TWI671494B - Dehumidifier - Google Patents

Dehumidifier Download PDF

Info

Publication number
TWI671494B
TWI671494B TW106114252A TW106114252A TWI671494B TW I671494 B TWI671494 B TW I671494B TW 106114252 A TW106114252 A TW 106114252A TW 106114252 A TW106114252 A TW 106114252A TW I671494 B TWI671494 B TW I671494B
Authority
TW
Taiwan
Prior art keywords
air
refrigerant
condenser
condensation
evaporator
Prior art date
Application number
TW106114252A
Other languages
Chinese (zh)
Other versions
TW201825838A (en
Inventor
伊東大輔
前山英明
露木元
Original Assignee
日商三菱電機股份有限公司
日商三菱電機家園機器股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 日商三菱電機股份有限公司, 日商三菱電機家園機器股份有限公司 filed Critical 日商三菱電機股份有限公司
Publication of TW201825838A publication Critical patent/TW201825838A/en
Application granted granted Critical
Publication of TWI671494B publication Critical patent/TWI671494B/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Gases (AREA)

Abstract

除濕裝置(1)包括框體(20)、冷媒迴路(10)以及送風機(6)。凝結器(3)包含:第1凝結部(3a),係過冷卻液狀態之冷媒流動;第2凝結部(3b),係氣液二相狀態之該冷媒流動;以及第3凝結部(3c),係過熱氣體狀態之該冷媒流動。第1隔開部(12)係將第1風路(11a)與第2風路(11b)隔開。第2隔開部(13)具有連接第1區域(22)與第2區域(23)的開口部(13a)。在沿著軸(6a)所延伸的方向從第1區域(22)觀察第2隔開部(13)的開口部(13a)時,風扇(6b)係被配置於該開口部(13a)內。 The dehumidifying device (1) includes a frame body (20), a refrigerant circuit (10), and a blower (6). The condenser (3) includes: a first condenser (3a), a refrigerant flow in a supercooled liquid state; a second condenser (3b), a refrigerant flow in a gas-liquid two-phase state; and a third condenser (3c) ), The refrigerant flows in the superheated gas state. The first partition (12) partitions the first air path (11a) from the second air path (11b). The second partition (13) has an opening (13a) that connects the first region (22) and the second region (23). When the opening (13a) of the second partition (13) is viewed from the first area (22) along the direction in which the shaft (6a) extends, the fan (6b) is arranged in the opening (13a). .

Description

除濕裝置 Dehumidifier

本發明係有關於一種除濕裝置,尤其係有關於一種包括冷媒迴路之除濕裝置。 The present invention relates to a dehumidifying device, and more particularly, to a dehumidifying device including a refrigerant circuit.

在以往之包括冷媒迴路的除濕裝置,並列地配置蒸發器與凝結器。蒸發器係在藉送風機產生空氣的流動位於比凝結器更上游。以往之除濕裝置係在蒸發器將在除濕裝置內所取入之空氣冷卻並除濕,而在凝結器對在蒸發器被冷卻並除濕的空氣加熱。 In the conventional dehumidifier including a refrigerant circuit, an evaporator and a condenser are arranged in parallel. The evaporator is located upstream of the condenser by the flow of air generated by the blower. In the conventional dehumidifier, the air taken in the dehumidifier was cooled and dehumidified in the evaporator, and the condenser cooled the dehumidified air in the evaporator.

作為表示除濕裝置之除濕性能的指標,已知表示每1kWh之除濕量L的EF(Energy Factor)值(L/kWh)。除濕裝置係EF值愈高可愈減少耗電量。作為提高除濕裝置之EF值的方法,想到降低冷媒之凝結溫度,使凝結壓力與蒸發壓力之差變小,藉此,減少壓縮機的負載。 As an index indicating the dehumidification performance of a dehumidification device, an EF (Energy Factor) value (L / kWh) indicating a dehumidification amount L per 1 kWh is known. The higher the EF value of the dehumidifier, the more power consumption can be reduced. As a method for increasing the EF value of the dehumidifier, it is thought to reduce the condensation temperature of the refrigerant so that the difference between the condensation pressure and the evaporation pressure becomes smaller, thereby reducing the load on the compressor.

又,在特開平5-87417號公報(專利文獻1),揭示一種除濕裝置,該除濕裝置係將凝結器的一部分配置於在蒸發器被進行熱交換之空氣的風路,且將凝結器的剩下部分配置於在蒸發器未被進行熱交換之空氣的風路。 Furthermore, in Japanese Patent Application Laid-Open No. 5-87417 (Patent Document 1), a dehumidifying device is disclosed in which a part of a condenser is disposed in an air path of air that is heat-exchanged in an evaporator, and the condenser The remainder is placed in the air path of the air that has not undergone heat exchange in the evaporator.

【先行專利文獻】 [Leading Patent Literature] 【專利文獻】 [Patent Literature]

[專利文獻1]特開平5-87417號公報 [Patent Document 1] Japanese Unexamined Patent Publication No. 5-87417

在以往之除濕裝置,在凝結器過熱氣體狀態之冷媒、氣液二相狀態之冷媒以及過冷卻液狀態之冷媒與在蒸發器被進行熱交換之空氣進行熱交換。因為降低凝結溫度時通過凝結器之空氣的溫度亦降低,所以通過凝結器之空氣的溫度與凝結溫度的差變小。因此,無法充分地降低凝結溫度。因此,難充分地提高EF值。 In conventional dehumidifiers, the refrigerant in the superheated gas state of the condenser, the refrigerant in the gas-liquid two-phase state, and the refrigerant in the supercooled liquid state exchange heat with the air subjected to heat exchange in the evaporator. Because the temperature of the air passing through the condenser decreases as the condensation temperature decreases, the difference between the temperature of the air passing through the condenser and the condensation temperature becomes smaller. Therefore, the coagulation temperature cannot be sufficiently reduced. Therefore, it is difficult to sufficiently increase the EF value.

又,在該公報所記載之除濕裝置,因為在凝結器之冷媒的出口被配置於在蒸發器未被進行熱交換之空氣的風路,所以在凝結器無法充分地得到過冷卻度。結果,在該公報所記載之除濕裝置,因為難得到大的除濕量,所以難充分地提高EF值。 Moreover, in the dehumidifier described in this publication, since the outlet of the refrigerant in the condenser is disposed in the air path of the air that has not been heat-exchanged in the evaporator, the degree of subcooling cannot be sufficiently obtained in the condenser. As a result, it is difficult to sufficiently increase the EF value in the dehumidifier described in this publication because it is difficult to obtain a large amount of dehumidification.

又,在除濕裝置內流動之空氣的通風阻力變大時,因為為了得到所要之除濕量所需之送風機的風量變大,所以送風機的輸入(耗電量)變大。因此,難充分地提高EF值。 In addition, when the ventilation resistance of the air flowing in the dehumidifying device becomes large, the input (power consumption) of the blower increases because the air volume of the blower required to obtain the desired amount of dehumidification increases. Therefore, it is difficult to sufficiently increase the EF value.

本發明係鑑於該課題而開發的,其目的在於提供一種EF值高的除濕裝置。 The present invention was developed in view of this problem, and an object thereof is to provide a dehumidifier having a high EF value.

本發明之除濕裝置包括框體、冷媒迴路以及送風機。冷媒迴路包含在框體之內部所收容的壓縮機、凝結器、降壓裝置以及蒸發器。送風機係具有以軸為中心轉動的風扇,且被收容於框體之該內部。在冷媒迴路,冷媒係在壓縮機、凝結 器、降壓裝置以及蒸發器依序流通。凝結器包含:第1凝結部,係過冷卻液狀態之冷媒流動;第2凝結部,係氣液二相狀態之冷媒流動;以及第3凝結部,係過熱氣體狀態之冷媒流動。框體包含第1隔開部與第2隔開部。第1隔開部係將第1風路與第2風路隔開,而該第1風路係藉由風扇以軸為中心轉動,從框體的外部被取入內部的空氣依序通過蒸發器、第1凝結部以及第2凝結部,該第2風路係藉由風扇以軸為中心轉動,從框體的外部被取入該內部的空氣通過第3凝結部。第2隔開部係具有連接被配置藉第1隔開部所隔開之第1風路及該第2風路的第1區域與被配置送風機之第2區域的開口部,且將第1區域與第2區域隔開。在沿著軸所延伸的方向從第1區域觀察第2隔開部的開口部時,風扇係被配置於開口部內。 The dehumidification device of the present invention includes a frame, a refrigerant circuit, and a blower. The refrigerant circuit includes a compressor, a condenser, a pressure reducing device, and an evaporator housed inside the casing. The blower is a fan that rotates around a shaft and is housed in the interior of the housing. In the refrigerant circuit, the refrigerant flows through the compressor, condenser, pressure reducing device and evaporator in sequence. The condenser includes: a first condensing portion, which is a refrigerant flow in a supercooled liquid state; a second condensing portion, which is a refrigerant flow in a gas-liquid two-phase state; and a third condensing portion, a refrigerant flow in a superheated gas state. The frame includes a first partition and a second partition. The first partitioning section partitions the first air path from the second air path, and the first air path is rotated by the fan around the shaft, and the air taken in from the outside of the casing sequentially passes through the evaporation. Device, the first condensation part, and the second condensation part, the second air path is rotated by the fan around the shaft, and the air taken in from the outside of the casing passes through the third condensation part. The second partition section has an opening that connects the first air path partitioned by the first partition section, the first region of the second air path, and the second region of the blower, and connects the first The area is separated from the second area. When the opening portion of the second partition portion is viewed from the first region along the direction in which the shaft extends, the fan system is disposed in the opening portion.

若依據本發明之除濕裝置,可提供一種EF值高的除濕裝置。 According to the dehumidifier according to the present invention, a dehumidifier having a high EF value can be provided.

1‧‧‧除濕裝置 1‧‧‧ Dehumidifier

2‧‧‧壓縮機 2‧‧‧compressor

3‧‧‧凝結器 3‧‧‧ Condenser

3a‧‧‧第1凝結部 3a‧‧‧The first condensation part

3b‧‧‧第2凝結部 3b‧‧‧ 2nd condensation unit

3c‧‧‧第3凝結部 3c‧‧‧3rd condensation unit

4‧‧‧降壓裝置 4‧‧‧ Buck device

5‧‧‧蒸發器 5‧‧‧Evaporator

6‧‧‧送風機 6‧‧‧ blower

6a‧‧‧軸 6a‧‧‧axis

6b‧‧‧風扇 6b‧‧‧fan

10‧‧‧冷媒迴路 10‧‧‧Refrigerant circuit

11a‧‧‧第1風路 11a‧‧‧The first wind road

11b‧‧‧第2風路 11b‧‧‧Second Wind Road

12‧‧‧第1隔開部 12‧‧‧ the first partition

13‧‧‧第2隔開部 13‧‧‧ 2nd Division

13a‧‧‧開口部 13a‧‧‧ opening

14a‧‧‧第1吸入口 14a‧‧‧1st suction port

14b‧‧‧第2吸入口 14b‧‧‧Second suction port

15‧‧‧第3吸入口 15‧‧‧3rd suction port

16‧‧‧第3隔開部 16‧‧‧ the third partition

17‧‧‧高低壓熱交換部 17‧‧‧High and low pressure heat exchange department

20‧‧‧框體 20‧‧‧Frame

20a‧‧‧背面 20a‧‧‧Back

20b‧‧‧前面 20b‧‧‧front

20c‧‧‧側面 20c‧‧‧side

21‧‧‧吹出口 21‧‧‧ blowing outlet

22‧‧‧第1區域 22‧‧‧Area 1

23‧‧‧第2區域 23‧‧‧ Zone 2

第1圖係本發明之第1實施形態之除濕裝置的冷媒迴路圖。 Fig. 1 is a refrigerant circuit diagram of a dehumidifier according to a first embodiment of the present invention.

第2圖係表示本發明之第1、第2以及第5實施形態的除濕裝置之構成的示意圖。 Fig. 2 is a schematic diagram showing the structure of a dehumidifier according to the first, second, and fifth embodiments of the present invention.

第3圖係表示本發明之第1實施形態的風扇與第2隔開部之位置關係的圖。 Fig. 3 is a diagram showing a positional relationship between a fan and a second partition portion according to the first embodiment of the present invention.

第4圖係表示本發明之第1實施形態的凝結器之冷媒及空 氣之溫度變化的圖形。 Fig. 4 is a graph showing changes in the temperature of the refrigerant and air in the condenser of the first embodiment of the present invention.

第5圖係本發明之第1實施形態的比較例之除濕裝置的冷媒迴路圖。 Fig. 5 is a refrigerant circuit diagram of a dehumidifier according to a comparative example of the first embodiment of the present invention.

第6圖係表示本發明之第1實施形態的比較例之凝結器的冷媒及空氣之溫度變化的圖形。 Fig. 6 is a graph showing changes in temperature of a refrigerant and air in a condenser of a comparative example of the first embodiment of the present invention.

第7圖係本發明之第1實施形態的第1變形例之除濕裝置的冷媒迴路圖。 Fig. 7 is a refrigerant circuit diagram of a dehumidifier according to a first modification of the first embodiment of the present invention.

第8圖係表示本發明之第1實施形態的第2變形之除濕裝置之構成的示意圖。 Fig. 8 is a schematic diagram showing the structure of a dehumidifier according to a second modification of the first embodiment of the present invention.

第9圖係表示本發明之第1實施形態的第2變形例之風扇、第2隔開部以及凝結器之位置關係的圖。 Fig. 9 is a diagram showing a positional relationship between a fan, a second partition, and a condenser in a second modification of the first embodiment of the present invention.

第10圖係表示本發明之第1實施形態的第3變形例之風扇、第2隔開部以及凝結器之位置關係的圖。 Fig. 10 is a diagram showing the positional relationship among a fan, a second partition, and a condenser according to a third modification of the first embodiment of the present invention.

第11圖係表示本發明之第2實施形態的凝結器與蒸發器之在凝結器的高度方向之位置關係的圖。 Fig. 11 is a diagram showing the positional relationship between the condenser and the evaporator in the height direction of the condenser according to the second embodiment of the present invention.

第12圖係表示本發明之第2實施形態的凝結器與蒸發器之在凝結器的寬度方向之位置關係的圖。 Fig. 12 is a diagram showing the positional relationship between the condenser and the evaporator in the width direction of the condenser according to the second embodiment of the present invention.

第13圖係表示本發明之第3實施形態的除濕裝置之構成的示意圖。 Fig. 13 is a schematic diagram showing the structure of a dehumidifier according to a third embodiment of the present invention.

第14圖係表示本發明之第4實施形態的除濕裝置之構成的示意圖。 Fig. 14 is a schematic diagram showing the structure of a dehumidifier according to a fourth embodiment of the present invention.

第15圖係表示本發明之第4實施形態的除濕裝置之構成的示意立體圖。 Fig. 15 is a schematic perspective view showing the structure of a dehumidifier according to a fourth embodiment of the present invention.

第16圖係表示本發明之第4實施形態的變形例之除濕裝 置之構成的示意圖。 Fig. 16 is a schematic diagram showing the structure of a dehumidifier according to a modification of the fourth embodiment of the present invention.

第17圖係表示本發明之第6實施形態的凝結器之構成的示意圖。 Fig. 17 is a schematic diagram showing the configuration of a condenser according to a sixth embodiment of the present invention.

第18圖係表示本發明之第6實施形態的凝結器之別的構成的示意圖。 Fig. 18 is a schematic diagram showing another configuration of a condenser according to a sixth embodiment of the present invention.

第19圖係表示本發明之第7實施形態的除濕裝置之構成的示意圖。 Fig. 19 is a schematic diagram showing the structure of a dehumidifier according to a seventh embodiment of the present invention.

第20圖係本發明之第8實施形態之除濕裝置的冷媒迴路圖。 Fig. 20 is a refrigerant circuit diagram of a dehumidifier according to an eighth embodiment of the present invention.

以下,參照圖面,說明本發明之實施形態。在以下的圖面,對相同或相當之部分附加相同的參照編號,其說明係不重複。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. In the following drawings, the same or corresponding parts are denoted by the same reference numerals, and descriptions thereof are not repeated.

第1實施形態 First Embodiment

參照第1圖及第2圖,第1實施形態之除濕裝置1包括:冷媒迴路10,係包含壓縮機2、凝結器3、降壓裝置4以及蒸發器5;送風機6;以及框體20,係將冷媒迴路10與送風機6收容於內部。凝結器3及蒸發器5係進行冷媒與空氣間的熱交換之熱交換器。各個凝結器3及蒸發器5係具有冷媒之入口與出口、及空氣之入口與出口。框體20係除濕裝置1面向作為除濕對象之外部空氣(室內空間)。 1 and 2, the dehumidifier 1 according to the first embodiment includes a refrigerant circuit 10 including a compressor 2, a condenser 3, a pressure reducing device 4, and an evaporator 5; a blower 6; and a frame 20, The refrigerant circuit 10 and the blower 6 are housed inside. The condenser 3 and the evaporator 5 are heat exchangers that perform heat exchange between the refrigerant and the air. Each of the condenser 3 and the evaporator 5 has an inlet and an outlet of a refrigerant, and an inlet and an outlet of air. The housing 20 is a dehumidifier 1 that faces external air (indoor space) as a dehumidification target.

除濕裝置1的冷媒迴路10係被收容於框體20的內部,並構成冷凍循環。冷媒迴路10係藉由以配管依序連接壓縮機2、凝結器3、降壓裝置4以及蒸發器5所構成。如第2圖中以箭號所示,在冷媒迴路10,冷媒係依序在壓縮機2、凝結器3、降壓裝置4以及蒸發器5流通。 The refrigerant circuit 10 of the dehumidifier 1 is housed inside the housing 20 and constitutes a refrigeration cycle. The refrigerant circuit 10 is configured by connecting the compressor 2, the condenser 3, the pressure reducing device 4, and the evaporator 5 in order by piping. As shown by an arrow in FIG. 2, in the refrigerant circuit 10, the refrigerant system flows through the compressor 2, the condenser 3, the pressure reducing device 4, and the evaporator 5 in this order.

壓縮機2係吸入低壓冷媒並壓縮後,作為高壓冷媒排出。壓縮機2係冷媒之排出容量可變之例如變頻器壓縮機。除濕裝置1內之冷媒循環量係藉由調整壓縮機2之排出容量所控制。壓縮機2具有排出口及吸入口。 Compressor 2 sucks in low-pressure refrigerant, compresses it, and discharges it as high-pressure refrigerant. The compressor 2 is, for example, an inverter compressor with a variable discharge capacity of the refrigerant. The amount of refrigerant circulation in the dehumidifier 1 is controlled by adjusting the discharge capacity of the compressor 2. The compressor 2 has a discharge port and a suction port.

凝結器3係使藉壓縮機2所升壓之冷媒凝結並冷卻。凝結器3包含:第1凝結部3a,係過冷卻液狀態之冷媒流動;第2凝結部3b,係氣液二相狀態之冷媒流動;以及第3凝結部3c,係過熱氣體狀態之冷媒流動。第1凝結部3a係只要具有過冷卻液狀態之冷媒所流動的區域即可,亦可具有過冷卻液狀態及氣液二相狀態之冷媒所流動的區域。第3凝結部3c係只要具有過熱氣體狀態之冷媒所流動的區域即可,亦可具有過熱氣體狀態及氣液二相狀態之冷媒所流動的區域。在凝結器3,冷媒係依序在第3凝結部3c、第2凝結部3b以及第1凝結部3a流動。 The condenser 3 condenses and cools the refrigerant pressurized by the compressor 2. Condenser 3 includes: a first condensing portion 3a, which is a refrigerant flow in a supercooled liquid state; a second condensing portion 3b, which is a refrigerant flow in a gas-liquid two-phase state; and a third condensing portion 3c, a refrigerant flow in a superheated gas state . The first condensing portion 3a only needs to have a region through which the refrigerant in the supercooled liquid state flows, and may also have a region through which the refrigerant in the supercooled liquid state and the gas-liquid two-phase state flows. The third condensing portion 3c only needs to have a region through which the refrigerant in a superheated gas state flows, and may also have a region through which the refrigerant in a superheated gas state and a gas-liquid two-phase state flows. In the condenser 3, the refrigerant system flows in sequence through the third condensation part 3c, the second condensation part 3b, and the first condensation part 3a.

各個第1凝結部3a、第2凝結部3b以及第3凝結部3c具有冷媒入口及冷媒出口。第3凝結部3c之冷媒入口係與壓縮機2之排出口連接。第2凝結部3b之冷媒入口係與第3凝結部3c之冷媒出口連接。第1凝結部3a之冷媒入口係與第2凝結部3b之冷媒出口連接。 Each of the first condensation part 3a, the second condensation part 3b, and the third condensation part 3c has a refrigerant inlet and a refrigerant outlet. The refrigerant inlet of the third condensing portion 3c is connected to the discharge outlet of the compressor 2. The refrigerant inlet of the second condensation part 3b is connected to the refrigerant outlet of the third condensation part 3c. The refrigerant inlet of the first condensation part 3a is connected to the refrigerant outlet of the second condensation part 3b.

亦可第1凝結部3a、第2凝結部3b以及第3凝結部3c係單列或複數列地構成。在本實施形態,第1凝結部3a、第2凝結部3b以及第3凝結部3c係經由配管彼此分離。此外,亦可第1凝結部3a、第2凝結部3b以及第3凝結部3c係一體地構成。 The first condensing portion 3a, the second condensing portion 3b, and the third condensing portion 3c may be configured in a single row or a plurality of rows. In this embodiment, the first coagulation part 3a, the second coagulation part 3b, and the third coagulation part 3c are separated from each other via a pipe. In addition, the first coagulation part 3a, the second coagulation part 3b, and the third coagulation part 3c may be integrally formed.

降壓裝置4係使在凝結器3所冷卻之冷媒降壓並膨脹。降壓裝置4係例如是膨脹閥。亦可此膨脹閥是電子式膨脹閥。此外,降壓裝置4係不限定為膨脹閥,例如亦可是毛細管。降壓裝置4具有冷媒入口及冷媒出口。降壓裝置4之冷媒入口係與第3凝結部3c之冷媒出口連接。 The pressure reducing device 4 depressurizes and expands the refrigerant cooled in the condenser 3. The pressure reducing device 4 is, for example, an expansion valve. This expansion valve may be an electronic expansion valve. The pressure reducing device 4 is not limited to an expansion valve, and may be, for example, a capillary tube. The pressure reducing device 4 has a refrigerant inlet and a refrigerant outlet. The refrigerant inlet of the pressure reducing device 4 is connected to the refrigerant outlet of the third condensing section 3c.

蒸發器5係使在降壓裝置4所膨脹之冷媒吸熱而使冷媒蒸發。蒸發器5具有冷媒入口及冷媒出口。蒸發器5之冷媒入口係與降壓裝置4之冷媒出口連接。蒸發器5之冷媒出口係與壓縮機2之吸入口連接。蒸發器5係與第1凝結部3a並列地配置。蒸發器5係在藉送風機6所產生之空氣的流動位於比凝結器3更上游。 The evaporator 5 absorbs heat from the refrigerant expanded in the pressure reducing device 4 to evaporate the refrigerant. The evaporator 5 has a refrigerant inlet and a refrigerant outlet. The refrigerant inlet of the evaporator 5 is connected to the refrigerant outlet of the pressure reducing device 4. The refrigerant outlet of the evaporator 5 is connected to the suction inlet of the compressor 2. The evaporator 5 is arranged in parallel with the first condensing portion 3a. The evaporator 5 is located upstream of the condenser 3 in the flow of air generated by the fan 6.

送風機6係被收容於框體20的內部。送風機6構成為將框體20之外部的空氣取入內部並可送風至凝結器3及蒸發器5。在本實施形態,送風機6具有以軸6a為中心轉動的風扇6b。藉由風扇6b以軸6a為中心轉動,如圖中以箭號A及箭號C所示從室內所取入之空氣在通過凝結器3及蒸發器5後,如圖中以箭號B所示再向室內被排出。在本實施形態,送風機6係在藉送風機6所產生之空氣的流動位於比凝結器3更下游。此外,送風機6係在藉送風機6所產生之空氣的流動,亦可被配置於凝結器3與蒸發器5之間,亦可被配置於比蒸發器5更上游。亦可送風機6係例如是一台。 The blower 6 is housed inside the housing 20. The blower 6 is configured to take in the air from the outside of the housing 20 into the inside and to send the air to the condenser 3 and the evaporator 5. In the present embodiment, the blower 6 includes a fan 6b that rotates around the shaft 6a. The fan 6b rotates around the axis 6a. As shown by arrows A and C in the figure, the air taken in from the room passes through the condenser 3 and the evaporator 5 and is shown by the arrow B in the figure. It is then discharged indoors. In the present embodiment, the blower 6 is such that the flow of air generated by the blower 6 is located further downstream than the condenser 3. In addition, the air blower 6 is based on the flow of air generated by the air blower 6, and may be disposed between the condenser 3 and the evaporator 5, or may be disposed further upstream than the evaporator 5. The blower 6 series may be one, for example.

框體20含有將第1風路11a與第2風路11b隔開的第1隔開部12。各個第1風路11a及第2風路11b係藉框體20及第1隔開部12所規定。即,在框體20的內部,被設置第1風路11a與第2風路11b之2條風路(空氣之流路)。在第1風路11a內,被配置第1凝結部3a、第2凝結部3b以及蒸發器5。在第1風路11a,如圖中以箭號A所示,藉由風扇6b以軸6a為中心轉動,從框體20的外部被取入內部的空氣依序通過蒸發器5、第1凝結部3a、第2凝結部3b。在第2風路11b內,被配置第3凝結部3c。在第2風路11b,如圖中以箭號C所示,藉由風扇6b以軸6a為中心轉動,從框體20的外部被取入內部的空氣通過第3凝結部3c。如圖中以箭號A及箭號C所示,第1風路11a內之空氣的流通方向與第2風路11b內之空氣的流通方向並行。 The housing 20 includes a first partition 12 that partitions the first air path 11a and the second air path 11b. Each of the first air path 11 a and the second air path 11 b is defined by the frame body 20 and the first partition 12. That is, two air paths (air flow paths) of the first air path 11a and the second air path 11b are provided inside the housing 20. In the first air passage 11a, a first condensation part 3a, a second condensation part 3b, and an evaporator 5 are arranged. In the first air path 11a, as shown by arrow A in the figure, the fan 6b rotates around the shaft 6a as the center, and the air taken in from the outside of the casing 20 passes through the evaporator 5 and the first condensation in order. Part 3a and the second condensation part 3b. A third condensation portion 3c is arranged in the second air path 11b. In the second air path 11b, as shown by an arrow C in the figure, the fan 6b rotates around the shaft 6a as the center, and the air taken in from the outside of the housing 20 passes through the third condensation part 3c. As shown by arrows A and C in the figure, the flow direction of the air in the first air path 11a is parallel to the flow direction of the air in the second air path 11b.

此外,規定第1風路11a之空間係不必與規定第2風路11b之空間完全地被分離。在本實施形態,規定第1風路11a之空間係在第1風路11a內之空氣的流通方向在比第2凝結部3b更下游,與規定第2風路11b之空間連接。 The space defining the first air passage 11a need not be completely separated from the space defining the second air passage 11b. In the present embodiment, the space of the first air passage 11a is defined as the air flow direction in the first air passage 11a is downstream of the second condensing portion 3b, and is connected to the space of the second air passage 11b.

在第1風路11a內之空氣的流通方向。位於第1隔開部12之上游側的一端(上游端部)係被配置於比蒸發器5的空氣出口更上游側。在第2風路11b內之空氣的流通方向,位於第1隔開部12之下游側的另一端(下游端部)係被配置於與第1凝結部3a之空氣出口相同的位置或比空氣出口更上游側。第1隔開部12係形成為例如平板形。第1隔開部12係被固定於框體20的內部。 The direction of air flow in the first air path 11a. One end (upstream end portion) located on the upstream side of the first partition portion 12 is disposed more upstream than the air outlet of the evaporator 5. In the air flow direction in the second air path 11b, the other end (downstream end) located on the downstream side of the first partition section 12 is disposed at the same position as or more than the air outlet of the first condensation section 3a. The exit is further upstream. The first partition 12 is formed in a flat plate shape, for example. The first partition 12 is fixed to the inside of the housing 20.

在框體20,形成:第1吸入口14a與第2吸入口 14b(吸入口14),係用以從作為除濕對象之外部空間(室內空間)將空氣吸入框體20的內部;及吹出口21,係用以從內部將空氣吹出至該外部空間。框體20具有背面20a與前面20b。第1吸入口14a及第2吸入口14b被設置於背面20a。在背面20a,第1吸入口14a構成為將空氣吸入第1風路11a。在背面20a,第2吸入口14b構成為將空氣吸入第2風路11b。 In the housing 20, a first suction port 14a and a second suction port are formed. 14b (suction port 14) is used to suck air into the inside of the housing 20 from an external space (indoor space) as a dehumidification target; and an air outlet 21 is used to blow air into the external space from the inside. The housing 20 includes a back surface 20a and a front surface 20b. The first suction port 14a and the second suction port 14b are provided on the back surface 20a. On the back surface 20a, the first suction port 14a is configured to suck air into the first air passage 11a. On the back surface 20a, the second suction port 14b is configured to suck air into the second air path 11b.

第1吸入口14a係在第1風路11a內之空氣的流通方向,被配置於比第1風路11a內之蒸發器5的空氣入口更上游側。第2吸入口14b係在第2風路11b內之空氣的流通方向,被配置於比第2風路11b內之第3凝結部3c的空氣入口更上游側。 The first suction port 14a is a flow direction of the air in the first air path 11a, and is disposed more upstream than the air inlet of the evaporator 5 in the first air path 11a. The second suction port 14b is a direction in which the air flows in the second air path 11b, and is disposed more upstream than the air inlet of the third condensation part 3c in the second air path 11b.

此外,在除濕裝置1,亦可在第1風路11a內,除了被配置於第2風路11b內之第2凝結部3b、第3凝結部3c以及蒸發器5以外,還被配置構成冷媒迴路之任意的構件。例如,亦可將降壓裝置4配置於第1風路11a內。 In addition, in the dehumidifier 1, the first air path 11a may be arranged to constitute a refrigerant in addition to the second condensation part 3b, the third condensation part 3c, and the evaporator 5 disposed in the second air path 11b. Any component of the circuit. For example, the pressure reducing device 4 may be arranged in the first air passage 11a.

又,框體20含有將第1區域22與第2區域23隔開的第2隔開部13。各個第1區域22及第2區域23係藉框體20及第2隔開部13所規定。即,在框體20的內部。被設置第1區域22與第2區域23之2個區域。在第1區域22內,被配置藉第1隔開部12所隔開的第1風路11a及第2風路11b。即,在第1區域22內,被配置在第1風路11a內所配置之第1凝結部3a、第2凝結部3b以及蒸發器5。又,在第1區域22內,被配置在第2風路11b內所配置之第3凝結部3c。送風機6被配置於第2區域23。The housing 20 includes a second partition portion 13 that partitions the first region 22 and the second region 23. Each of the first region 22 and the second region 23 is defined by the frame 20 and the second partition 13. That is, it is inside the housing 20. Two areas, a first area 22 and a second area 23, are provided. In the first area 22, a first air path 11a and a second air path 11b partitioned by the first partition 12 are arranged. That is, in the first region 22, the first condensation portion 3a, the second condensation portion 3b, and the evaporator 5 are disposed in the first air passage 11a. Further, in the first region 22, a third condensation portion 3c arranged in the second air passage 11b is arranged. The blower 6 is arranged in the second area 23.

參照第2圖及第3圖,第2隔開部13具有連接第1區域22與第2區域23的開口部13a。第2隔開部13係形成為例如平板形。在沿著送風機6之軸6a所延伸的方向從第1區域22觀察第2隔開部13的開口部13a時,風扇6b係被配置於開口部13a內。風扇6b的外徑D1係比開口部13a的內徑D2更小。第2隔開部13構成為不封閉風扇6b的吸入面積。又,將第2隔開部13的高度調整成從第1區域22流至第2區域23的空氣通過第3凝結部3c的上端。因此,因為至第3凝結部3c的上端進行熱交換,所以不會阻礙第3凝結部3c的熱交換。 2 and 3, the 2nd partition part 13 has the opening part 13a which connects the 1st area 22 and the 2nd area 23. The second partition 13 is formed in a flat plate shape, for example. When the opening portion 13a of the second partition portion 13 is viewed from the first region 22 along the direction in which the axis 6a of the blower 6 extends, the fan 6b is disposed inside the opening portion 13a. The outer diameter D1 of the fan 6b is smaller than the inner diameter D2 of the opening portion 13a. The second partition portion 13 is configured not to close the suction area of the fan 6b. In addition, the height of the second partition portion 13 is adjusted so that air flowing from the first region 22 to the second region 23 passes through the upper end of the third condensation portion 3c. Therefore, since heat exchange is performed to the upper end of the third condensation part 3c, heat exchange of the third condensation part 3c is not hindered.

其次,參照第1圖、第2圖以及第4圖,說明除濕裝置1之除濕運轉時的動作。第4圖係表示在除濕裝置1的凝結器3之冷媒與空氣之溫度變化的圖形。第4圖之縱軸表示冷媒及空氣的溫度,橫軸表示冷媒及空氣之流路的位置。第4圖中之圓形係表示冷媒,三角形係表示空氣。第4圖之符號c~f、x2、y2係對應於第1圖之相同之符號的位置。符號c表示第1凝結部3a之空氣入口。符號d表示第2凝結部3b之空氣入口(第1凝結部3a之空氣出口)。符號e表示第2凝結部3b之空氣出口。符號f表示第3凝結部3c之空氣入口。符號g表示第3凝結部3c之空氣出口。符號x2表示凝結器3之冷媒入口。符號y2表示凝結器3之冷媒出口。 Next, the operation during the dehumidifying operation of the dehumidifying device 1 will be described with reference to FIGS. 1, 2 and 4. FIG. 4 is a graph showing changes in the temperature of the refrigerant and air in the condenser 3 of the dehumidifier 1. The vertical axis of FIG. 4 indicates the temperature of the refrigerant and the air, and the horizontal axis indicates the position of the flow path of the refrigerant and the air. The circle in FIG. 4 indicates the refrigerant, and the triangle indicates air. Symbols c to f, x2, and y2 in FIG. 4 correspond to positions of the same symbols in FIG. 1. The symbol c indicates an air inlet of the first condensation portion 3a. The symbol d indicates the air inlet of the second condensation portion 3b (the air outlet of the first condensation portion 3a). The symbol e indicates an air outlet of the second condensation portion 3b. The symbol f indicates the air inlet of the third condensation part 3c. The symbol g indicates an air outlet of the third condensation portion 3c. The symbol x2 indicates the refrigerant inlet of the condenser 3. The symbol y2 indicates a refrigerant outlet of the condenser 3.

從壓縮機2所排出之過熱氣體狀態的冷媒係流入被配置於第2風路11b內的第3凝結部3c。流入第3凝結部3c之溫度T1之過熱氣體狀態的冷媒係藉由與經由第2吸入口14b從外部空間被取入第1風路11a內之溫度T6的空氣進行熱交換而被冷卻,成為凝結溫度T2(在第4圖係39℃)之氣液二相狀態的冷媒。凝結溫度T2係溫度T6以上。 The refrigerant in the superheated gas state discharged from the compressor 2 flows into the third condensing portion 3c arranged in the second air passage 11b. The refrigerant in the superheated gas state at temperature T1 flowing into the third condensing portion 3c is cooled by heat exchange with air having temperature T6 taken into the first air passage 11a from the external space through the second suction port 14b, and becomes Refrigerant in a gas-liquid two-phase state with a condensation temperature T2 (39 ° C in Fig. 4). The coagulation temperature T2 is higher than the temperature T6.

另一方面,第2風路11b內所取入之溫度T6的空氣係藉由在第3凝結部3c與超過溫度T2且溫度T1以下之過熱氣體狀態的冷媒進行熱交換而被加熱。藉此,已通過第2風路11b之第3凝結部3c之空氣的溫度T7(在第4圖係50℃)係可變成該冷媒之凝結溫度T2以上。 On the other hand, the air taken in at the temperature T6 in the second air passage 11b is heated by heat exchange between the third condensing portion 3c and a refrigerant in a superheated gas state exceeding the temperature T2 and below the temperature T1. As a result, the temperature T7 (50 ° C. in FIG. 4) of the air that has passed through the third condensing portion 3c of the second air path 11 b can be equal to or higher than the condensation temperature T2 of the refrigerant.

從第3凝結部3c所流出之溫度T2之氣液二相狀態的冷媒流入被配置於第1風路11a內的第2凝結部3b。流入第2凝結部3b之溫度T2之氣液二相狀態的冷媒係與已通過第1凝結部3a之溫度T8的空氣進行熱交換。從第2凝結部3b所流出之氣液二相狀態的冷媒流入被配置於第1風路11a內的第1凝結部3a。流入第1凝結部3a的冷媒係藉由與在第1風路11a內已通過蒸發器5之溫度T4的空氣進行熱交換,而更被冷卻,成為溫度T3之過冷卻液狀態的冷媒。從第1凝結部3a所流出之過冷卻液狀態的冷媒係藉由通過降壓裝置4而被降壓,成為氣液二相狀態的冷媒後,流入被配置於第1風路11a內的蒸發器5。流入蒸發器5之氣液二相狀態的冷媒係與經由第1吸入口14a從外部空間被取入第1風路11a內的空氣進行熱交換而被加熱,成為過熱氣體狀態的冷媒。 The refrigerant in a gas-liquid two-phase state at a temperature T2 flowing from the third condensation portion 3c flows into the second condensation portion 3b disposed in the first air passage 11a. The refrigerant flowing into the gas-liquid two-phase state at the temperature T2 of the second condensation section 3b exchanges heat with the air having passed through the temperature T8 of the first condensation section 3a. The gas-liquid two-phase refrigerant flowing out from the second condensation portion 3b flows into the first condensation portion 3a arranged in the first air passage 11a. The refrigerant flowing into the first condensing portion 3a is cooled by heat exchange with the air that has passed through the temperature T4 of the evaporator 5 in the first air path 11a, and becomes a refrigerant in a supercooled liquid state at temperature T3. The refrigerant in the supercooled liquid state flowing from the first condensing portion 3a is depressurized by the pressure reducing device 4 to become a refrigerant in a gas-liquid two-phase state, and then flows into the evaporation disposed in the first air path 11a.器 5。 5. The refrigerant in the gas-liquid two-phase state flowing into the evaporator 5 exchanges heat with the air taken into the first air passage 11a from the external space through the first suction port 14a, and is heated to become a refrigerant in a superheated gas state.

另一方面,第1風路11a內所取入之空氣係首先,藉由在蒸發器5被冷卻至空氣之露點以下的溫度T4而被除濕。被冷卻並除濕之空氣係藉由在第1凝結部3a與過冷卻液狀態之冷媒進行熱交換,被加熱至溫度T8。在第1凝結部3a 與過冷卻液狀態的冷媒進行熱交換之溫度T8的空氣係藉由在第2凝結部3b與氣液二相狀態的冷媒進行熱交換,被加熱至溫度T5。 On the other hand, the air taken in the first air path 11a is first dehumidified by the temperature T4 at which the evaporator 5 is cooled below the dew point of the air. The cooled and dehumidified air is heated to a temperature T8 by exchanging heat with a refrigerant in a supercooled liquid state at the first condensation portion 3a. In the first condensation part 3a The air at a temperature T8 that performs heat exchange with the refrigerant in the supercooled liquid state is heated to the temperature T5 by performing heat exchange with the refrigerant in the gas-liquid two-phase state at the second condensation portion 3b.

藉此,已通過第1風路11a之空氣的溫度T5係超過空氣之露點,可變成該冷媒之凝結溫度以下。溫度T5及溫度T7係被設定成外部空間的氣溫不會因已通過第1風路11a之空氣及已通過第2風路11b之空氣而降低。 As a result, the temperature T5 of the air that has passed through the first air path 11a exceeds the dew point of the air, and may become lower than the condensation temperature of the refrigerant. The temperatures T5 and T7 are set such that the temperature of the external space is not lowered by the air that has passed through the first air path 11a and the air that has passed through the second air path 11b.

其次,在與比較例對比下,說明本實施形態之除濕裝置1的作用效果。 Next, the operation and effect of the dehumidifier 1 according to this embodiment will be described in comparison with a comparative example.

參照第5圖,比較例之除濕裝置1包括:冷媒迴路10,係冷媒在壓縮機2、凝結器3、降壓裝置4以及蒸發器5依序流通;及框體,係將冷媒迴路10收容於內部。在比較例之除濕裝置1,僅形成其內部所取入之空氣依序通過蒸發器5與凝結器3之風路。第6圖係比較例的除濕裝置1之在凝結器3的冷媒與空氣之溫度變化的圖形。第6圖之縱軸表示冷媒及空氣的溫度,橫軸表示冷媒及空氣之流路的位置。第6圖中之圓形係表示冷媒,三角形係表示空氣。第6圖之符號a、b、x1、y1係對應於第5圖之相同之符號的位置。符號a表示凝結器3之空氣入口。符號b表示凝結器3之空氣出口。符號x1表示凝結器3之冷媒入口。符號y1表示凝結器3之冷媒出口。 Referring to FIG. 5, the dehumidifying device 1 of the comparative example includes a refrigerant circuit 10 that circulates the refrigerant in the compressor 2, the condenser 3, the pressure reducing device 4, and the evaporator 5 in sequence; and a housing that houses the refrigerant circuit 10. Inside. In the dehumidifying device 1 of the comparative example, only the air taken in the inside thereof passes through the air path of the evaporator 5 and the condenser 3 in this order. FIG. 6 is a graph of temperature changes of the refrigerant and air in the condenser 3 of the dehumidifier 1 of the comparative example. The vertical axis of FIG. 6 indicates the temperature of the refrigerant and the air, and the horizontal axis indicates the position of the flow path of the refrigerant and the air. The circle in FIG. 6 indicates the refrigerant, and the triangle indicates air. The symbols a, b, x1, and y1 in FIG. 6 correspond to the positions of the same symbols in FIG. 5. The symbol a indicates the air inlet of the condenser 3. The symbol b indicates an air outlet of the condenser 3. The symbol x1 indicates the refrigerant inlet of the condenser 3. The symbol y1 indicates a refrigerant outlet of the condenser 3.

參照第5圖及第6圖,在比較例之除濕裝置1,從壓縮機2所排出之過熱氣體狀態的冷媒係流入凝結器3。流入凝結器3之溫度T1之過熱氣體狀態的冷媒係藉由與在從外部空間被取入除濕裝置1並通過蒸發器5時被冷卻之溫度T12的 空氣進行熱交換而被冷卻。冷媒係成為凝結溫度T10(在第6圖係44℃)之氣液二相狀態,進而被冷卻,成為溫度T11之過冷卻液狀態。凝結溫度T10及溫度T11係溫度T12以上。 Referring to FIGS. 5 and 6, in the dehumidifier 1 of the comparative example, the refrigerant in the superheated gas state discharged from the compressor 2 flows into the condenser 3. The refrigerant in the superheated gas state at the temperature T1 flowing into the condenser 3 is compared with the temperature T12 which is cooled when taken into the dehumidifier 1 from the external space and passed through the evaporator 5 The air is cooled by heat exchange. The refrigerant system is in a gas-liquid two-phase state at a condensation temperature T10 (44 ° C in FIG. 6), and is further cooled to a supercooled liquid state at a temperature T11. The coagulation temperature T10 and the temperature T11 are above the temperature T12.

另一方面,溫度T12的空氣係藉由在凝結器3與超過溫度T10且溫度T1以下之過熱氣體狀態的冷媒、溫度T10之氣液二相狀態的冷媒、或溫度T11之過冷卻液狀態的冷媒進行熱交換而被加熱。具體而言,溫度T12的空氣係藉由在凝結器3與溫度T11之過冷卻液狀態的冷媒或溫度T10之氣液二相狀態的冷媒進行熱交換,被加熱至溫度T20,進而,藉由在凝結器3與超過溫度T10且溫度T1以下之過熱氣體狀態的冷媒進行熱交換,被加熱至溫度T13。藉此,依序通過蒸發器5及凝結器3之空氣的溫度T13係可變成該冷媒之凝結溫度T10以上。溫度T13係被設定成與除濕裝置1之外部空間的氣溫同程度。因此,在比較例之除濕裝置1,使冷媒之凝結溫度T10降低時,通過凝結器3之空氣的溫度T13亦降低。在比較例之除濕裝置1,凝結溫度T10、和凝結溫度T10之位於氣液二相狀態的冷媒進行熱交換之空氣之溫度的最高值T20之差變小。因此,在比較例之除濕裝置1,因為無法使凝結溫度T10充分地降低,所以難提高EF值。 On the other hand, the air at the temperature T12 passes through the condenser 3 and the refrigerant in a superheated gas state exceeding the temperature T10 and below the temperature T1, the gas-liquid two-phase refrigerant in the temperature T10, or the supercooled liquid in the temperature T11. The refrigerant is heated by heat exchange. Specifically, the air at the temperature T12 is heated to the temperature T20 by heat exchange between the condenser 3 and the refrigerant in the supercooled liquid state at the temperature T11 or the refrigerant in the gas-liquid two-phase state at the temperature T10. The condenser 3 exchanges heat with a refrigerant in a superheated gas state exceeding the temperature T10 and below the temperature T1, and is heated to a temperature T13. Thereby, the temperature T13 of the air passing through the evaporator 5 and the condenser 3 in this order can become the condensation temperature T10 of the refrigerant or more. The temperature T13 is set to the same degree as the temperature of the outer space of the dehumidifier 1. Therefore, in the dehumidifier 1 of the comparative example, when the condensation temperature T10 of the refrigerant is reduced, the temperature T13 of the air passing through the condenser 3 is also reduced. In the dehumidifying device 1 of the comparative example, the difference between the condensation temperature T10 and the highest value T20 of the temperature of the air at which the refrigerant in the gas-liquid two-phase state at the condensation temperature T10 performs heat exchange becomes smaller. Therefore, in the dehumidifier 1 of the comparative example, since the condensation temperature T10 cannot be sufficiently lowered, it is difficult to increase the EF value.

相對地,在本實施形態之除濕裝置1,在第3凝結部3c在過熱氣體狀態的冷媒、與是比通過第2凝結部3b之溫度T5的空氣更低溫之溫度T6的空氣之間進行熱交換。因此,即使降低冷媒之凝結溫度T2,亦抑制通過第3凝結部3c之空氣之溫度T7的降低。因此,若依據本實施形態之除 濕裝置1,在若將除濕運轉時之設定溫度設定成與比較例之除濕裝置1相同的情況,可使凝結溫度T2和凝結溫度T2之位於氣液二相狀態的冷媒進行熱交換之空氣之溫度的最高值T20之差,比凝結溫度T10和凝結溫度T10之位於氣液二相狀態的冷媒進行熱交換之空氣之溫度的最高值T20之差更大。因此,在本實施形態之除濕裝置1,即使降低凝結溫度T2,亦因為可使凝結溫度T2與該最高值T20之差成為與比較例之除濕裝置1同等以上,所以可使凝結溫度T2比比較例之除濕裝置1更降低,而可提高EF值。 In contrast, in the dehumidifier 1 according to this embodiment, heat is generated between the refrigerant in the superheated gas state in the third condensation section 3c and the air at a temperature T6 which is lower than the temperature of the air passing through the temperature T5 of the second condensation section 3b. exchange. Therefore, even if the condensation temperature T2 of the refrigerant is reduced, a decrease in the temperature T7 of the air passing through the third condensation portion 3c is suppressed. Therefore, if the division according to this embodiment is In the humid device 1, if the set temperature during the dehumidification operation is set to be the same as that of the dehumidifier 1 of the comparative example, the refrigerant at the condensation temperature T2 and the condensation temperature T2 in the gas-liquid two-phase state can exchange heat with the air. The difference between the highest temperature T20 is larger than the difference between the highest temperature T20 of the condensation temperature T10 and the highest temperature T20 of the air in which the refrigerant in the gas-liquid two-phase state performs heat exchange. Therefore, in the dehumidifier 1 of this embodiment, even if the condensation temperature T2 is reduced, the difference between the condensation temperature T2 and the highest value T20 can be made equal to or more than the dehumidifier 1 of the comparative example, so the ratio of the condensation temperature T2 can be compared. For example, the dehumidifier 1 is lowered, and the EF value can be increased.

即,若依據本實施形態之除濕裝置1,在第2風路11b內,在第3凝結部3c在過熱氣體狀態的冷媒與未通過蒸發器5的空氣之間進行熱交換。因此,與在凝結器3在過熱氣體狀態的冷媒與通過蒸發器5的空氣之間進行熱交換之比較例的除濕裝置1相比,可在不會降低從除濕裝置1所出來之空氣的溫度下,降低冷媒的凝結溫度。結果,與比較例之除濕裝置1相比,降低凝結溫度,而可使凝結壓力與蒸發壓力之差變小。因此,可提高表示除濕性能的EF值。 That is, according to the dehumidifier 1 according to this embodiment, heat exchange is performed between the refrigerant in the supercondensed gas state in the third condensation section 3c and the air that has not passed through the evaporator 5 in the second air path 11b. Therefore, compared with the dehumidifier 1 of the comparative example in which heat is exchanged between the refrigerant in the superheated gas state of the condenser 3 and the air passing through the evaporator 5, the temperature of the air coming out of the dehumidifier 1 can be reduced. Lower the condensation temperature of the refrigerant. As a result, as compared with the dehumidifier 1 of the comparative example, the condensation temperature is reduced, and the difference between the condensation pressure and the evaporation pressure can be made small. Therefore, it is possible to increase the EF value indicating dehumidification performance.

又,在第2凝結部3b在過冷卻液狀態的冷媒與通過蒸發器5的空氣之間進行熱交換。因此,與在凝結器3在過冷卻液狀態的冷媒與未通過蒸發器5的空氣之間進行熱交換的除濕裝置1相比,可充分地取得過冷卻度。因此,可得到大的除濕量。結果,在本實施形態之除濕裝置1,表示除濕性能的EF值變高。 In the second condensing portion 3b, heat exchange is performed between the refrigerant in the supercooled liquid state and the air passing through the evaporator 5. Therefore, compared with the dehumidifier 1 that performs heat exchange between the refrigerant in the supercooled liquid state of the condenser 3 and the air that has not passed through the evaporator 5, the degree of subcooling can be sufficiently obtained. Therefore, a large amount of dehumidification can be obtained. As a result, in the dehumidifying device 1 according to this embodiment, the EF value indicating the dehumidifying performance becomes high.

進而,在沿著送風機6之軸6a所延伸的方向從第1區域22觀察第2隔開部13的開口部13a時,風扇6b係被配置於開口部13a內。因此,因為從第1區域22往第2區域23之空氣的流動難被第2隔開部13妨礙,所以可使通風阻力變小。因此,因為可使得到所要的除濕量所需之送風機的風量變小,所以可使送風機的輸入(耗電量)變小。因此,可充分地提高表示除濕性能的EF值。 Furthermore, when the opening portion 13a of the second partition portion 13 is viewed from the first region 22 along the direction in which the axis 6a of the blower 6 extends, the fan 6b is disposed inside the opening portion 13a. Therefore, since the flow of air from the first region 22 to the second region 23 is difficult to be hindered by the second partition 13, the ventilation resistance can be reduced. Therefore, since the air volume of the blower required to obtain the desired amount of dehumidification can be reduced, the input (power consumption) of the blower can be reduced. Therefore, it is possible to sufficiently increase the EF value indicating dehumidification performance.

其次,說明本實施形態之變形例。 Next, a modification of this embodiment will be described.

參照第7圖,說明本實施形態之第1變形例。在本實施形態之第1變形例,一體地構成第2凝結部3b及第3凝結部3c。即,第2凝結部3b與第3凝結部3c係未經由配管彼此被分離。另一方面,第1凝結部3a與第2凝結部3b係經由配管彼此被分離。 A first modification of this embodiment will be described with reference to FIG. 7. In the first modification of this embodiment, the second coagulation portion 3b and the third coagulation portion 3c are integrally formed. That is, the second coagulation portion 3b and the third coagulation portion 3c are separated from each other without a pipe. On the other hand, the first coagulation part 3a and the second coagulation part 3b are separated from each other via a pipe.

若依據本第1實施形態之第1變形例,因為一體地構成第2凝結部3b及第3凝結部3c,所以可使凝結器3的構成變得簡單。又,因為一體地構成第2凝結部3b及第3凝結部3c,所以凝結器3之製造變成容易。 According to the first modification of the first embodiment, since the second coagulation portion 3b and the third coagulation portion 3c are integrally formed, the configuration of the condenser 3 can be simplified. Moreover, since the 2nd coagulation part 3b and the 3rd coagulation part 3c are integrally comprised, manufacture of the condenser 3 becomes easy.

接著,參照第8圖及第9圖,說明本實施形態之第2變形例。在本實施形態之第2變形例,在沿著送風機6之軸6a所延伸的方向從第2區域23觀察第2隔開部13的開口部13a時,凝結器3的上端及下端係被配置於開口部13a內。凝結器3之上下方向的高度尺寸D3係比開口部13a之內徑D2更小。 Next, a second modification of this embodiment will be described with reference to FIGS. 8 and 9. In the second modification of this embodiment, when the opening portion 13a of the second partition portion 13 is viewed from the second region 23 along the direction in which the axis 6a of the blower 6 extends, the upper and lower ends of the condenser 3 are arranged. In the opening 13a. The height dimension D3 in the up-down direction of the condenser 3 is smaller than the inner diameter D2 of the opening portion 13a.

若依據本實施形態之第2變形例,在沿著送風機6之軸6a所延伸的方向從第2區域23觀察第2隔開部13的開口 部13a時,凝結器3的上端及下端係被配置於開口部13a內。因此,因為在凝結器3之上下方向從第1區域22往第2區域23之空氣的流動難被凝結器3妨礙,所以可使通風阻力變成更小。 According to the second modification of this embodiment, when the opening portion 13a of the second partition portion 13 is viewed from the second region 23 along the direction in which the axis 6a of the blower 6 extends, the upper and lower ends of the condenser 3 are covered. It is arrange | positioned in the opening part 13a. Therefore, since the flow of air from the first region 22 to the second region 23 in the up-down direction of the condenser 3 is hardly obstructed by the condenser 3, the ventilation resistance can be made smaller.

進而,參照第10圖,說明本實施形態之第3變形例。在本實施形態之第3變形例,在沿著送風機6之軸6a所延伸的方向從第2區域23觀察第2隔開部13的開口部13a時,凝結器3的上端及下端係被配置於開口部13a內,且凝結器3之左右方向的兩端係被配置於開口部13a內。凝結器3之上下方向的高度尺寸D3係比開口部13a之內徑D2更小。又,凝結器3之左右方向的寬度尺寸D4係比開口部13a之內徑D2更小。 Furthermore, a third modification of this embodiment will be described with reference to FIG. 10. In the third modification of the present embodiment, when the opening portion 13 a of the second partition portion 13 is viewed from the second region 23 along the direction in which the axis 6 a of the blower 6 extends, the upper and lower ends of the condenser 3 are arranged. Both ends in the left-right direction of the condenser 3 are arranged in the opening portion 13a in the opening portion 13a. The height dimension D3 in the up-down direction of the condenser 3 is smaller than the inner diameter D2 of the opening portion 13a. The width dimension D4 in the left-right direction of the condenser 3 is smaller than the inner diameter D2 of the opening portion 13a.

若依據本實施形態之第3變形例,在沿著送風機6之軸6a所延伸的方向從第2區域23觀察第2隔開部13的開口部13a時,凝結器3的上端及下端係被配置於開口部13a內,且凝結器3之左右方向的兩端係被配置於開口部13a內。因此,因為在凝結器3之上下方向及左右方向從第1區域22往第2區域23之空氣的流動難被凝結器3妨礙,所以可使通風阻力變成更小。 According to the third modification of this embodiment, when the opening portion 13a of the second partition portion 13 is viewed from the second region 23 along the direction in which the axis 6a of the blower 6 extends, the upper and lower ends of the condenser 3 are covered. It is arrange | positioned in the opening part 13a, and both ends of the condenser 3 in the left-right direction are arrange | positioned in the opening part 13a. Therefore, since the flow of air from the first region 22 to the second region 23 in the up-down direction and the left-right direction of the condenser 3 is difficult to be hindered by the condenser 3, the ventilation resistance can be made smaller.

第2實施形態 Second embodiment

在第2實施形態之除濕裝置1,包括第2圖所示之構造。第11圖係表示凝結器3與蒸發器5之高度的圖。第12圖係表示凝結器3與蒸發器5之寬度的圖。 The dehumidifier 1 according to the second embodiment includes a structure shown in Fig. 2. FIG. 11 is a diagram showing the heights of the condenser 3 and the evaporator 5. FIG. 12 is a diagram showing the widths of the condenser 3 and the evaporator 5.

參照第11圖及第12圖,在第2實施形態之除濕裝置1,凝結器3係在位於蒸發器5與送風機6之間並在從蒸發器5往送風機6的方向被配置成與蒸發器5重疊時,比蒸發器5更向外側突出。 Referring to FIGS. 11 and 12, in the dehumidifier 1 of the second embodiment, the condenser 3 is located between the evaporator 5 and the blower 6 and is arranged in a direction from the evaporator 5 to the blower 6 so as to be connected to the evaporator. When 5 overlaps, it projects more outward than the evaporator 5.

具體而言,第2凝結部3b及第3凝結部3c係被配置於空氣之流動方向的最下游。蒸發器5係被配置於空氣之流動方向的最上游。在空氣之流動方向將第1凝結部3a配置於第2凝結部3b及第3凝結部3c與蒸發器5之間。即,蒸發器5係被配置於比第1凝結部3a、第2凝結部3b以及第3凝結部3c更上游。 Specifically, the second condensing portion 3b and the third condensing portion 3c are arranged at the most downstream in the flow direction of the air. The evaporator 5 is arranged at the most upstream of the air flow direction. The first condensation part 3 a is arranged between the second condensation part 3 b and the third condensation part 3 c and the evaporator 5 in the air flow direction. That is, the evaporator 5 is arranged further upstream than the first condensation part 3a, the second condensation part 3b, and the third condensation part 3c.

第2凝結部3b之高度h2和第3凝結部3c之高度h3的和比蒸發器5的高度h1更大。此外,在本實施形態,蒸發器5之高度h1係與第2凝結部3b之高度h2相等。又,第1凝結部3a之高度係與蒸發器5之高度h1及第2凝結部3b之高度h2相等。在凝結器3之高度方向,第3凝結部3c係比蒸發器5更向上側突出。 The sum of the height h2 of the second condensation part 3b and the height h3 of the third condensation part 3c is larger than the height h1 of the evaporator 5. In this embodiment, the height h1 of the evaporator 5 is equal to the height h2 of the second condensing portion 3b. The height of the first condensation portion 3a is equal to the height h1 of the evaporator 5 and the height h2 of the second condensation portion 3b. In the height direction of the condenser 3, the third condensing portion 3c projects more upward than the evaporator 5.

第2凝結部3b的寬度w2比蒸發器5的寬度w1更大。此外,在本實施形態,蒸發器5的寬度w1係與第1凝結部3a的寬度相等。又,第3凝結部3c的寬度係與第2凝結部3b的寬度w2相等。在凝結器3的寬度方向,第2凝結部3b及第3凝結部3c係比蒸發器5更向右側及左側突出。 The width w2 of the second condensation portion 3 b is larger than the width w1 of the evaporator 5. In the present embodiment, the width w1 of the evaporator 5 is equal to the width of the first condensing portion 3a. The width of the third condensation portion 3c is equal to the width w2 of the second condensation portion 3b. In the width direction of the condenser 3, the second condensation part 3b and the third condensation part 3c protrude further to the right and left than the evaporator 5.

若依據本實施形態之除濕裝置1,凝結器3係在位於蒸發器5與送風機6之間並在從蒸發器5往送風機6的方向被配置成與蒸發器5重疊時,比蒸發器5更向外側突出。因此,在從蒸發器5往送風機6之空氣的流動方向可在不會被蒸發器5妨礙下使空氣流至凝結器3。因此,風路的構成變成容易。 According to the dehumidifying device 1 according to this embodiment, the condenser 3 is located between the evaporator 5 and the blower 6 and is arranged to overlap the evaporator 5 in a direction from the evaporator 5 to the blower 6, which is more than the evaporator 5. Protrudes outward. Therefore, in the flow direction of the air from the evaporator 5 to the blower 6, the air can be caused to flow to the condenser 3 without being hindered by the evaporator 5. Therefore, the configuration of the air passage becomes easy.

在凝結器3之上部及下部的至少其中之一比蒸發器5更突出的情況,可將在凝結器3之上部及下部的至少其中之一取入來自室內的空氣之第2風路11b的第2吸入口14b配置於框體20的背面20a。又,在凝結器3的寬度方向(左右方向)凝結器3比蒸發器5更突出的情況,即在凝結器3的寬度比蒸發器5之寬度更大的情況,可將在凝結器3之左側及右側的至少其中之一取入來自室內的空氣之第2風路11b的第2吸入口14b配置於框體20的背面20a。因此,可在不大為變更以往之除濕裝置的構成下,構成本實施形態之除濕裝置1。 In a case where at least one of the upper and lower portions of the condenser 3 is more prominent than the evaporator 5, at least one of the upper and lower portions of the condenser 3 may be taken into the second air path 11b of the indoor air. The second suction port 14 b is arranged on the back surface 20 a of the housing 20. When the condenser 3 is more prominent than the evaporator 5 in the width direction (left-right direction) of the condenser 3, that is, when the width of the condenser 3 is larger than the width of the evaporator 5, the At least one of the left and right sides of the second intake port 14b for taking in the air from the room into the second air path 11b is arranged on the back surface 20a of the housing 20. Therefore, the dehumidifier 1 of this embodiment can be configured without substantially changing the configuration of the conventional dehumidifier.

又,藉由將第2風路11b之第2吸入口14b配置成對準凝結器3之冷媒的入口,可提高熱交換效率。即,在被配置於第2風路11b的最下游之凝結器3之冷媒的流動為上下方向的情況,高溫冷媒之入口被配置於凝結器3的上部。因此,藉由將第2風路11b配置成對準凝結器3之上部,可提高熱交換效率。又,在被配置於第2風路11b的最下游之凝結器3之冷媒從右向左流動的情況,高溫冷媒之入口被配置於凝結器3的右側。因此,藉由將第2風路11b配置成對準凝結器3之右側,可提高熱交換效率。 In addition, by arranging the second suction port 14b of the second air path 11b so as to be aligned with the refrigerant inlet of the condenser 3, the heat exchange efficiency can be improved. That is, when the flow of the refrigerant in the condenser 3 arranged in the most downstream of the second air path 11 b is in the up-down direction, the inlet of the high-temperature refrigerant is arranged above the condenser 3. Therefore, by arranging the second air path 11b so as to be aligned with the upper portion of the condenser 3, the heat exchange efficiency can be improved. Moreover, when the refrigerant | coolant of the condenser 3 arrange | positioned at the most downstream of the 2nd air path 11b flows from right to left, the inlet of a high temperature refrigerant is arrange | positioned on the right side of the condenser 3. Therefore, by arranging the second air path 11b to the right side of the condenser 3, the heat exchange efficiency can be improved.

第3實施形態 Third Embodiment

參照第13圖,在第3實施形態之除濕裝置1,第1凝結部3a係被配置於蒸發器5與第2凝結部3b之間。第1凝結部3a與第2凝結部3b之間隔t2係比第1凝結部3a與蒸發器5之間隔t1更大。即,在從蒸發器5往送風機6之空氣的流動方向之第1凝結部3a與第2凝結部3b的間隔t2係比第1凝結部3a與蒸發器5之間隔t1更大。又,在從蒸發器5往送風機6之空氣的流動方向之第1凝結部3a與第3凝結部3c的間隔係和第1凝結部3a與第2凝結部3b之間隔t2相等。 Referring to FIG. 13, in the dehumidifying device 1 according to the third embodiment, the first condensation portion 3 a is disposed between the evaporator 5 and the second condensation portion 3 b. The interval t2 between the first condensation section 3a and the second condensation section 3b is larger than the interval t1 between the first condensation section 3a and the evaporator 5. That is, the interval t2 between the first condensing portion 3a and the second condensing portion 3b in the flow direction of the air from the evaporator 5 to the blower 6 is larger than the interval t1 between the first condensing portion 3a and the evaporator 5. In addition, the interval between the first condensation portion 3a and the third condensation portion 3c in the flow direction of the air from the evaporator 5 to the blower 6 is equal to the interval t2 between the first condensation portion 3a and the second condensation portion 3b.

在蒸發器5與第1凝結部3a之間,在蒸發器5與冷媒進行熱交換之比室溫(例如27℃)更低之溫度(例如13℃)的空氣向第1凝結部3a流動。在第1凝結部3a與第2凝結部3b之間,在第1凝結部3a與冷媒進行熱交換之比室溫(例如27℃)更高之溫度(例如28℃)的空氣向第2凝結部3b流動。 Between the evaporator 5 and the first condensing section 3a, air at a temperature (for example, 13 ° C) lower than the room temperature (for example, 27 ° C) for heat exchange between the evaporator 5 and the refrigerant flows to the first condensing section 3a. Between the first condensation part 3a and the second condensation part 3b, air at a higher temperature (for example, 28 ° C) than the room temperature (for example, 27 ° C) for heat exchange between the first condensation part 3a and the refrigerant is condensed toward the second The portion 3b flows.

在蒸發器5與第1凝結部3a之間,因為通過蒸發器5之空氣與室內之空氣混合時凝結溫度與空氣溫度的差變小,所以凝結器性能係降低,而蒸發器5與第1凝結部3a的間隔t1亦可變小。另一方面,在第1凝結部3a與第2凝結部3b之間,藉由使第1凝結部3a與第2凝結部3b之間隔t2變大,設置通通第1凝結部3a後之空氣與室外之空氣的混合區域。藉此,因為第2凝結部3b之凝結溫度與空氣溫度的差變大,所以可提高凝結性能。 Between the evaporator 5 and the first condensing portion 3a, since the difference between the condensation temperature and the air temperature becomes smaller when the air passing through the evaporator 5 is mixed with the indoor air, the performance of the condenser decreases, and the evaporator 5 and the first The interval t1 of the coagulation portion 3a can also be made smaller. On the other hand, between the first condensation part 3a and the second condensation part 3b, by increasing the interval t2 between the first condensation part 3a and the second condensation part 3b, the air and the air after the first condensation part 3a is passed through are provided. Mixed area of outdoor air. Thereby, since the difference between the condensation temperature and the air temperature of the second condensation portion 3b becomes large, the condensation performance can be improved.

若依據本實施形態之除濕裝置1,第1凝結部3a與第2凝結部3b的間隔t2係比第1凝結部3a與蒸發器5之間隔t1更大。因此,在第1凝結部3a與蒸發器5之間係藉由抑制通過蒸發器5之空氣與室內之空氣混合,而可抑制第1凝結部3a之凝結溫度與空氣溫度的差變小。藉此,可抑制凝結性能的降低。又,在第1凝結部3a與第2凝結部3b之間係藉由促進通過第1凝結部3a之空氣與室內之空氣混合,而可使第2凝結部3b之凝結溫度與空氣溫度的差變大。藉此,可提高凝結性能。又,因為可設置於通過第1凝結部3a與第2凝結部3b之空氣的助走區域,所以可使通過第2凝結部3b之空氣的風速分布變成均勻。 According to the dehumidifying device 1 according to this embodiment, the interval t2 between the first condensation portion 3a and the second condensation portion 3b is larger than the interval t1 between the first condensation portion 3a and the evaporator 5. Therefore, by preventing the air passing through the evaporator 5 from mixing with the indoor air between the first condensing portion 3a and the evaporator 5, the difference between the condensation temperature of the first condensing portion 3a and the air temperature can be reduced. This can suppress a decrease in the coagulation performance. The difference between the condensation temperature of the second condensation portion 3b and the air temperature is promoted between the first condensation portion 3a and the second condensation portion 3b by promoting the mixing of the air passing through the first condensation portion 3a and the indoor air. Get bigger. Thereby, coagulation performance can be improved. Moreover, since it can be provided in the assisted area of the air passing through the first condensation part 3a and the second condensation part 3b, the wind speed distribution of the air passing through the second condensation part 3b can be made uniform.

第4實施形態 Fourth Embodiment

參照第14圖及第15圖,在第4實施形態之除濕裝置1,被配置於空氣之流動的最下游之向第2凝結部3b及第3凝結部3c之空氣的吸入口被設置於背面20a及側面20c。 Referring to FIG. 14 and FIG. 15, in the dehumidifying device 1 of the fourth embodiment, the air inlets for the air to the second condensation part 3 b and the third condensation part 3 c, which are arranged at the most downstream of the air flow, are provided on the back surface. 20a and 20c.

第3吸入口15被設置於框體20的側面20c。在側面20c,第3吸入口15構成為將空氣吸入第1風路11a及第2風路11b。第3吸入口15係在第1風路11a構成為將室內空氣吸入第1凝結部3a與第2凝結部3b之間。又,第3吸入口15係在第2風路11b構成為將室內空氣吸入第2吸入口14b與第3凝結部3c之間。 The third suction port 15 is provided on a side surface 20 c of the housing 20. On the side surface 20c, the third suction port 15 is configured to suck air into the first air path 11a and the second air path 11b. The third suction port 15 is configured in the first air passage 11a to suck indoor air between the first condensation part 3a and the second condensation part 3b. The third suction port 15 is configured in the second air passage 11b to suck indoor air between the second suction port 14b and the third condensation part 3c.

又,在本實施形態之除濕裝置1,亦可與上述之第3實施形態一樣,第1凝結部3a與第2凝結部3b的間隔t2係比第1凝結部3a與蒸發器5之間隔t1更大。 In addition, in the dehumidifying device 1 of this embodiment, as in the third embodiment described above, the interval t2 between the first condensation section 3a and the second condensation section 3b is greater than the interval t1 between the first condensation section 3a and the evaporator 5. Bigger.

若依據本實施形態之除濕裝置1,因為在框體20,不僅設置第1吸入口14a及第2吸入口14b,而且設置將空氣吸入第1風路11a及第2風路11b的第3吸入口15,所以可增加通過第2凝結部3b及第3凝結部3c之空氣的風量。藉此,可提高凝結性能。 According to the dehumidifying device 1 according to this embodiment, not only the first suction port 14a and the second suction port 14b, but also the third suction means for sucking air into the first air path 11a and the second air path 11b are provided in the housing 20. The opening 15 can increase the air volume of the air passing through the second condensation part 3b and the third condensation part 3c. Thereby, coagulation performance can be improved.

又,第1吸入口14a、第2吸入口14b以及第3吸入口15係因為藉由將開口設置於框體20而可易於製作,所以可在不大幅度地變更以往之除濕裝置的構成下,將本實施形態之除濕裝置1作成產品。 In addition, the first suction port 14a, the second suction port 14b, and the third suction port 15 can be easily manufactured by providing the openings in the housing 20, so that the structure of the conventional dehumidifier can be changed without significantly changing the structure. The dehumidifier 1 of this embodiment is made into a product.

其次,說明第4實施形態之變形例的除濕裝置1。 Next, a dehumidifier 1 according to a modification of the fourth embodiment will be described.

參照第16圖,第4實施形態之變形例的除濕裝置1包括用以分離通過過冷卻液狀態之冷媒所流動的第1凝結部3a之過冷卻部的空氣之第3隔開部16。第3隔開部16係在第1凝結部3a與第2凝結部3b之間被配置成塞住第1凝結部3a與第2凝結部3b之間的空間。第3吸入口15係被設置於比第3隔開部16更上方。 Referring to FIG. 16, a dehumidifier 1 according to a modification of the fourth embodiment includes a third partition portion 16 for separating the air of the subcooling portion of the first condensation portion 3 a flowing through the refrigerant in a supercooled liquid state. The third partition portion 16 is arranged between the first condensation portion 3a and the second condensation portion 3b so as to block a space between the first condensation portion 3a and the second condensation portion 3b. The third suction port 15 is provided above the third partition 16.

若依據第4實施形態之變形例的除濕裝置1,因為藉第3隔開部16抑制在第1凝結部3a的過冷卻部與冷媒進行熱交換之溫度比室溫更低的空氣、和室內空氣的混合,所以可更提高凝結性能。 According to the dehumidifier 1 according to the modification of the fourth embodiment, the third partition 16 prevents the subcooling section in the first condensation section 3a from performing heat exchange with the refrigerant at a temperature lower than room temperature, and indoors Mixing of air can improve the coagulation performance.

第5實施形態 5th Embodiment

第5實施形態之除濕裝置1包括第2圖所示之構造。在第5實施形態之除濕裝置1,凝結器3的冷媒入口x2係被配置於凝結器3的上側,凝結器3的冷媒出口y2係被配置於凝結器3的下側。又,凝結器3的冷媒入口x2係被配置於空氣之流動的最下游,凝結器3的冷媒出口y2係被配置於空氣之流動的最上游。即,凝結器3的冷媒入口x2係被設置於第3凝結部3c,凝結器3的冷媒出口y2係被設置於第1凝結部3a。又,蒸發器5的冷媒入口z係被配置於蒸發器5的下側。 The dehumidifier 1 according to the fifth embodiment includes a structure shown in FIG. 2. In the dehumidifier 1 of the fifth embodiment, the refrigerant inlet x2 of the condenser 3 is arranged on the upper side of the condenser 3, and the refrigerant outlet y2 of the condenser 3 is arranged on the lower side of the condenser 3. The refrigerant inlet x2 of the condenser 3 is arranged at the most downstream of the air flow, and the refrigerant outlet y2 of the condenser 3 is arranged at the most upstream of the air flow. That is, the refrigerant inlet x2 of the condenser 3 is provided in the third condensation part 3c, and the refrigerant outlet y2 of the condenser 3 is provided in the first condensation part 3a. The refrigerant inlet z of the evaporator 5 is arranged below the evaporator 5.

若依據本實施形態之除濕裝置,冷媒係在第3凝結部3c、第2凝結部3b以及第1凝結部3a依序流通。因此,在第3凝結部3c流動之冷媒係與在第2風路11b流動之空氣相對向地流動。在第2凝結部3b及第1凝結部3a流動之冷媒係與在第1風路11a流動之空氣及在第2風路11b流動之空氣相對向地流動。藉此,因為可進行高溫度效率之熱交換,所以可提高凝結效率。 According to the dehumidifying device of this embodiment, the refrigerant flows through the third condensation part 3c, the second condensation part 3b, and the first condensation part 3a in this order. Therefore, the refrigerant flowing through the third condensing portion 3c flows opposite to the air flowing through the second air path 11b. The refrigerant flowing through the second condensation part 3b and the first condensation part 3a flows opposite to the air flowing through the first air path 11a and the air flowing through the second air path 11b. Thereby, heat exchange with high temperature efficiency can be performed, and condensing efficiency can be improved.

又,冷媒之入口被設置於在第2風路11b所配置的第3凝結部3c,所以在凝結器3中溫度高的冷媒可與在第2風路11b流動之室內溫度的空氣進行熱交換。藉此,熱交換性能變高。 The inlet of the refrigerant is provided in the third condensing section 3c arranged in the second air path 11b. Therefore, the refrigerant having a high temperature in the condenser 3 can perform heat exchange with the air of the room temperature flowing through the second air path 11b. . This improves heat exchange performance.

又,因為凝結器3的冷媒出口y2被配置於凝結器3的下側,所以對被配置於蒸發器5之下側的冷媒入口z連結凝結器3的冷媒出口y2這件事變成容易。又,因為凝結器3的冷媒出口y2被設置於第1凝結部3a,所以可縮短連結第1凝結部3a與蒸發器5之配管。又,可使在蒸發器5流動之冷媒與在第1風路11a流動之空氣相對向地流動。藉此,可提高蒸發性能。又,一般而言,在蒸發器5流動之冷媒係為了流動的穩定性而從下向上流動。若依據本實施形態之凝結器3及蒸發器5的配置,在蒸發器5可使冷媒從下向上流動。 Moreover, since the refrigerant outlet y2 of the condenser 3 is arranged on the lower side of the condenser 3, it is easy to connect the refrigerant inlet y2 of the condenser 3 to the refrigerant inlet z arranged on the lower side of the evaporator 5. Moreover, since the refrigerant outlet y2 of the condenser 3 is provided in the first condensation part 3a, the pipe connecting the first condensation part 3a and the evaporator 5 can be shortened. In addition, the refrigerant flowing through the evaporator 5 and the air flowing through the first air passage 11a can be caused to face each other. Thereby, evaporation performance can be improved. In general, the refrigerant flowing in the evaporator 5 flows from the bottom to the top for the stability of the flow. According to the arrangement of the condenser 3 and the evaporator 5 according to this embodiment, the refrigerant can flow from the bottom to the top of the evaporator 5.

第6實施形態 Sixth embodiment

參照第17圖,在第6實施形態之除濕裝置1,第2凝結部3b及第3凝結部3c之各個的分配數係比第1凝結部3a的分配數更多。即,使第2凝結部3b及第3凝結部3c之各個的冷媒流至內部之導熱管的支數係比使第1凝結部3a的冷媒流至內部之導熱管的支數更多。 Referring to Fig. 17, in the dehumidifier 1 of the sixth embodiment, the number of allocations of each of the second condensation part 3b and the third condensation part 3c is larger than that of the first condensation part 3a. In other words, the number of the heat transfer tubes flowing the refrigerant in each of the second condensing portion 3b and the third condensing portion 3c to the inside is larger than the number of heat transfer tubes flowing the refrigerant in the first condensing portion 3a to the inside.

此外,如第17圖所示,亦可對各個第1凝結部3a、第2凝結部3b以及第3凝結部3c改變分配數。又,參照第18 圖,亦可在第1凝結部3a之中途減少分配數。 In addition, as shown in FIG. 17, the number of allocations may be changed for each of the first condensation part 3 a, the second condensation part 3 b, and the third condensation part 3 c. In addition, referring to Fig. 18, the number of allocations may be reduced in the middle of the first condensation portion 3a.

若依據本實施形態之除濕裝置1,第2凝結部3b及第3凝結部3c之各個的分配數係比第1凝結部3a的分配數更多。因此,在因為在冷媒為過熱氣體狀態或氣液二相狀態冷媒的流速快而壓力損失大的區域,藉由降低冷媒的流速,可減少壓力損失。另一方面,在因為在冷媒為過冷卻液狀態冷媒的流速慢而壓力損失小的區域,藉由提高冷媒的流速,可進行效率高的熱交換。 According to the dehumidifying device 1 according to this embodiment, the number of allocations of each of the second coagulation portion 3b and the third coagulation portion 3c is larger than the number of allocations of the first coagulation portion 3a. Therefore, in a region where the refrigerant has a high flow rate and a large pressure loss because the refrigerant is in a superheated gas state or a gas-liquid two-phase state, reducing the flow rate of the refrigerant can reduce the pressure loss. On the other hand, in a region where the flow rate of the refrigerant is slow and the pressure loss is small because the refrigerant is in the supercooled liquid state, by increasing the flow rate of the refrigerant, efficient heat exchange can be performed.

第7實施形態 Seventh embodiment

參照第19圖,在第7實施形態之除濕裝置1,第3凝結部3c係在第2風路11b,構成為對第2隔開部13在與送風機6相反側延伸。 Referring to FIG. 19, in the dehumidifier 1 according to the seventh embodiment, the third condensation portion 3c is connected to the second air passage 11b, and is configured to extend the second partition portion 13 on the side opposite to the blower 6.

因為第1凝結部3a、第2凝結部3b以及蒸發器5被配置於第2風路11b,所以在第2風路11b流動之空氣的壓力損失係比在第1風路11a流動之空氣的壓力損失更小。因此,因為在第2風路11b流動之空氣的風量增加,而在第1風路11a流動之空氣的第量減少。因此,因為在被配置於第1風路11a之蒸發器5流動之空氣的風量減少,所以除濕量減少。例如,若使蒸發器5、第1凝結部3a、第2凝結部之列數、散熱片片數的總和、與第3凝結部3c之列數、散熱片片數相等,在同一前面面積時成為相同的通風阻力。因此,根據蒸發器5、第1凝結部3a以及第2凝結部3b之前面面積與第3凝結部之前面面積的百分比,可易於調整在第1風路11a及第2風路11b流動之空氣的風量。 Since the first condensing portion 3a, the second condensing portion 3b, and the evaporator 5 are disposed in the second air path 11b, the pressure loss of the air flowing in the second air path 11b is greater than that of the air flowing in the first air path 11a. Less pressure loss. Therefore, because the amount of air flowing through the second air path 11b increases, the amount of air flowing through the first air path 11a decreases. Therefore, the amount of dehumidification is reduced because the volume of air flowing through the evaporator 5 disposed in the first air path 11a is reduced. For example, if the total number of rows of the evaporator 5, the first condensation part 3a, the second condensation part, and the number of fins is equal to the number of rows of the third condensation part 3c, and the number of fins, the same area Become the same ventilation resistance. Therefore, the air flowing through the first air path 11a and the second air path 11b can be easily adjusted according to the percentage of the area of the front surface of the evaporator 5, the first condensation part 3a, and the second condensation part 3b and the front surface area of the third condensation part. Amount of wind.

若依據本實施形態之除濕裝置1,第3凝結部3c係在第2風路11b,構成為對第2隔開部13在與送風機6相反側延伸。因此,可使第2風路11b的壓力損失變大。在第1風路11a係因為被配置第1凝結部3a、第2凝結部3b以及蒸發器5而壓力損失變大,藉由使第2風路11b的壓力損失變大,可抑制空氣之往第2風路11b的偏流。藉此,可抑制在蒸發器5之除濕量的減少。因此,可得到高效率的除濕裝置1。 According to the dehumidifier 1 according to this embodiment, the third condensation portion 3c is connected to the second air path 11b, and is configured to extend the second partition portion 13 on the side opposite to the blower 6. Therefore, the pressure loss in the second air passage 11b can be increased. In the first air passage 11a, the pressure loss is increased because the first condensing portion 3a, the second condensing portion 3b, and the evaporator 5 are disposed. By increasing the pressure loss in the second air passage 11b, the air flow can be suppressed. Deflection of the second air path 11b. This can suppress a decrease in the amount of dehumidification in the evaporator 5. Therefore, a highly efficient dehumidifier 1 can be obtained.

第8實施形態 Eighth embodiment

參照第20圖,在第8實施形態之除濕裝置1,冷媒迴路10係構成為使從蒸發器5所流出的冷媒經由凝結器3流至壓縮機2。在本實施形態之除濕裝置1,凝結器3包括高低壓熱交換部17。高低壓熱交換部17包括:第1流路,係連接第1凝結部3a的冷媒出口與降壓裝置4的冷媒入口;及第2流路,係連接蒸發器5的冷媒出口與壓縮機2的吸入口(冷媒入口)。 Referring to FIG. 20, in the dehumidifier 1 according to the eighth embodiment, the refrigerant circuit 10 is configured so that the refrigerant flowing from the evaporator 5 flows to the compressor 2 through the condenser 3. In the dehumidifier 1 of this embodiment, the condenser 3 includes a high-low pressure heat exchange unit 17. The high-low pressure heat exchange unit 17 includes a first flow path connected to the refrigerant outlet of the first condensing portion 3a and a refrigerant inlet of the pressure reducing device 4; and a second flow path connected to the refrigerant outlet of the evaporator 5 and the compressor 2 Suction inlet (refrigerant inlet).

在高低壓熱交換部17,在第1流路流動之冷媒與在第2流路流動的冷媒之間進行熱交換。藉此,在凝結器3之冷媒出口流動之冷媒與在蒸發器5之冷媒出口流動的冷媒之間進行熱交換。因此,在蒸發器5流動的冷媒之藉焓差之擴大的蒸發性能(除濕量)可增大。 In the high-low pressure heat exchange unit 17, heat is exchanged between the refrigerant flowing through the first flow path and the refrigerant flowing through the second flow path. Thereby, heat exchange is performed between the refrigerant flowing through the refrigerant outlet of the condenser 3 and the refrigerant flowing through the refrigerant outlet of the evaporator 5. Therefore, the evaporation performance (dehumidification amount) of the refrigerant by flowing in the evaporator 5 can be increased by the enthalpy difference.

又,壓縮機2的吸入口(冷媒入口)係為了維持可靠性,需要吸入在蒸發器5內令氣化的冷媒。可是,在蒸發器5因冷媒的氣體部係局部地成為高溫而熱交換性能降低。 In addition, the suction port (refrigerant inlet) of the compressor 2 is a refrigerant that is required to be vaporized in the evaporator 5 in order to maintain reliability. However, in the evaporator 5, the gas part of the refrigerant becomes locally high in temperature, which reduces the heat exchange performance.

在本實施形態之冷媒迴路10,即使從蒸發器5所流出的冷媒是氣液二相狀態,亦可使令氣化的冷媒向壓縮機2 的冷媒吸入口回去。因此,蒸發器5的性能不會降低,壓縮機2的可靠性亦不會受損。又,即使蒸發器5之冷媒的分配變差,亦因為使氣液二相狀態的冷媒流至蒸發器5,所以可最大限度地利用蒸發器5的性能。 In the refrigerant circuit 10 of this embodiment, even if the refrigerant flowing out of the evaporator 5 is in a gas-liquid two-phase state, the vaporized refrigerant can be returned to the refrigerant suction port of the compressor 2. Therefore, the performance of the evaporator 5 is not degraded, and the reliability of the compressor 2 is not impaired. In addition, even if the distribution of the refrigerant in the evaporator 5 is deteriorated, the refrigerant in the gas-liquid two-phase state is caused to flow to the evaporator 5, so that the performance of the evaporator 5 can be used to the maximum.

如以上所示,若依據本實施形態之除濕裝置1,冷媒迴路10構成為使從蒸發器5所流出的冷媒經由凝結器3流通至壓縮機2。因此,可將液冷媒供給至在蒸發器5因過熱氣體的發生而降低熱交換效率的區域。藉此,可改善蒸發器5的熱交換性能。 As described above, according to the dehumidifier 1 according to this embodiment, the refrigerant circuit 10 is configured to allow the refrigerant flowing out from the evaporator 5 to flow through the condenser 3 to the compressor 2. Therefore, the liquid refrigerant can be supplied to a region where the heat exchange efficiency is reduced by the occurrence of the superheated gas in the evaporator 5. Thereby, the heat exchange performance of the evaporator 5 can be improved.

應認為這次所揭示之實施形態係在所有的事項上是舉例表示,不是用以限制的。本發明的範圍係不是根據上述之說明,而是根據申請專利範圍所表示,圖謀包含與申請專利範圍同等之意義及在範圍內之所有的變更。 It should be considered that the embodiments disclosed this time are examples on all matters and are not intended to be limiting. The scope of the present invention is not based on the above description, but is expressed according to the scope of the patent application. The intention is to include all changes within the meaning and scope of the scope of the patent application.

Claims (8)

一種除濕裝置,係包括:框體;冷媒迴路,係包含在該框體之內部所收容的壓縮機、凝結器、降壓裝置以及蒸發器;以及送風機,係具有以軸為中心轉動的風扇,且被收容於該框體之該內部;在該冷媒迴路,冷媒係在該壓縮機、該凝結器、該降壓裝置以及該蒸發器依序流通;該凝結器係包含:第1凝結部,係過冷卻液狀態之該冷媒流動;第2凝結部,係氣液二相狀態之該冷媒流動;以及第3凝結部,係過熱氣體狀態之該冷媒流動;該框體係包含:第1隔開部,係具有:第1風路,係藉由該風扇以該軸為中心轉動,從該框體的外部被取入該內部的空氣依序通過該蒸發器、該第1凝結部以及該第2凝結部;及第2風路,係藉由該風扇以該軸為中心轉動,從該框體的該外部被取入該內部的空氣通過該第3凝結部;第2隔開部,係具有連接被配置藉該第1隔開部所隔開之該第1風路及該第2風路之第1區域與被配置該送風機之第2區域的開口部,且將該第1區域與該第2區域隔開;在沿著該軸所延伸的方向從該第1區域觀察該第2隔開部的該開口部時,該風扇係被配置於該開口部內;該第1風路內之空氣的流通方向與該第2風路內之空氣的流通方向並行;通過該第1風路的空氣與通過該第2風路的空氣,藉由該送風機而朝同一個方向送出;通過該第1風路後的空氣與通過該第2風路後的空氣,從該框體的吹出口被吹出至室內空間。A dehumidifying device includes: a frame body; a refrigerant circuit including a compressor, a condenser, a pressure reducing device, and an evaporator contained in the frame body; and a blower including a fan rotating around a shaft, And is contained in the interior of the frame; in the refrigerant circuit, the refrigerant flows through the compressor, the condenser, the pressure reducing device, and the evaporator in sequence; the condenser includes: a first condensation section, The refrigerant flow in the supercooled liquid state; the second condensation part, the refrigerant flow in the gas-liquid two-phase state; and the third condensation part, the refrigerant flow in the superheated gas state; the frame system includes: the first partition The unit includes a first air path, and the fan rotates around the shaft, and the air taken in from the outside of the frame body passes through the evaporator, the first condensing unit, and the first 2 condensation section; and a second air path, through which the fan rotates around the shaft, the air taken in from the outside of the housing through the third condensation section; the second partition section, the The connection is arranged to be separated by the first partition. Openings of the first area of the first air passage and the second area of the second air passage and the second area where the blower is arranged, and separating the first area from the second area; in a direction extending along the axis When the opening of the second partition is viewed from the first area, the fan is disposed in the opening; the direction of air flow in the first air path and the air flow in the second air path The directions are parallel; the air passing through the first air path and the air passing through the second air path are sent out in the same direction by the blower; the air passing through the first air path and the air passing through the second air path Air is blown out to the indoor space from the blow-out port of this housing. 如申請專利範圍第1項之除濕裝置,其中該凝結器係在位於該蒸發器與該送風機之間並在從該蒸發器往該送風機的方向被配置成與該蒸發器重疊時,比該蒸發器更向外側突出。For example, the dehumidifying device of the first patent application range, wherein the condenser is located between the evaporator and the blower and is arranged to overlap the evaporator in a direction from the evaporator to the blower, which is greater than the evaporation. The device protrudes more outward. 如申請專利範圍第1項之除濕裝置,其中該第1凝結部係被配置於該蒸發器與該第2凝結部之間;該第1凝結部與該第2凝結部的間隔係比該第1凝結部與該蒸發器的間隔更大。For example, in the dehumidifying device of the first scope of the application for a patent, the first condensation part is disposed between the evaporator and the second condensation part; the distance between the first condensation part and the second condensation part is greater than that of the first condensation part The distance between the condensation section and the evaporator is larger. 如申請專利範圍第1項之除濕裝置,其中該框體係包含被設置第1吸入口及第2吸入口之背面、與被設置第3吸入口的側面;在該背面該第1吸入口係構成為將空氣吸入該第1風路,且該第2吸入口係構成為將空氣吸入該第2風路;在該側面該第3吸入口係構成為將空氣吸入該第1風路及該第2風路;該第3吸入口係在第1風路構成為將空氣吸入該第1凝結部與該第2凝結部之間。For example, the dehumidification device of the first scope of the patent application, wherein the frame system includes a back surface on which the first suction port and the second suction port are provided, and a side surface on which the third suction port is provided; In order to suck air into the first air path, the second suction port is configured to suck air into the second air path; on the side, the third suction port is configured to suck air into the first air path and the first air path. 2 air passages; the third suction port is configured in the first air passage to suck air between the first condensation part and the second condensation part. 如申請專利範圍第1項之除濕裝置,其中在該凝結器,冷媒係在該第3凝結部、該第2凝結部以及該第1凝結部依序流通;該冷媒之入口係被配置於該凝結器的上側,且被設置於該第3凝結部;該冷媒之出口係被配置於該凝結器的下側,且被設置於該第1凝結部。For example, in the dehumidifier of the first scope of the patent application, in the condenser, the refrigerant flows through the third condensation part, the second condensation part, and the first condensation part in sequence; the inlet of the refrigerant is arranged in the condenser. An upper side of the condenser is provided on the third condensing portion; an outlet of the refrigerant is arranged on the lower side of the condenser and is provided on the first condensing portion. 如申請專利範圍第1項之除濕裝置,其中該第2凝結部及該第3凝結部之各個的分配數係比該第1凝結部的分配數更多。For example, in the dehumidifying device of the first scope of the patent application, the number of allocations of each of the second condensation part and the third condensation part is greater than that of the first condensation part. 如申請專利範圍第1項之除濕裝置,其中該第3凝結部係在該第2風路,構成為對該第2隔開部在與該送風機相反側延伸。For example, in the dehumidifying device according to the first item of the patent application, the third condensation portion is connected to the second air path, and the second partition portion is configured to extend on the opposite side of the blower. 如申請專利範圍第1項之除濕裝置,其中該冷媒迴路係構成為使從該蒸發器所流出的冷媒經由該凝結器流通至該壓縮機。 For example, the dehumidification device according to the first patent application range, wherein the refrigerant circuit is configured to circulate the refrigerant flowing out from the evaporator to the compressor through the condenser.
TW106114252A 2017-01-12 2017-04-28 Dehumidifier TWI671494B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
??PCT/JP2017/000835 2017-01-12
PCT/JP2017/000835 WO2018131121A1 (en) 2017-01-12 2017-01-12 Dehumidifying device

Publications (2)

Publication Number Publication Date
TW201825838A TW201825838A (en) 2018-07-16
TWI671494B true TWI671494B (en) 2019-09-11

Family

ID=62840595

Family Applications (1)

Application Number Title Priority Date Filing Date
TW106114252A TWI671494B (en) 2017-01-12 2017-04-28 Dehumidifier

Country Status (4)

Country Link
JP (1) JP6644173B2 (en)
CN (1) CN110139700B (en)
TW (1) TWI671494B (en)
WO (1) WO2018131121A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP7204906B2 (en) * 2019-05-27 2023-01-16 三菱電機株式会社 dehumidifier
WO2021117199A1 (en) * 2019-12-12 2021-06-17 三菱電機株式会社 Dehumidifier
CN115867752A (en) * 2020-06-05 2023-03-28 三菱电机株式会社 Dehumidifying device
WO2022224416A1 (en) * 2021-04-22 2022-10-27 三菱電機株式会社 Dehumidifying device
JPWO2022264375A1 (en) * 2021-06-17 2022-12-22

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52135354U (en) * 1976-04-09 1977-10-14
JPS60191140A (en) * 1984-03-12 1985-09-28 Hitachi Ltd Dehumidifying drier
KR100675900B1 (en) * 2004-10-05 2007-01-29 류경륜 Refrigeration and air conditioning system
KR101224157B1 (en) * 2012-08-21 2013-01-22 유경윤 Heatpump type dehumidifier apparatus
CN202955786U (en) * 2011-12-06 2013-05-29 高国栋 Air conditioning equipment with dehumidification and heating function and dehumidification system
CN203083033U (en) * 2013-01-15 2013-07-24 广东省建筑科学研究院 Double-cold-source dehumidification air conditioner unit
CN203928478U (en) * 2014-05-16 2014-11-05 上海伯涵热能科技有限公司 A kind of low condensing pressure degree of depth is crossed cold high-efficiency dehumidifier
TWI528001B (en) * 2013-01-29 2016-04-01 Mitsubishi Electric Corp Dehumidification device

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0587417A (en) * 1991-09-26 1993-04-06 Hitachi Air Conditioning & Refrig Co Ltd Dehumidifying device
JP2003172557A (en) * 2001-12-06 2003-06-20 Daikin Ind Ltd Air-conditioner
JP5046685B2 (en) * 2007-03-01 2012-10-10 三菱電機株式会社 Dehumidifier
CN102338428A (en) * 2010-07-26 2012-02-01 珠海格力电器股份有限公司 Total heat recovery fresh air dehumidifying unit
JP5452565B2 (en) * 2011-10-27 2014-03-26 三菱電機株式会社 Dehumidifier
CN203671981U (en) * 2012-12-21 2014-06-25 三菱电机株式会社 Cooling circulating device
KR102184544B1 (en) * 2014-10-16 2020-11-30 엘지전자 주식회사 Dehumidifier

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52135354U (en) * 1976-04-09 1977-10-14
JPS60191140A (en) * 1984-03-12 1985-09-28 Hitachi Ltd Dehumidifying drier
KR100675900B1 (en) * 2004-10-05 2007-01-29 류경륜 Refrigeration and air conditioning system
CN202955786U (en) * 2011-12-06 2013-05-29 高国栋 Air conditioning equipment with dehumidification and heating function and dehumidification system
KR101224157B1 (en) * 2012-08-21 2013-01-22 유경윤 Heatpump type dehumidifier apparatus
CN203083033U (en) * 2013-01-15 2013-07-24 广东省建筑科学研究院 Double-cold-source dehumidification air conditioner unit
TWI528001B (en) * 2013-01-29 2016-04-01 Mitsubishi Electric Corp Dehumidification device
CN203928478U (en) * 2014-05-16 2014-11-05 上海伯涵热能科技有限公司 A kind of low condensing pressure degree of depth is crossed cold high-efficiency dehumidifier

Also Published As

Publication number Publication date
CN110139700B (en) 2021-11-26
JP6644173B2 (en) 2020-02-12
CN110139700A (en) 2019-08-16
TW201825838A (en) 2018-07-16
JPWO2018131121A1 (en) 2019-06-27
WO2018131121A1 (en) 2018-07-19

Similar Documents

Publication Publication Date Title
TWI671494B (en) Dehumidifier
US20200378660A1 (en) Multistage, Microchannel Condensers with Displaced Manifolds for Use in HVAC Systems
US8205470B2 (en) Indoor unit for air conditioner
US9702637B2 (en) Heat exchanger, indoor unit, and refrigeration cycle apparatus
CN108139088B (en) Air conditioner
JP6466047B1 (en) Heat exchanger and air conditioner
EP1757869A2 (en) Heat exchanger for air conditioner having different circuit pattern depending on distance from fan
TW202043684A (en) Dehumidifier
EP3825628B1 (en) Refrigeration cycle device
CN111512099B (en) Heat exchanger and refrigeration cycle device
JP7394993B2 (en) dehumidifier
KR20190050652A (en) Air Conditioner
CN111448423B (en) Air conditioner
TWI810896B (en) Dehumidifier
WO2022224416A1 (en) Dehumidifying device
JP7394722B2 (en) dehumidifier
KR20150098141A (en) Heat exchanger and air conditional having the same
JP7561878B2 (en) Dehumidifier
EP4141348A1 (en) Refrigeration cycle device
JP7450807B2 (en) air conditioner
JP7050538B2 (en) Heat exchanger and air conditioner
JP2018048769A (en) Heat exchanger
KR20150103579A (en) Heat exchanger and air conditional having the same