CN203083043U - Novel efficient-cooling-type dehumidifier - Google Patents
Novel efficient-cooling-type dehumidifier Download PDFInfo
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- CN203083043U CN203083043U CN 201220720205 CN201220720205U CN203083043U CN 203083043 U CN203083043 U CN 203083043U CN 201220720205 CN201220720205 CN 201220720205 CN 201220720205 U CN201220720205 U CN 201220720205U CN 203083043 U CN203083043 U CN 203083043U
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Abstract
The utility model discloses a novel efficient-cooling-type dehumidifier. A Water evaporation condensation system placed on an outdoor principal machine of the novel efficient-cooling-type dehumidifier comprises a shell, a water evaporation module, a low-temperature water-collecting groove and a condensation module, wherein the water evaporation module, the low-temperature water-collecting groove and the condensation module are all placed in the shell, the water evaporation module is used for absorbing heat by evaporating high-temperature water and meanwhile forming low-temperature water drops, the low-temperature water-collecting groove is used for collecting the low-temperature water drops generated by the water evaporation module, and the condensation module is used for exchanging the low-temperature water in the low-temperature water-collecting groove and refrigerant heat to form high-temperature water. The water evaporation module, the low-temperature water-collecting groove and the condensation module are sequentially communicated to form water circulation; the water evaporation module further comprises at least one air inlet, at least one air outlet and at least one cooling fan; and air is absorbed in through the cooling fan and form hot air after heat of the air is absorbed by the high-temperature water, and the hot air is discharged from the air outlet through the cooling fan. The novel efficient-cooling-type dehumidifier is high in condensation effect and low in compressor compression ratio, improves energy efficiency ratios of a traditional whole cooling-type dehumidifier and achieves high efficiency.
Description
Technical field
The present invention relates to the application of evaporation type condensing plant in refrigerating plant, belong to the HVAC technical field, relate in particular to a kind of novel high-energy and imitate cooling type dehumidifier.
Background technology
Dehumidifier is of a great variety at present, mainly contains GENERAL TYPE (being heating type) dehumidifier, cooling type dehumidifier, temperature regulating dehumidifier, the new wind type dehumidifier of part, brand-new wind type dehumidifier, Mobyneb dehumidifier.
The structure of traditional cooling type dehumidifier as shown in Figure 1, it comprises outdoor main frame 1002 (comprising compressor 10010, blower fan, air-cooled condenser system 1000 and expansion valve 10012) and indoor set 1001 (blower fan and copper tube and fin evaporimeter 10011), wherein heat exchange takes place in the air-conditioning system refrigerant in the air-conditioning air-cooled condenser, and the heat that the heat that indoor set 1001 is absorbed in copper tube and fin evaporimeter 10011 and the input work of compressor 10010 transform is transferred to the heat release loop together.
In this system, air-cooled condenser system 1000 is generally powerful axial flow blower and air-cooled condenser, and the refrigerant in the heat release loop carries out heat exchange with the wind that flows through in the air-cooled condenser.Yet the defective of this system is, the theoretical condensation temperature of GB operating mode is forever greater than 35 ℃, and actual condensation temperature is generally with reference to the AIR operating mode of the U.S., and promptly condensation temperature is 54.4 ℃, causes the input power of compressor bigger.Therefore generally between 1.8～2.4L/(hkW), even by improving manufacturing process and increasing system matches, the space of its raising is also very little for the unit power moisture removal of common cooling type dehumidifier.Because the popularity of cooling type dehumidifier is very high, therefore cause the huge waste of the energy.Also have a kind of wet curtain device in the existing water evaporative condenser technology, make hot-air pass through wet curtain evaporation, the temperature of hot-air can reduce, thereby is converted to cold air.Though it is very low that this wet curtain device can not be reduced to air themperature, still can around the workman, create refrigerant, as to be full of bright wind environment as traditional air-conditioning.And the power consumption in when cooling only is 8.9% of traditional air-conditioning.
A kind of air handling system of the prior art based on wet curtain device, as shown in Figure 2, make air contact (contact area increases hundreds of times) with moisture, water absorbs heat-gasification latent heat (heat of 2300kj is taken away in the water evaporation of 1kg approximately) in evaporation process, promptly under the constant condition of enthalpy, absorb the sensible heat of air, the temperature (dry-bulb temperature) of air is reduced.Detailed process is: when the core component (evaporation filter screen 2000) of ozone by equipment, produce heat exchange and filter out airborne dust, making proximal air be similar to along isenthalp changes and is lowered the temperature, the temperature of air is finally dropped to the wet-bulb temperature that is bordering on air, sends air outlet 2003 by blower fan 2002 then.
Summary of the invention
The objective of the invention is to overcome deficiency of the prior art, provide a kind of novel high-energy to imitate cooling type dehumidifier, it can promote the condensation efficiency of cooling type dehumidifier, saves a large amount of operating costs, reduce the compression ratio of compressor simultaneously, improved the service life of unit greatly.
For achieving the above object, described novel high-energy is imitated cooling type dehumidifier, comprise the outdoor main frame of air-conditioning and the indoor set that is communicated with it, be characterized in, described outdoor main frame also comprises a water evaporative condenser system, and described water evaporative condenser system comprises a housing, and the water that all is arranged at described housing interior being used for formation simultaneously by the evaporation high-temperature water absorption heat low temperature globule evaporates module, be used to collect the water at low temperature feeder and the condensation module that is used for water at low temperature in the water at low temperature feeder and refrigerant heat exchange formation high-temperature water that water evaporates the low temperature globule of module generation; Described water evaporation module, water at low temperature feeder and condensation module are communicated with the circulation of formation water in turn; And,
Described water evaporation module also comprises at least one air inlet, at least one air outlet and at least one cooling blower, and air is sucked by described cooling blower, forms hot blast after the evaporation high-temperature water absorbs heat, and hot blast is discharged by air outlet by described cooling blower.
Preferably, described water evaporation module comprises that at least one is arranged at air inlet on the housing, at least one is arranged at air outlet on the housing, at least one cooling blower, at least one evaporates net, at least one sparge pipe and one first water pipe; Each air inlet place disposes an evaporation net, and each evaporation net place disposes a sparge pipe that is used for to evaporation net water spray, and the described sparge pipe of each bar all is connected with described first water pipe; Also comprise the water inlet that is used for water filling in sparge pipe on the described sparge pipe of each bar; Each air outlet place disposes one and is used for air from the air inlet suction and through the described cooling blower of pervaporation net by the air outlet discharge;
Described water at low temperature feeder is positioned at the below of water evaporation module, is used for that water is evaporated the low temperature globule that each evaporation of module drips on the net and collects;
Described condensation module comprises water-cooled condenser and one second water pipe, and described water-cooled condenser comprises separate and adjoins the circulate aquaporin of water of the refrigerant passage and being used to of refrigerant that circulates that is used to of setting; The two ends of described refrigerant passage are respectively by advancing the refrigerant pipe and going out the copper pipe that the refrigerant pipe is connected in the described indoor set and be connected with evaporator fin; One end of described aquaporin connects described water pipe by water pump, and the other end of described aquaporin connects the water at low temperature feeder by second water pipe; And,
It is online that water in each described sparge pipe is sprayed onto corresponding evaporation, stay the low temperature globule on the net in evaporation, the water at low temperature droplet falls and is collected by described water at low temperature feeder, under the effect of described water pump, water at low temperature in the water at low temperature feeder flows in the aquaporin of water-cooled condenser, carry out heat exchange with refrigerant in the condensation channel after, heating up forms high-temperature water, high-temperature water flows to each sparge pipe through the effect of water pump by first water pipe, participates in the water evaporative condenser process of next circulation.
Preferably, each described sparge pipe is provided with a plurality of holes that are used to spray water.
Preferably, each described sparge pipe is provided with a plurality of holes that are used to spray water, and each hole disposes a spray equipment.
Preferably, each described sparge pipe is positioned at the top of corresponding evaporation net, and along the circumferential direction setting that this evaporation is netted, offers a plurality of described holes at the lower wall of each described sparge pipe.
Preferably, each described sparge pipe is positioned at the oblique upper of corresponding evaporation net, and along the circumferential direction setting that this evaporation is netted, offers a plurality of described holes at the sidewall of each described sparge pipe.
Preferably, described water evaporative condenser system comprises that also at least one is used for the water replanishing device of moisturizing in the water at low temperature feeder, described water replanishing device comprises the moisturizing upper hose that at least one is connected with the water at low temperature feeder, and at least one is used for detecting the water at low temperature condensate tank of dehumidifier of described water at low temperature feeder water at low temperature water level.
Preferably, described air outlet is obliquely installed on described housing.
Preferably, described evaporation net is a kind of in common evaporation net, organic filler evaporation net, organic filler honeycomb fashion evaporation net, inorganic filler evaporation net, the inorganic filler honeycomb fashion evaporation net; Described water-cooled condenser is screw shell heat-exhanger, plate type heat exchanger or shell and tube exchanger.
Preferably, describedly advance the refrigerant pipe and go out the refrigerant pipe to be copper pipe.
The operation principle of described water evaporative condenser system is, water pump is pressed into water at low temperature in the water-cooled condenser and refrigerant generation heat exchange, water temperature raises, enter the high-temperature water water entering section, the high-temperature water water entering section provides the higher water of temperature and drenches in evaporation online, high-temperature water toward dirty, when high-temperature water flows to the bottom, has just become water at low temperature along the evaporation net.Cooling blower sucks the air in the environment from air inlet, pass the evaporation net and the water for cooling higher in the process of passing the evaporation net to temperature, water after the cooling continues the dirty water at low temperature gathering-device that enters, the hot blast that the evaporation of flowing through is simultaneously netted is through cooling blower discharge water evaporative condenser system, water pump is pressed into water at low temperature in the water-cooled condenser and refrigerant generation heat exchange once more then, so moves in circles.
Beneficial effect of the present invention is, described novel high-energy is imitated cooling type dehumidifier and is adopted water evaporative condenser mode, to reduce water temperature greatly, and then reduction condensation temperature, make the heat exchanger effectiveness of air-conditioning refrigerant improve greatly, and compact conformation, owing to adopt wet curtain principle heat exchange, the moisturizing that needs seldom, rate of water make-up only is the water yield of evaporative phase-change.Simultaneously by regulating the wind speed of blower fan, can control the water yield of evaporation, and then the water temperature (promptly entering the water temperature in the water-cooled condenser) in the control water at low temperature feeder, thereby adjusting condensation temperature, therefore under different environment, even under the situation of 35 ℃ of environment dry-bulb temperatures, 34 ℃ of wet-bulb temperature, also condensation temperature can be controlled at (being about absolute pressure 12.55bar) about 32 ℃.Therefore the unit power moisture removal of cooling type dehumidifier generally can reach 4.0L/(hkW) even can reach 4.5L/(hkW) more than, saved operating cost greatly, reduced the compression ratio of compressor simultaneously, improved the service life of unit greatly.
Description of drawings
Fig. 1 is the refrigeration system fundamental diagram of traditional cooling type dehumidifier of the prior art.
Fig. 2 is the fundamental diagram of wet curtain air-conditioning (being environment-friendly air conditioner) in the prior art.
Fig. 3 is the structural representation that novel high-energy of the present invention is imitated cooling type dehumidifier.
Fig. 4 is in one embodiment of this invention, and novel high-energy is imitated the internal structure schematic diagram of the water evaporative condenser system in the cooling type dehumidifier.
Fig. 5 is the structural representation of water evaporation module.
Fig. 6 is the fundamental diagram of the water evaporative condenser system shown in Fig. 4 and Fig. 5.
Fig. 7 a is the location diagram that evaporates net and sparge pipe in the water evaporative condenser system shown in Fig. 3 to Fig. 6.
Fig. 7 b is the location diagram that evaporates the another kind of embodiment of net and sparge pipe in the water evaporative condenser system shown in Fig. 3 to Fig. 6.
Fig. 8 shows the side view of the water evaporative condenser system in another embodiment of the present invention.
The specific embodiment
The present invention will be further described in detail below in conjunction with the drawings and specific embodiments:
In the present invention, high-temperature water, water at low temperature are relative concept, but should be appreciated that, in the Air-conditioning Engineering field, high-temperature water can refer to the water of temperature about 32 ℃, and water at low temperature can refer to the water of temperature about 26 ℃.
To shown in Figure 5, described novel high-energy is imitated cooling type dehumidifier and is comprised the outdoor main frame 1002 of air-conditioning and the indoor set 1001 that is connected with this outdoor main frame 1002 as Fig. 3.Especially, described outdoor main frame 1002 also comprises a water evaporative condenser system 100, and described water evaporative condenser system 100 comprises a housing 1 and all is arranged at being used in the described housing 1 and absorbs water evaporation module that heat forms the low temperature globule 306 simultaneously, is used to collect the water at low temperature feeder 5 of the low temperature globule 306 that water evaporation module produces and is used for the condensation module of the water at low temperature in the water at low temperature feeder 5 with refrigerant heat exchange formation high-temperature water by the evaporation high-temperature water; Described water evaporation module, water at low temperature feeder 5 and condensation module are communicated with the circulation of formation water in turn.
In addition, described water evaporation module also comprises at least one air inlet 102, at least one air outlet 103 and at least one cooling blower 4, air is sucked by described cooling blower 4, forms hot blast after the evaporation high-temperature water absorbs heat, and hot blast is discharged by air outlet 103 by described cooling blower 4.Here, the quantity of air inlet 102 can increase or reduce, and for example can be one, two, three, four or six, and each air inlet 102 can be equipped with the baffle plate that has hole 321 or groove.
Particularly, described water evaporation module as shown in Figure 4 comprise four sides that are arranged at housing 1 respectively four air inlets 102, be arranged at housing 1 top air outlet 103, be arranged at the cooling blower 4(axial flow blower at these air outlet 103 places), four evaporation nets 2, four sparge pipes 302 and one first water pipes 304; Each air inlet 102 place disposes an evaporation net 2, described evaporation net 2 can be for having certain thickness, for example 100 millimeters, what evaporation net 2 can be in common evaporation net, organic filler evaporation net, organic filler honeycomb fashion evaporation net, inorganic filler evaporation net, the inorganic filler honeycomb fashion evaporation net is a kind of; Each evaporation net 2 place disposes a sparge pipe 302 that is used for to evaporation net 2 spray high-temperature water, and the described sparge pipe 302 of each bar all is connected with described first water pipe 304; Also comprise the water inlet 301 that is used in sparge pipe 302, annotating high-temperature water on the described sparge pipe 302 of each bar; Described cooling blower 4 sucks air (according to the direction shown in arrow P Fig. 3 and Fig. 41 and the P2) and discharges (according to the direction shown in the arrow P among Fig. 3 and Fig. 4 3) through the thermogenic action of pervaporation net 2 by air outlet 103 from air inlet 102.Especially, for the width that dwindles unit helps preventing the air-out water phenomenon simultaneously, oblique air-out mode is selected in air-out usually, so described air outlet 103 is obliquely installed on described housing 1, as shown in Figure 6.
Described water at low temperature feeder 5 is positioned at the below of water evaporation module, is used for that water is evaporated the low temperature globule 306 that drips on each evaporation net 2 of module and collects.
Described condensation module comprises water-cooled condenser 504 and one second water pipe 305, and described water-cooled condenser 504 is screw shell heat-exhanger, plate type heat exchanger or shell and tube exchanger; Described water-cooled condenser 504 comprises separate and adjoins the circulate aquaporin of water of the refrigerant passage and being used to of refrigerant that circulates that is used to of setting; The two ends of described refrigerant passage are respectively by advancing refrigerant pipe 500 and going out the copper pipe that refrigerant pipe 501 is connected in the described indoor set 1001 and be connected with evaporator fin 10011, advance refrigerant pipe 500 through being connected with evaporator fin 10011 with copper pipe, go out refrigerant pipe 501 and be connected with evaporator fin 10011 with copper pipe through expansion valve 10012 at compressor 10010.Describedly advance refrigerant pipe 500 and go out refrigerant pipe 501 to be copper pipe.One end of described aquaporin connects described first water pipe 304 by water pump 303, and the other end of described aquaporin connects the water at low temperature outlet 6 of water at low temperature feeder 5 by second water pipe 305.Water at low temperature feeder 5 is sent into water-cooled condenser 504 as the water source after the high-temperature water cooling that sparge pipe 302 can be sent becomes water at low temperature more at this moment.
Water in each described sparge pipe 302 is sprayed onto on the corresponding evaporation net 2, on evaporation net 2, stay the low temperature globule 306, the low temperature globule 306 drippages are collected by described water at low temperature feeder 5, under the effect of described water pump 303, water at low temperature in the water at low temperature feeder 5 flows in the aquaporin of water-cooled condenser 504, after carrying out heat exchange with refrigerant in the condensation channel, heat up and form high-temperature water, high-temperature water flows to each sparge pipe 302 through the effect of water pump 303 by first water pipe 304, participates in the water evaporative condenser process of next circulation.
Especially, the position relation between evaporation net 2 and the sparge pipe 302 has two kinds, respectively shown in Fig. 7 a and 7b.With reference to figure 7a, each described sparge pipe 302 is positioned at the top of corresponding evaporation net 2, and along this circumferential direction setting of evaporating net 2, offers a plurality of holes 321 at the lower wall of each described sparge pipe 302, sprays water from the bottom surface to evaporation net 2.With reference to figure 7b, each described sparge pipe 302 is positioned at the oblique upper of corresponding evaporation net 2, and along this circumferential direction setting of evaporating net 2, offers a plurality of holes 321 at the sidewall of each described sparge pipe 302, from the side to evaporation net 2 water sprays.
In the above-described embodiments, sparge pipe 302 is along the circumferential direction setting of evaporation net 2.Here, as shown in Figure 8, the cross section of described evaporation net 2 is " returning " font, the centre is a hollow, circumferential direction along described evaporation net 2, refer to along the zone setting between two " mouths " of the evaporation net 2 that is " returning " font, the shape of the sparge pipe 302 of formation also is " mouth " font, and promptly " mouth " word of these sparge pipe 302 formation is between two " mouths " of evaporation net 2.
Further, can on each hole 321 of offering on the sparge pipe 302, dispose a spray equipment 322 fully to evaporation net 2 water sprays for increasing sparge pipe 302.
In aforementioned cooling procedure, because the part water blower fan 4(axial flow blower that can be cooled with the form of steam to high-temperature water) extract out, so the water in the water at low temperature feeder 5 might reduce gradually, this situation is especially obvious when surrounding air humidity is very low.Be necessary like this water in the water at low temperature feeder 5 is replenished, this replenishing can be realized by a water replanishing device is set.Particularly, described water replanishing device comprises the moisturizing upper hose 71 that at least one is connected with water at low temperature feeder 5, at least one is used for detecting the water at low temperature condensate tank of dehumidifier 72 of described water at low temperature feeder 5 water at low temperature water levels and the switching device that links with this water at low temperature condensate tank of dehumidifier 72, and described water at low temperature condensate tank of dehumidifier 72 can be a ball float.
Preferably, moisturizing magnetic valve and float switch can also be set, be arranged at the top of water at low temperature feeder 5, and link to each other, guarantee not have water to enter water at low temperature feeder 5 when being used for keeping the skin wet with draining with moisturizing upper hose 71.
And, drain solenoid valve can also be set, be arranged at the bottom of water at low temperature feeder 5, be used for regularly getting rid of the more water of impurity in the water at low temperature feeder 5, guarantee good heat exchange efficiency.Described water at low temperature condensate tank of dehumidifier 72 and switching device can also be other mechanical devices well known in the prior art, electromechanics, surge, pneumatic means.
In addition, Fig. 3 and Fig. 4 illustrate two kinds of position relations of water at low temperature feeder 5 and condensation module respectively: in Fig. 3, water at low temperature feeder 5 is arranged on the bottommost in the housing 1, and condensation module places on the same horizontal plane with evaporation net 2; In Fig. 4, condensation module places the bottommost in the housing 1, and water at low temperature feeder 5 is positioned at the top of condensation module.
Described water evaporative condenser system 100 is in work, sparge pipe 302 provides the higher water of temperature and drenches on evaporation net 2, cooling blower 4 sucks the air in the environment from air inlet 102, pass evaporation net 2 and the water for cooling higher in the process of passing evaporation net 2 to temperature, water after the cooling continues the dirty water at low temperature feeder 5 that enters, and the air themperature of the evaporation net 2 of flowing through raises after cooling blower 4 is discharged cooling device.
Water evaporative condenser system 100 can cool off the heat exchange water from the energy of the water cooling heat exchanger of plate type heat exchanger or other types, utilizes the high-efficiency evaporating of evaporation net 2 to take away heat.Heat exchange water is evenly distributed on honeycomb fashion evaporation net 2 surfaces, form the moisture film of hundreds of times of areas, cooling blower 4 driving air streams skim over cascade and impel water film evaporation, the high-temperature water that water-cooled condenser 504 is come out is reduced to environment wet-bulb temperature for about 32 ℃ rapidly, even lower, can stablize and be controlled at 26 ℃.
According to the compressor pressure-enthalpy chart, 1 ℃ of the every reduction of condensation temperature, compressor 10010 Energy Efficiency Ratio improve about 2.3%, and the input power of compressor 10010 descends about 2%.The condensation temperature of tradition cooling type dehumidifier is generally 54.4 ℃, and the described novel high-energy of this patent is imitated cooling type dehumidifier, under the harshest situation, also condensation temperature can be reduced to 32 ℃, thus, compressor 10010 Energy Efficiency Ratio have improved about 100%, about systematic energy efficiency ratio is doubled.
Novel high-energy of the present invention is imitated cooling type dehumidifier, adopts water evaporative condenser system 100, invest very low, the occupation of land space is very little.Rate of water make-up only is the water yield of evaporative phase-change.Simultaneously by regulating the wind speed of cooling blower 4, can control the water yield of evaporation, and then the water temperature in the control water tank (promptly entering the water temperature in the water-cooled condenser 504), thereby adjusting condensation temperature, therefore under different environment, even under the situation of 35 ℃ of environment dry-bulb temperatures, 34 ℃ of wet-bulb temperature, also condensation temperature can be controlled at (being about absolute pressure 12.55bar) about 32 ℃.Therefore the unit power moisture removal of cooling type dehumidifier generally can reach 4.0L/(hkW) even can reach 4.5L/(hkW) more than, saved operating cost greatly, reduced the compression ratio of compressor simultaneously, improved the service life of unit greatly.This novel high-energy effect cooling type dehumidifier is compared with the common cooling type dehumidifier of same 10L/h moisture removal, the power consumption expense in 1 year is saved 4000 yuans approximately, the water rate that evaporation consumes only is (1 year according to calculating in 2000 hours) about 300 yuans, if in state-owned 200,000 users, then annual about 800,000,000 yuan of the national resources of saving.
Through test, under the sprinkle density of 2300 Kilograms Per Square Meters hour, when intake velocity is 1.5 meter per seconds, (environment dry-bulb temperature: 27 ℃ of wet-bulb temperature: 19.5 ℃) under standard condition, the heat exchange current are behind the evaporation net 2 of 80cmX60cmX10cm, and temperature can drop in 30 ℃ by 45 ℃.
The present invention is by preferred embodiment having carried out detailed explanation.Yet, by to the studying carefully of preamble, to the variation of each embodiment with to increase also be that one of ordinary skill in the art institute is conspicuous.The applicant is intended that all these variations and increases the part that has comprised in the scope that drops on claim of the present invention of the present invention.
Similar numbering refers to similar element in the whole text.For the purpose of clear, has the situation that some line, layer, element, parts or feature are amplified in the accompanying drawings.
Claims (13)
1. a novel high-energy is imitated cooling type dehumidifier, comprise the outdoor main frame of air-conditioning and the indoor set that is communicated with it, it is characterized in that: described outdoor main frame also comprises a water evaporative condenser system, and described water evaporative condenser system comprises a housing and all is arranged at being used in the described housing and absorbs water evaporation module that heat forms the low temperature globule simultaneously, is used to collect the water at low temperature feeder of the low temperature globule that water evaporation module produces and is used for the condensation module of the water at low temperature in the water at low temperature feeder with refrigerant heat exchange formation high-temperature water by the evaporation high-temperature water;
Described water evaporation module, water at low temperature feeder and condensation module are communicated with the circulation of formation water in turn; And,
Described water evaporation module also comprises at least one air inlet, at least one air outlet and at least one cooling blower, and air is sucked by described cooling blower, forms hot blast after the evaporation high-temperature water absorbs heat, and hot blast is discharged by air outlet by described cooling blower.
2. novel high-energy according to claim 1 is imitated cooling type dehumidifier, it is characterized in that:
Described water evaporation module comprises that at least one is arranged at air inlet on the housing, at least one is arranged at air outlet on the housing, at least one cooling blower, at least one evaporates net, at least one sparge pipe and one first water pipe; Each air inlet place disposes an evaporation net, and each evaporation net place disposes a sparge pipe that is used for to evaporation net water spray, and the described sparge pipe of each bar all is connected with described first water pipe; Also comprise the water inlet that is used for water filling in sparge pipe on the described sparge pipe of each bar; Each air outlet place disposes one and is used for air from the air inlet suction and through the described cooling blower of pervaporation net by the air outlet discharge;
Described water at low temperature feeder is positioned at the below of water evaporation module, is used for that water is evaporated the low temperature globule that each evaporation of module drips on the net and collects;
Described condensation module comprises water-cooled condenser and one second water pipe, and described water-cooled condenser comprises separate and adjoins the circulate aquaporin of water of the refrigerant passage and being used to of refrigerant that circulates that is used to of setting; The two ends of described refrigerant passage are respectively by advancing the refrigerant pipe and going out the copper pipe that the refrigerant pipe is connected in the described indoor set and be connected with evaporator fin; One end of described aquaporin connects described water pipe by water pump, and the other end of described aquaporin connects the water at low temperature feeder by second water pipe; And,
It is online that water in each described sparge pipe is sprayed onto corresponding evaporation, stay the low temperature globule on the net in evaporation, the water at low temperature droplet falls and is collected by described water at low temperature feeder, under the effect of described water pump, water at low temperature in the water at low temperature feeder flows in the aquaporin of water-cooled condenser, carry out heat exchange with refrigerant in the condensation channel after, heating up forms high-temperature water, high-temperature water flows to each sparge pipe through the effect of water pump by first water pipe, participates in the water evaporative condenser process of next circulation.
3. novel high-energy according to claim 2 is imitated cooling type dehumidifier, and it is characterized in that: each described sparge pipe is provided with a plurality of holes that are used to spray water.
4. novel high-energy according to claim 2 is imitated cooling type dehumidifier, and it is characterized in that: each described sparge pipe is provided with a plurality of holes that are used to spray water, and each hole disposes a spray equipment.
5. imitate cooling type dehumidifier according to claim 3 or 4 described novel high-energies, it is characterized in that: each described sparge pipe is positioned at the top of corresponding evaporation net, and along the circumferential direction setting that this evaporation is netted, offers a plurality of described holes at the lower wall of each described sparge pipe.
6. novel high-energy according to claim 2 is imitated cooling type dehumidifier, and it is characterized in that: each described sparge pipe is positioned at the oblique upper of corresponding evaporation net, and along the circumferential direction setting that this evaporation is netted, offers a plurality of described holes at the sidewall of each described sparge pipe.
7. novel high-energy according to claim 2 is imitated cooling type dehumidifier, it is characterized in that: described water evaporative condenser system comprises that also at least one is used for the water replanishing device of moisturizing in the water at low temperature feeder, described water replanishing device comprises the moisturizing upper hose that at least one is connected with the water at low temperature feeder, and at least one is used for detecting the water at low temperature condensate tank of dehumidifier of described water at low temperature feeder water at low temperature water level.
8. novel high-energy according to claim 2 is imitated cooling type dehumidifier, and it is characterized in that: described air outlet is obliquely installed on described housing.
9. novel high-energy according to claim 2 is imitated cooling type dehumidifier, it is characterized in that: described evaporation net is an organic filler evaporation net; Described water-cooled condenser is screw shell heat-exhanger, plate type heat exchanger or shell and tube exchanger.
10. novel high-energy according to claim 9 is imitated cooling type dehumidifier, it is characterized in that: described organic filler evaporation net is organic filler honeycomb fashion evaporation net.
11. novel high-energy according to claim 2 is imitated cooling type dehumidifier, it is characterized in that: described evaporation net is an inorganic filler evaporation net; Described water-cooled condenser is screw shell heat-exhanger, plate type heat exchanger or shell and tube exchanger.
12. novel high-energy according to claim 11 is imitated cooling type dehumidifier, it is characterized in that: described inorganic filler evaporation net is inorganic filler honeycomb fashion evaporation net.
13. novel high-energy according to claim 2 is imitated cooling type dehumidifier, it is characterized in that: describedly advance the refrigerant pipe and go out the refrigerant pipe to be copper pipe.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102997346A (en) * | 2012-12-24 | 2013-03-27 | 王涛 | Novel energy-efficient cooling dehumidifier |
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2012
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102997346A (en) * | 2012-12-24 | 2013-03-27 | 王涛 | Novel energy-efficient cooling dehumidifier |
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Effective date of registration: 20160316 Address after: 518000 Shenzhen, Guangming New District, Gongming street, Tong Tong Community Reservoir Road, No. 8 Patentee after: SHENZHEN LIBING ENERGY SAVING TECHNOLOGY CO., LTD. Address before: 3, 1, 550000, 9 West Lake Road, Nanming District, Guizhou, Guiyang, No. 8 Patentee before: Wang Tao |
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