
Described discharge outlet 9 is arranged on the extreme lower position in demist chamber.
The comfortable economical air conditioner of health, to a processing method for air, comprises the following steps, 1) the air entered from the external world by inlet channel precooling; 2) air after precooling is passed through dehumidifying heat pipe peripheral region condensation water droplet; 3) air after condensation water droplet is intercepted net separation water smoke wherein by water smoke; 4) again being intercepted the air of net by water smoke by return gas channel backheat; 5) again by air outlet heat pipe going out extraneous air conditioning to temperature required rear outflow.
Operation principle:
Below the present invention is mainly set forth to the processing method of air humidity and temperature, flow process and relative theory, and its difference with conventional art and the part that improves.
The healthy comfortable economical air conditioner of the present invention, ordered about by refrigeration compressor, refrigerant is entered by the dehumidifying heat pipe of choke valve by combined evaporimeter, roundabout arrival elevated outlet flows out from the bottom to top, be divided into two-way afterwards, room temperature control valve of leading up to enters air outlet heat pipe, and another road exports through by-passing valve and air outlet heat pipe the refrigerant flowed out and converges and enter refrigeration compressor.Room air is ordered about by blower fan, inlet channel is entered by each air inlet in air intake cover by total air inlet, flow through fin and dehumidifying heat pipe from top to bottom, intercept net through water smoke after arriving demist chamber and enter return gas channel, and flow through dehumidifying heat pipe and its periphery fin from the bottom to top, flowed out by return air outlet after flowing through air outlet heat pipe and its periphery fin again, concentrate finally by outlet housing and flowed out by total air outlet.In combined evaporimeter, the air of each inlet channel from top to bottom flows, first heat exchange is produced by conduit wall with the air flowed out from the bottom to top through return air channel after cooling, then the refrigerant flowed from the bottom to top with dehumidifying heat pipe produces heat exchange, combined evaporimeter Inside Air Temperature is from top to bottom reduced gradually, close to the temperature of room air above it, below is close to the surface temperature of dehumidifying heat pipe.
Cross heat pipe and the swelling metal section of inlet channel and return gas channel, the air of its internal flow can be allowed to form turbulent flow, improve the heat exchanger effectiveness of turnover air further.
Intensive adjacent air inlet return gas channel in combined evaporimeter, the convection current of turnover air-flow large area intersection is made to realize efficient heat exchange by the air access ports of the distribution in diagonal angle, realize the sensible heat fast transfer between turnover air, make the air entering in combined evaporimeter and go out obtain pre-cold-peace backheat respectively.
Air is by inlet channel contact heat spreader and dehumidifying heat pipe from top to bottom, and its temperature progressively reduces, and when the saturated dew point of temperature lower than steam, in air, the moisture of supersaturated concentration will be separated out and air separation.
Become liquid state with the moisture after air separation from gaseous state, part water droplet flows to bottom demist chamber and discharges through discharge outlet, but part can in vaporific suspension in atmosphere, if not to this part water smoke process, these moisture are easy to follow air and return to indoor.
For preventing that the water smoke that formed in demist chamber is altered, in demist chamber, arrange water smoke intercept net, must flow through obstruct net from the turn back air of return gas channel of inlet channel like this, the water smoke in air meets the obstruct net of low temperature, extension pearl can be formed gutter down, effectively stop water smoke to be taken out of with air.
Air after cooling demist is turned back from the bottom to top from demist chamber and is entered each return gas channel, because the temperature of combined evaporimeter raises from the bottom to top gradually, can absorb the heat of air in inlet channel by conduit wall when air up flows below return gas channel makes its temperature progressively recover, because its temperature of the heat exchange temperature difference can be more lower slightly than room temperature, as needs cool further to air, by the cold medium flux of room temperature governor valve control air outlet heat pipe, again can lower the temperature to air-out as required, be adjustable to suitable leaving air temp.By controlling throttle valve control cold medium flux or evaporating pressure, controlled refrigeration coagulates dew-point temperature to regulate moisture removal, by controlling the cold medium flux ratio between room temperature control valve and by-passing valve, can control leaving air temp flexibly, the leaving air temp of air-conditioner and humidity can independently control.
Flow path due to refrigerant first arrives air outlet heat pipe again by dehumidifying heat pipe, how many refrigerants will consume certain cold in the dehumidifying stage, so, the temperature of refrigerant when arriving air outlet heat pipe can not be lower than before, the temperature of air outlet heat pipe is not less than the temperature of dehumidifying heat pipe, the air themperature formed in demist chamber is relatively minimum in all regions, by return gas channel to the last air flowed out, its steam there will not be full concentration that condensation also would not be had again to produce, and or else has the possibility that water smoke or water droplet are taken out of.
When room air flows through inlet channel near dehumidifying heat pipe, absorb the cold of most of air of turning back away after cooling in return gas channel, air fully precooling before contact dehumidifying heat pipe, after flowing through dehumidifying heat pipe peripheral region, a lot of less with the Temperature Difference Ratio conventional air conditioner of periphery heat pipe and fin surface, the lower condensation condition that makes of dew point obtained because of air is improved greatly, when equal evaporating temperature and equal air quantity excessively, the present invention significantly improves than conventional air conditioner dehumidifying usefulness.
The leaving air temp of conventional air conditioner is generally at 8-14 DEG C, and summer its leaving air temp all at 12 DEG C or more, the moisture removal of conventional air conditioner and its leaving air temp have direct relation, air is the region that in its whole cooling procedure, temperature is minimum leaving the region of evaporator fin moment, and the steam-laden concentration in this region determines the water content of the rear air of dehumidifying.The present invention is then different, because its air outlet is not the air region that temperature is minimum in whole cooling procedure, but be positioned at demist chamber, the air moisture content after dehumidifying depends on the saturated concentration of steam in demist chamber.
Conventional air conditioner time of the heat exchange of air and evaporimeter and path very short, the surface temperature of evaporimeter differs very large with its cooled air themperature, more than 30 DEG C, during EAT, its temperature difference is generally at about 10 DEG C, and EAT its temperature difference higher is larger.The present invention makes the heat exchange path of air and fin and time will grow a lot, and its heat exchange temperature difference can at about 2 DEG C, and EAT is high also influenced hardly again.That is, both are when identical evaporator temperature, and the dew point of dehumidification zone of the present invention is low about 8 DEG C, calculates respective steam-laden concentration according to both dew point difference, for air moisture content during air-out air 12 DEG C, conventional air conditioner can only reach 10g/m
3, and the present invention can reach 6.4g/m
3, moisture removal improves 36%.
It should be noted that, evaporating temperature to be turned down exchange low dew point for by being sacrificed the Energy Efficiency Ratio of refrigeration machine by the present invention, but on existing evaporating temperature basis, improve heat exchanger effectiveness to reduce the dew point of air, add water smoke obstruct net in demist chamber to intercept the most dewdrops flowed through in air, and the water smoke suspended between the dew that the fin of conventional air conditioner adheres to and sheet, be easy to be taken out of by blower fan, be commonly called as " spraying white cigarette ".The present invention and conventional air conditioner to the disposal ability of moisture can describe for: the former " grabs many, lacking of race ", and the latter's " grab few, race many ".
The present invention's dehumidifying effect in hot and humid environment significantly improves, be mainly reflected in the air that efficient heat exchange makes to flow through obtain lower dew point and separate out more juicy, connecting inner structure is kept the moisture of separating out here more, comprehensive above when equal evaporating temperature, the present invention can reduce about half than its air-out water content of existing air-conditioner, greatly improves effect on moisture extraction.
The dehumidification mode that traditional air conditioner is taked when room temperature is lower realizes dehumidifying by intermittently starting refrigeration compressor, and which can cause making people feel cold when compressor operation, makes us producing unhappy sensation when compressor stops.When the present invention can reduce room temperature in these cases hardly, continuous dehumidifying produces dry and comfortable air, allows people feel as snug as a bug in a rug.
As below 20 DEG C, the clammy season of relative air humidity more than 95%, can reduce and even close room temperature control valve, air directly blows out by no longer lowering the temperature after the dehumidifying of dehumidifying heat pipe also backheat, air-out relative humidity can about 35%, and by the heat exchange of return air channel and inlet channel air, last leaving air temp can reach 18 DEG C, the air of this temperature is estimated after entering indoor circulation only to reduce within room temperature 1 DEG C, but significantly can reduce air humidity.And conventional air conditioner at the temperature disclosed above, leaving air temp can, below 12 DEG C, in order to satisfied dehumidifying needs, make the indoor of original low temperature can become colder and increase power consumption.
" dehumidification mode " that conventional air conditioner is provided with, may be provided in temperature lower when adopt, when " dehumidification mode ", refrigeration compressor intermittent running constantly reduces to prevent room temperature, also avoids evaporimeter to occur frosting.Simultaneously; the speed of service of breeze fan can reduce when " dehumidification mode "; sometimes slowly; that air is too fast flows through evaporator surface in order to prevent; causing because heat exchange is insufficient steam have little time condensation and affect effect on moisture extraction, also preventing the excessive water droplet being attached to evaporator surface of wind-force from blowing toward indoor.But problem is: the excessive cycle of compressor start-stop, the change wave amplitude of indoor temperature and humidity can be caused excessive, people is allowed to have sense of discomfort, if the cycle of compressor start-stop is too short, because frequent starting can reduce its life-span, and increase power consumption, and breeze fan slows down and also can affect the mobility of room air, and people can be allowed to feel unhappy.
The present invention improves above-mentioned condition completely, when low temperature adopts " dehumidification mode ", the flow-control of refrigerant obtains and seldom even closes by room temperature control valve, the cold that compressor operating produces, almost concentrate on the region release of the dehumidifying heat pipe below combined evaporimeter, the cold finally taken away due to the air flowing through combined evaporimeter is little, the latent heat of the mainly water vapor condensation phase transformation of actual consumption cold, and generally latent heat energy consumption account for refrigeration total amount ratio little, even if compressor break-off, cold stored by combined evaporimeter inside can maintain long period consumption, thus the compressor operating resting period can extend greatly, fast in refrigeration, consume cold slow situation order compressor operating time scale reduce, quit work period at compressor, breeze fan can preserve normal air output always, as long as the temperature below combined evaporimeter is still low, its dehumidification function just can maintain always, as being connected in series constant pressure valve between evaporimeter and compressor, or adopt frequency-changeable compressor or digital scroll compressor, constant evaporating pressure and minimizing cold medium flux when simple dehumidifying, compressor underload can be made to operate continuously, dry air can be produced continuously and less reduce room temperature, continue the humidity keeping room air suitable, temperature and mobility, and it is very energy-conservation.
The present invention when low temperature dehumidification by the commutative sensible heat of about ninety percent of combined evaporimeter, leaving air temp can be allowed close to EAT, namely being used for the power consumption of air cooling-down part during dehumidifying is about 10% of conventional air conditioner, so compared with conventional air conditioner, when dehumidifying, the load of compressor will be lacked a lot, no matter be continuous operation or discontinuous operation, its energy-saving effect all clearly.
The present invention controls the refrigerating capacity of dehumidifying heat pipe by control refrigeration compressor or choke valve, and the water content of adjustable air-out, is strengthened by the regulating valve flow that regulates the room temperature or reduce the refrigerating capacity of air outlet heat pipe, the cooling extent of adjustable air-out.
If dehumidification requirements scope allows, the evaporating temperature of the inner refrigerant of dehumidifying heat pipe can be relatively fixing, and choke valve can adopt capillary.
The heat-conducting medium of dehumidifying heat pipe and air outlet heat pipe internal circulation flow can be the circularly cooling working medium that refrigeration compressor directly provides, also can be the circulating frozen liquid be made up of refrigeration system, the effect produced is similar, overlapped combined evaporimeter between respectively and by multi-pipeline branch cold water more and circulate, can be applicable to central air conditioning project.
The air outlet heat pipe of combined evaporimeter can belong to same heat exchange circulation loop with dehumidifying heat pipe, also three-way valve can be set respectively at air outlet heat pipe gateway end and switch connection peripheral conduits, air outlet heat pipe and dehumidifying heat pipe can be made independently to belong to different heat exchange circulation loops respectively separately.When indoor need conveying warm braw and dehumidify simultaneously, air outlet heat pipe can coordinate with other heat exchange circulation loop, realizes the function that the air after to dehumidifying heats.
Application test example 1:
Answer the detachable air conditioner of the technology of the present invention, comprise and intercept by refrigeration compressor, condenser, outdoor cooling blower, storage tank, filter, choke valve, combined evaporimeter, indoor breeze fan, demist chamber, water smoke the desiccant cooling air-conditioner that net, discharge outlet etc. form.By the air-conditioner configured above, refrigeration working medium can be adopted as heat exchange medium, heat is absorbed at dehumidifying heat pipe and the evaporation of air outlet heat pipe by refrigeration working medium, realize dehumidifying and cooling function to room air, in clammy season, close room temperature control valve, open by-passing valve and can do the use of independent humidity control device.
Application test example 2:
The water-cooled central air-conditioning of application the technology of the present invention, comprises cooling-water machine, circulating chilled water induction system and how overlap the choke valve, combined evaporimeter, breeze fan, demist chamber, the water smoke that are arranged at indoor and intercept net, discharge outlet etc. and jointly form desiccant cooling central air conditioner system.By the central air conditioner system configured above, cooling-water machine can be adopted and by circulating chilled water induction system transporting low temperature cold water as heat exchange medium, implement the dehumidifying of air and cooling by cold water at dehumidifying heat pipe and air outlet heat pipe, when megathermal climate, the air be used in large-scale public place, factory building or many rooms family carries out dehumidifying and lowering the temperature, clammy season closable chamber's temperature control valve do the use of independent humidity control device.Open room temperature control valve, close by-passing valve, dehumidifying heat pipe and air outlet heat pipe are ganged up, only need the flow by controlling throttle valve control cold water, just can control air-out humidity and temperature under certain limit simultaneously, use simple and convenient, during as controlled cold water less flow, air flows through dehumidifying heat pipe and only obtains a small amount of cold, its dew-point temperature can not be too low, moisture is separated out limited, and cold water its temperature when flowing through air outlet heat pipe raises, and does not play cooling effect to air, few flow cold water can only do a small amount of dehumidifying to air.During as controlled cold water intermediate flow, air flows through dehumidifying heat pipe can obtain more cold, its dew-point temperature is lower, larger moisture removal can be realized, but cold water its temperature when flowing through air outlet heat pipe slightly raises, the cold that air obtains at this place is limited, and intermediate flow cold water can be done larger dehumidifying to air and lower the temperature by a small margin.As control cold water comparatively large discharge time, air flows through dehumidifying heat pipe can obtain more cold, its dew-point temperature is relatively low, larger moisture removal can be realized, cold water its temperature when flowing through air outlet heat pipe can keep substantially, can proceed significantly to lower the temperature to air, large discharge cold water can do dehumidifying by a relatively large margin and cooling to air simultaneously.Generally speaking, cold water with cold be first consumed in latent heat needed for dehumidifying, the cold of remainder is used further to the cooling to air-out.
Application test example 3:
The Multifunctional air processing system of application the technology of the present invention, comprises heat pump water chiller-heater machine, hot and cold water cyclic delivery system, four-port conversion value, choke valve, combined evaporimeter, breeze fan, demist chamber, composition jointly such as water smoke obstruct net, discharge outlet etc.By the air treatment system configured above, water chiller/heater can be adopted and circulate conveying cold water and hot water respectively as heat exchange medium by independently hot and cold water cyclic delivery system, circulating water implements dehumidifying or cooling by dehumidifying heat pipe or air outlet heat pipe to air, circulating hot water can be heated air-out by air outlet heat pipe, the circulation route of hot and cold water can be switched as required by switching valve, can dehumidify to air, lower the temperature or heat, can adopt and carry hot and cold water simultaneously, independent conveying hot water, the various ways of independent conveying cold water, realize respectively heating to air dewetting, heat merely, dehumidifying and cooling, the several functions of simple dehumidifying, industry can be widely used in, agricultural, the room air adjustment in the fields such as scientific research or the drying to material.
Application test example 4:
The indoor pool heat pump heat supply of application the technology of the present invention and air dehumidification system.Comprise heat pump compressor, condenser, choke valve, evaporimeter (outdoor), combined evaporimeter (indoor), indoor breeze fan, demist chamber, water smoke obstruct net, discharge outlet, room temperature control valve in combined evaporimeter, air outlet heat pipe and by-passing valve are cancelled, and bypass line is directly connected.The dehumidifying heat pipe of one or more sets combined evaporimeters of indoor is connected in series or in parallel with the refrigerant pipe of outdoor evaporimeter, the latent heat of the indoor damp-heat air of simultaneously stability that cryogenic freezing medium is dehumidified by combined evaporimeter, absorb outside heat together with outdoor evaporator, common support condenser is to the heating of swimming-pool water.Although room air make its temperature the same as original independent dehumidification device after apparatus of the present invention dehumidifying remains unchanged substantially, but the former implements air intake cooling and air-out backheat realizes mainly through heat exchange between air, and the latter is all realized by the acting of compressor, so the former has advantage than the latter from aspects such as energy-conservation, the reliabilities of equipment, and device structure and pipeline more simple, equipment manufacturing cost and engineering cost are more cheap.
Embodiment 2: as shown in Fig. 7 to Figure 11.Described air inlet 17 and return air outlet 20 are correspondingly arranged on the top of inlet channel, return gas channel respectively, and described gas entry outlet 19 and return air inlet 21 are correspondingly arranged on the bottom of inlet channel, return gas channel respectively.
The described central point of its air inlet 17 of each inlet channel and the central point line of gas entry outlet 19 are the first line, the central point of the return air inlet 21 of the adjacent return gas channel of this inlet channel and the central point line of return air outlet 20 are the second line, first line produces orthographic projection on the vertical plane crossing the second line, and this orthographic projection is crossing with the second line.Vertical plane is with horizontal plane orthogonal.All the other are with embodiment 1.In addition in order to design needs, also multiple row air inlet or gas entry outlet can be set in an inlet channel, also multiple row return air inlet or multiple return air outlet can be set at a return gas channel.
Embodiment 3: its heat exchange circulation loop of described heat exchange circulating device is made up of heat exchange circulation major loop and heat exchange circulation branch road, heat exchange circulation major loop is connected with dehumidifying heat pipe, and heat exchange circulation branch road is connected with air outlet heat pipe.
In addition, between adjacent inlet channel, return gas channel, mutual hithermost wall also can be connected.All the other are with embodiment 1.
As shown in figure 12, in addition in order to design needs, also can arrange multiple row air inlet 17 or gas entry outlet 19 in an inlet channel 14, return gas channel 15 is provided with a row return air outlet 20 or return air inlet 21.In like manner, need also to arrange multiple row return air inlet 21 or multiple row return air outlet 20 at a return gas channel 15 by design, inlet channel 14 is provided with a row gas entry outlet 19 or air inlet 17.
Embodiment 4: the feature of this example is, described choke valve can be capillary.
Described combined evaporimeter and demist chamber, except each inlet and outlet and discharge outlet, remaining surface is provided with thermal insulation layer.
Described air outlet heat pipe can belong to same heat exchange circulation loop with dehumidifying heat pipe, also three-way valve can be set respectively at air-out heat pipe gateway end and switch connection peripheral conduits, make air outlet heat pipe can belong to different heat exchange circulation loops respectively from dehumidifying heat pipe is independent separately.
Described combined evaporimeter can be erect to place, and also can be tiltedly place or placing flat, described discharge outlet must be arranged on the extreme lower position in demist chamber.
Embodiment 5: a kind of processing method to air, is characterized in that: comprise the following steps, 1) air entered from the external world is carried out precooling; 2) air setting after precooling is separated out water droplet; 3) air after condensation water droplet is intercepted net separation water smoke wherein by water smoke; 4) again the air backheating being intercepted net by water smoke; 5) again going out extraneous air conditioning to temperature required rear outflow.
The above embodiment only have expressed several embodiment of the present invention, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the scope of the claims of the present invention.It should be pointed out that for the person of ordinary skill of the art, without departing from the inventive concept of the premise, can also make some distortion and improvement, these all belong to protection scope of the present invention.Therefore, the protection domain of patent of the present invention should be as the criterion with claims.