TWI528001B - Dehumidification device - Google Patents
Dehumidification device Download PDFInfo
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- TWI528001B TWI528001B TW102108590A TW102108590A TWI528001B TW I528001 B TWI528001 B TW I528001B TW 102108590 A TW102108590 A TW 102108590A TW 102108590 A TW102108590 A TW 102108590A TW I528001 B TWI528001 B TW I528001B
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/147—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification with both heat and humidity transfer between supplied and exhausted air
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/343—Heat recovery
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F11/00—Control or safety arrangements
- F24F11/89—Arrangement or mounting of control or safety devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
- F24F3/1423—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B13/00—Compression machines, plants or systems, with reversible cycle
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/65—Employing advanced heat integration, e.g. Pinch technology
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/144—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/144—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only
- F24F2003/1446—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only by condensing
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Description
本發明係有關於一種除濕裝置。 The present invention relates to a dehumidification apparatus.
以往，在將乾燥劑與熱泵組合的除濕裝置，提議具有如下之構件者，2條風路，係相對濕度相異的空氣流動，並彼此被劃分；及乾燥劑材料，係轉動自如地配置成跨在該2條風路，並載持進行水分之吸附、脫附的吸附劑(例如，參照專利文獻1)。 Conventionally, in a dehumidifying device that combines a desiccant and a heat pump, it is proposed to have the following components, two air passages, which are different in relative humidity, and are divided into each other; and the desiccant material is rotatably arranged The adsorbent which adsorbs and desorbs moisture is carried in the two air passages (for example, refer patent document 1).
在專利文獻1所記載之技術係藉由使構成圓板狀之乾燥劑材料轉動，因應於風路的相對濕度，產生吸附空氣中之水分的吸附反應及將所吸附之水分脫附於空氣的脫附反應。 The technique described in Patent Document 1 generates an adsorption reaction for adsorbing moisture in the air and desorbs the adsorbed moisture to the air by rotating the desiccant material constituting the disk shape in response to the relative humidity of the air passage. Desorption reaction.
又，在專利文獻1所記載之技術係為了利用從熱泵所產生之凝結熱的一部分，而將風路二分割，使通過乾燥劑材料之空氣的相對濕度降低，以促進脫附反應，而剩下的凝結熱係直接向除濕對象空間排出。 Further, in the technique described in Patent Document 1, in order to utilize a part of the heat of condensation generated from the heat pump, the air passage is divided into two, and the relative humidity of the air passing through the desiccant material is lowered to promote the desorption reaction. The lower condensation heat is directly discharged to the dehumidification object space.
[專利文獻1]日本專利4649967號(例如申請專利範圍第1項) [Patent Document 1] Japanese Patent No. 4,649,967 (for example, Patent Application No. 1)
專利文獻1所記載之技術係藉由使乾燥劑材料轉動，而產生吸附反應及脫附反應。因此，在作為乾燥劑材料的轉動機構，例如需要馬達等，而具有製造費用增加、或耗電力增大、或機器構成變得複雜的課題。 The technique described in Patent Document 1 generates an adsorption reaction and a desorption reaction by rotating a desiccant material. Therefore, in the rotating mechanism as the desiccant material, for example, a motor or the like is required, and there is a problem that the manufacturing cost increases, the power consumption increases, or the machine configuration becomes complicated.
在專利文獻1所記載之技術係設置彼此被劃分的2條風路。在風路間空氣洩漏時，因所洩漏的空氣而在阻礙吸附反應或脫附反應的方向作用。因此，配置成跨在2條風路之乾燥劑材料係被設置成與跨在風路的部分接觸。 In the technique described in Patent Document 1, two air passages that are divided from each other are provided. When the air leaks between the wind passages, it acts in a direction that hinders the adsorption reaction or the desorption reaction due to the leaked air. Therefore, the desiccant material configured to straddle the two air paths is placed in contact with the portion that straddles the air path.
即，因為在專利文獻1所記載之技術係為了避免風路間之空氣的洩漏，而乾燥劑材料與劃分風路的部分滑動，所以因滑動而馬達扭力需要變大、而具有耗電力變大的課題。 In other words, in the technique described in Patent Document 1, in order to prevent leakage of air between the air passages, the desiccant material and the portion dividing the air passage are slid, so that the motor torque needs to be increased due to the sliding, and the power consumption is increased. Question.
因為在專利文獻1所記載之技術係乾燥劑材料與劃分風路的部分滑動，所以構件彼此相摩擦而受損，因風路間之空氣的洩漏，而具有吸附及脫附之效率降低的課題，而且需要用以修補該損傷的維修，而具有耗費上漲的課題。 In the technique described in Patent Document 1, the desiccant material and the portion dividing the air passage are slid, so that the members are rubbed against each other and damaged, and the efficiency of adsorption and desorption is lowered due to leakage of air between the air passages. And it is necessary to repair the repair of the damage, and it has a problem of rising costs.
因為在專利文獻1所記載之技術係將凝結熱的一部分用作乾燥劑之脫附反應的熱源，所以需要2條風路，而具有機器構成變得複雜的課題，而且因為壓力損失增加，風扇之動力增加，而具有耗電力增加的課題。 In the technique described in Patent Document 1, a part of the heat of condensation is used as a heat source for the desorption reaction of the desiccant. Therefore, two air passages are required, which has a problem that the machine configuration is complicated, and the fan is increased in pressure loss. The power is increased, and there is a problem of increasing power consumption.
在專利文獻1所記載之技術係在外氣溫度低時驅動附設於室外熱交換器的加熱器，抑制室外熱交換器的著霜。可是，在露點溫度成為冰點以下的情況，因為難抑制在熱交換器所產生之著霜，所以需要除霜運轉，而具有每小時之除濕量 大為降低的課題。 The technique described in Patent Document 1 drives a heater attached to an outdoor heat exchanger when the outside air temperature is low, and suppresses frosting of the outdoor heat exchanger. However, when the dew point temperature is below the freezing point, it is difficult to suppress the frost generated in the heat exchanger, so the defrosting operation is required, and the dehumidification amount per hour is required. A problem that is greatly reduced.
本發明係為了解決如上述所示之課題中的至少一個而開發的，其目的在於提供一種除濕裝置，該除濕裝置係用以實現抑制費用上升、抑制耗電力、抑制機器構成之複雜化、及抑制吸附、脫附之效率的降低。 The present invention has been made in order to solve at least one of the problems described above, and an object of the invention is to provide a dehumidifying apparatus for suppressing an increase in cost, suppressing power consumption, and suppressing complication of a device configuration, and Reduce the efficiency of adsorption and desorption.
本發明之除濕裝置係包括：從除濕對象空間取入之空氣所流動的第1風路；送風手段，係將除濕對象空間的空氣取入第1風路；水分吸附手段，係設置於第1風路內，並進行在第1風路流動的空氣所含之水分的吸附、及將本身所吸附之水分脫附於在第1風路流動的空氣；第1熱交換器，係設置於比水分吸附手段更靠近第1風路之空氣流動方向的上游側，並使空氣與冷媒進行熱交換；第2熱交換器，係設置於比水分吸附手段更靠近第1風路之空氣流動方向的下游側，並使空氣與冷媒進行熱交換；第3熱交換器，係設置於比第2熱交換器更靠近第1風路之空氣流動方向的下游側，並使空氣與冷媒進行熱交換；第1節流手段，係設置於第1熱交換器與第2熱交換器之間，並使冷媒降壓；及壓縮機，係排出側與第3熱交換器連接，並壓縮冷媒；使第1熱交換器及第2熱交換器選擇性地作為凝結器及蒸發器發揮功能。 The dehumidifying apparatus according to the present invention includes: a first air passage through which air taken in from the space to be dehumidified; and a blowing means for taking air from the space to be dehumidified into the first air passage; and a moisture adsorbing means being provided in the first In the air passage, the moisture contained in the air flowing through the first air passage is adsorbed, and the water adsorbed by itself is desorbed to the air flowing through the first air passage; the first heat exchanger is set in the ratio The moisture adsorption means is disposed closer to the upstream side of the air flow direction of the first air passage and exchanges heat between the air and the refrigerant, and the second heat exchanger is disposed closer to the air flow direction of the first air passage than the moisture adsorption means. a downstream side that exchanges heat between the air and the refrigerant; and a third heat exchanger disposed downstream of the air flow direction of the first air passage than the second heat exchanger to exchange heat between the air and the refrigerant; The first throttling means is disposed between the first heat exchanger and the second heat exchanger to depressurize the refrigerant, and the compressor is connected to the third heat exchanger by the discharge side, and compresses the refrigerant; 1 heat exchanger and second heat exchanger selectivity As the condenser and evaporator function.
若依據本發明之除濕裝置，因為具有該構成，所以可抑制費用上升、抑制耗電力、抑制機器構成之複雜化、及抑制吸附、脫附之效率的降低。 According to the dehumidifying apparatus of the present invention, it is possible to suppress an increase in cost, suppress power consumption, suppress complication of the device configuration, and suppress a decrease in efficiency of adsorption and desorption.
1a~1f‧‧‧溫濕度感測器 1a~1f‧‧‧temperature and humidity sensor
2‧‧‧風速感測器 2‧‧‧Wind speed sensor
3a~3h‧‧‧溫度感測器 3a~3h‧‧‧temperature sensor
4‧‧‧控制電路 4‧‧‧Control circuit
11‧‧‧熱交換器 11‧‧‧ heat exchanger
11a‧‧‧第1熱交換器 11a‧‧‧1st heat exchanger
11b‧‧‧第2熱交換器 11b‧‧‧2nd heat exchanger
11c‧‧‧第3熱交換器 11c‧‧‧3rd heat exchanger
12‧‧‧送風手段 12‧‧‧Air supply means
12a‧‧‧第1送風手段 12a‧‧‧1st air supply means
12b‧‧‧第2送風手段 12b‧‧‧2nd air supply means
13‧‧‧壓縮機 13‧‧‧Compressor
14‧‧‧節流手段 14‧‧‧Throttle means
14a‧‧‧第2節流手段 14a‧‧‧2nd throttling means
14b‧‧‧第1節流手段 14b‧‧‧1st throttling means
14c‧‧‧第3節流手段 14c‧‧‧3rd throttling means
14d‧‧‧第4節流手段 14d‧‧‧4th throttling means
15‧‧‧四通閥(冷媒流路切換手段) 15‧‧‧ four-way valve (refrigerant flow path switching means)
16‧‧‧水分吸附手段 16‧‧‧Water adsorption means
50‧‧‧第1風路 50‧‧‧1st wind road
51‧‧‧第2風路 51‧‧‧2nd wind road
100‧‧‧除濕單元 100‧‧‧Dehumidification unit
200‧‧‧散熱單元 200‧‧‧heating unit
300‧‧‧除濕裝置 300‧‧‧Dehumidification device
A‧‧‧冷媒迴路 A‧‧‧ refrigerant circuit
第1圖係表示本發明之第1實施形態之除濕裝置的示意構成圖。 Fig. 1 is a schematic configuration diagram of a dehumidifying apparatus according to a first embodiment of the present invention.
第2圖係表示本發明之第1實施形態的水分吸附手段之相對相對濕度的飽和水分吸附量之轉移的吸附等溫線圖。 Fig. 2 is an adsorption isotherm diagram showing the transition of the saturated moisture adsorption amount with respect to the relative humidity of the moisture adsorption means according to the first embodiment of the present invention.
第3圖係本發明之第1實施形態的除濕裝置之測量控制系統的構成圖。 Fig. 3 is a configuration diagram of a measurement control system of the dehumidifying apparatus according to the first embodiment of the present invention.
第4圖係表示本發明之第1實施形態的除濕裝置之在各模式之溫濕度轉移的濕空氣線圖。 Fig. 4 is a wet air diagram showing the temperature and humidity shift in each mode of the dehumidifying apparatus according to the first embodiment of the present invention.
第5圖係表示本發明之第2實施形態之除濕裝置的示意構成圖。 Fig. 5 is a schematic configuration diagram of a dehumidifying apparatus according to a second embodiment of the present invention.
第6圖係表示本發明之第2實施形態的除濕裝置之在各模式之溫濕度轉移的濕空氣線圖。 Fig. 6 is a wet air diagram showing the temperature and humidity shift in each mode of the dehumidifying apparatus according to the second embodiment of the present invention.
第7圖係本發明之第3實施形態的除濕裝置之示意構成圖。 Fig. 7 is a schematic configuration diagram of a dehumidifying apparatus according to a third embodiment of the present invention.
第8圖係表示本發明之第3實施形態的除濕裝置之冷媒壓力與焓之變動的莫理爾線圖。 Fig. 8 is a Mollier diagram showing changes in refrigerant pressure and enthalpy of the dehumidifying apparatus according to the third embodiment of the present invention.
第9圖係本發明之第4實施形態的除濕裝置之示意構成圖。 Fig. 9 is a schematic configuration diagram of a dehumidifying apparatus according to a fourth embodiment of the present invention.
第10圖係表示本發明之第4實施形態的除濕裝置之在各模式之溫濕度轉移的濕空氣線圖。 Fig. 10 is a wet air diagram showing the temperature and humidity shift in each mode of the dehumidifying apparatus according to the fourth embodiment of the present invention.
以下，根據圖面，說明本發明之實施形態。 Hereinafter, embodiments of the present invention will be described based on the drawings.
第1圖係第1實施形態之除濕裝置300的示意構成圖。第2圖係表示第1實施形態之除濕裝置300的水分吸附手段16之相對相對濕度的飽和水分吸附量之轉移的吸附等溫線圖。第3圖係第1實施形態的除濕裝置300之測量控制系統的構成圖。參照第1圖~第3圖，說明除濕裝置300的構成等。 Fig. 1 is a schematic configuration diagram of a dehumidifying apparatus 300 according to the first embodiment. Fig. 2 is an adsorption isotherm diagram showing the transition of the saturated moisture adsorption amount with respect to the relative humidity of the moisture adsorbing means 16 of the dehumidifying apparatus 300 of the first embodiment. Fig. 3 is a configuration diagram of a measurement control system of the dehumidifying apparatus 300 of the first embodiment. The configuration of the dehumidifying apparatus 300 and the like will be described with reference to Figs. 1 to 3 .
本第1實施形態之除濕裝置300係被施加可抑制費用上升、抑制耗電力、抑制機器構成之複雜化、及抑制吸附、脫附之效率之降低的改良。 In the dehumidifier 300 of the first embodiment, it is possible to suppress an increase in cost, suppress power consumption, suppress complication of the device configuration, and improve the efficiency of suppressing adsorption and desorption.
除濕裝置300具有：對冷媒壓縮的壓縮機13、作為凝結器或蒸發器發揮功能的第1熱交換器11a與第2熱交換器11b、作為凝結器發揮功能的第3熱交換器11c、使凝結後之冷媒降壓的節流手段14、及切換冷媒流路的四通閥15。以冷媒配管連接該壓縮機13、第1熱交換器11a、第2熱交換器11b、第3熱交換器11c、節流手段14及四通閥15，而構成冷媒迴路A。 The dehumidifying device 300 includes a compressor 13 that compresses a refrigerant, a first heat exchanger 11a and a second heat exchanger 11b that function as a condenser or an evaporator, and a third heat exchanger 11c that functions as a condenser. The throttling means 14 for reducing the pressure of the refrigerant after condensation and the four-way valve 15 for switching the refrigerant flow path. The compressor 13, the first heat exchanger 11a, the second heat exchanger 11b, the third heat exchanger 11c, the throttle means 14, and the four-way valve 15 are connected by a refrigerant pipe to constitute a refrigerant circuit A.
此外，在以下的說明，有將第1熱交換器11a、第2熱交換器11b及第3熱交換器11c合在一起總稱為熱交換器11的情況。 In the following description, the first heat exchanger 11a, the second heat exchanger 11b, and the third heat exchanger 11c may be collectively referred to as a heat exchanger 11.
除濕裝置300具有：水分吸附手段16，係進行水分的吸附及脫附；及送風手段12，係將空氣供給至熱交換器11及水分吸附手段16。 The dehumidifying apparatus 300 includes a moisture adsorbing means 16 for adsorbing and desorbing moisture, and a blowing means 12 for supplying air to the heat exchanger 11 and the moisture adsorbing means 16.
除濕裝置300具有：溫濕度感測器1a~1e，係用以檢測出空氣的溫度及濕度；風速感測器2，係用以檢測出風速；溫度感測器3a~3h，係用以檢測出冷媒的溫度；及控制電路4，係根據溫濕度感測器1a~1e、風速感測器2及溫度感測器3a~3h的檢測結果，切換四通閥15等。 The dehumidifying device 300 has a temperature and humidity sensor 1a~1e for detecting the temperature and humidity of the air, a wind speed sensor 2 for detecting the wind speed, and a temperature sensor 3a~3h for detecting The temperature of the refrigerant is discharged; and the control circuit 4 switches the four-way valve 15 and the like based on the detection results of the temperature and humidity sensors 1a to 1e, the wind speed sensor 2, and the temperature sensors 3a to 3h.
除濕裝置300具有至少設置熱交換器11及水分吸附手段16之省略圖示的風路(第1風路50)。在除濕裝置300之該風路的上游側係設置空氣吸入口，該空氣吸入口係與除濕對象空間連通，並用以將除濕對象空間的空氣取入風路內。又，在除濕裝置300之該風路的下游側係設置空氣排出口，該空氣排出口係與除濕對象空間連通，並用以將以除濕裝置300除濕後的空氣排出至除濕對象空間。此外，在第1圖，以實線箭號表示第1風路50之空氣的流動。 The dehumidifying apparatus 300 has an air passage (first air passage 50) (not shown) that is provided with at least the heat exchanger 11 and the moisture adsorbing means 16. An air intake port is provided on the upstream side of the air passage of the dehumidifying device 300, and the air suction port communicates with the dehumidification object space, and is used to take air from the dehumidification object space into the air passage. Further, an air discharge port is provided on the downstream side of the air passage of the dehumidifying device 300, and the air discharge port communicates with the dehumidification target space to discharge the air dehumidified by the dehumidifying device 300 to the dehumidification target space. Further, in Fig. 1, the flow of the air in the first air passage 50 is indicated by a solid arrow.
壓縮機13係排出側與第3熱交換器11c連接，吸入側與四通閥15連接。壓縮機13係例如可由藉馬達(未圖示)所驅動之容積式壓縮機構成。此外，壓縮機13的台數未限定為一台，亦可是2台以上之壓縮機所並聯或串聯者。 The discharge side of the compressor 13 is connected to the third heat exchanger 11c, and the suction side is connected to the four-way valve 15. The compressor 13 can be constituted, for example, by a positive displacement compressor driven by a motor (not shown). Further, the number of the compressors 13 is not limited to one, and two or more compressors may be connected in parallel or in series.
第1熱交換器11a及第2熱交換器11b係一方與節流手段14連接，另一方與四通閥15連接。即，第1熱交換器11a、節流手段14及第2熱交換器11b串聯。 The first heat exchanger 11a and the second heat exchanger 11b are connected to the throttle means 14 and the other to the four-way valve 15. That is, the first heat exchanger 11a, the throttle means 14 and the second heat exchanger 11b are connected in series.
第3熱交換器11c係一方與壓縮機13的排出側連接，另一方與四通閥15連接。此外，從空氣流動方向的上游側依序 配置第1熱交換器11a、第2熱交換器11b及第3熱交換器11c。 The third heat exchanger 11c is connected to the discharge side of the compressor 13 and the other to the four-way valve 15. In addition, from the upstream side of the air flow direction The first heat exchanger 11a, the second heat exchanger 11b, and the third heat exchanger 11c are disposed.
熱交換器11係例如可由藉導熱管與多個散熱片所構成之交叉散熱片式的翅管式熱交換器等所構成。 The heat exchanger 11 can be constituted, for example, by a fin-and-tube heat exchanger having a cross fin type composed of a heat transfer tube and a plurality of fins.
節流手段14係使冷媒降壓者。節流手段14係一方與第1熱交換器11a連接，另一方與第2熱交換器11b連接。 The throttling means 14 is to lower the refrigerant. The throttle means 14 is connected to the first heat exchanger 11a and the other to the second heat exchanger 11b.
節流手段14係可調整在冷媒迴路內流動之冷媒的流量等，係可藉步進馬達(未圖示)調整節流器之開口大小的電子式膨脹閥或在受壓部採用隔膜之機械式膨脹閥或毛細管。 The throttle means 14 is capable of adjusting the flow rate of the refrigerant flowing through the refrigerant circuit, etc., and is an electronic expansion valve which can adjust the opening size of the throttle by a stepping motor (not shown) or a diaphragm which is a diaphragm in the pressure receiving portion. Expansion valve or capillary.
四通閥15係切換冷媒流路，而可切換成冷媒迴路A之冷媒的流動者。四通閥15係未與第1熱交換器11a中之節流手段14連接的一側、未與第2熱交換器11b中之節流手段14連接的一側、未與第3熱交換器11c中之壓縮機之排出側連接的一側及和壓縮機13的吸入側連接。 The four-way valve 15 switches the refrigerant flow path and switches to the flow of the refrigerant of the refrigerant circuit A. The four-way valve 15 is a side that is not connected to the throttle means 14 in the first heat exchanger 11a, a side that is not connected to the throttle means 14 in the second heat exchanger 11b, and a third heat exchanger. One side of the discharge side of the compressor in 11c is connected to the suction side of the compressor 13.
四通閥15係在後述之第1運轉模式時，切換成將第3熱交換器11c與第2熱交換器11b連接，而且將第1熱交換器11a與壓縮機13的吸入側連接。 When the four-way valve 15 is in the first operation mode described later, the fourth heat exchanger 11c is connected to the second heat exchanger 11b, and the first heat exchanger 11a is connected to the suction side of the compressor 13.
又，四通閥15係在後述之第2運轉模式時，切換成將第3熱交換器11c與第1熱交換器11a連接，而且將第2熱交換器11b與壓縮機13的吸入側連接。 Further, when the four-way valve 15 is in the second operation mode to be described later, the fourth heat exchanger 11c is connected to the first heat exchanger 11a, and the second heat exchanger 11b is connected to the suction side of the compressor 13. .
送風手段12係將空氣取入設置熱交換器11及水分吸附手段16的風路，並將風路所取入之空氣供給至除濕對 象空間。送風手段12係在第1圖，圖示成配置於第3熱交換器11c之空氣流動方向的下游側，但是未限定如此，例如亦可是第1熱交換器11a的上游側。 The air blowing means 12 takes in air into the air path in which the heat exchanger 11 and the moisture adsorbing means 16 are provided, and supplies the air taken in by the air path to the dehumidifying pair. Like space. The air blowing means 12 is shown in Fig. 1 and is disposed on the downstream side in the air flow direction of the third heat exchanger 11c. However, the present invention is not limited thereto, and may be, for example, the upstream side of the first heat exchanger 11a.
送風手段12係可由可改變通過除濕裝置300內的風路之空氣之流量的風扇，例如可由藉DC風扇馬達等之馬達所驅動的離心式風扇或多翼風扇等所構成。 The air blowing means 12 is a fan which can change the flow rate of the air passing through the air path in the dehumidifying apparatus 300, for example, a centrifugal fan or a multi-blade fan driven by a motor such as a DC fan motor.
水分吸附手段16係為了可確保更寬之相對除濕裝置300之風路截面積的通風截面積，例如作成對應於風路截面的形狀。例如，若風路截面是四角形，則將水分吸附手段16之通風截面作成四角形，若風路截面是六角形，則將水分吸附手段16之通風截面作成六角形。 The moisture adsorbing means 16 is formed in a shape corresponding to the cross section of the air passage, for example, in order to secure a wider ventilation cross-sectional area of the air passage cross-sectional area of the dehumidifying apparatus 300. For example, if the cross section of the air passage is a quadrangular shape, the ventilation cross section of the moisture adsorbing means 16 is formed into a quadrangular shape, and if the cross section of the air passage is hexagonal, the ventilation cross section of the moisture adsorbing means 16 is formed into a hexagonal shape.
水分吸附手段16係具有以第1風路50之空氣通過的方式所形成之複數個透孔的通風體。水分吸附手段16係例如為多孔質平板等，並構成為在厚度方向空氣可通過。 The moisture adsorbing means 16 is a venting body having a plurality of through holes formed so that the air of the first air passage 50 passes therethrough. The moisture adsorbing means 16 is, for example, a porous flat plate or the like, and is configured to allow air to pass through in the thickness direction.
此外，水分吸附手段16係使用在多孔質平板的表面，將如沸石、矽膠、活性碳等具有從濕度比較高的空氣吸濕後對濕度比較低的空氣放出濕氣之特性的吸附劑進行塗布、表面處理、或浸漬者。 Further, the moisture adsorbing means 16 is applied to the surface of the porous flat plate, and is coated with an adsorbent having characteristics of releasing moisture from a relatively low humidity air such as zeolite, tannin, or activated carbon, which is moisturized by air having a relatively high humidity. , surface treatment, or impregnation.
此外，水分吸附手段16係不是如以往以馬達等轉動者，而是固定於第1風路50。 Further, the moisture adsorbing means 16 is not fixed to the first air passage 50 as in the conventional case of being rotated by a motor or the like.
水分吸附手段16所使用之吸附劑可對空氣之相對濕度吸附的水量(平衡吸附量)係如第2圖所示。平衡吸附量係一般空氣之相對濕度變高時增加。水分吸附手段16所使用之 吸附劑使用相對濕度為80%以上之平衡吸附量與相對濕度為40~60%之平衡吸附量的差大的吸附劑。藉此，可提高水分吸附手段16的吸附及脫附容量。 The amount of water (balanced adsorption amount) which the adsorbent used in the moisture adsorption means 16 can adsorb to the relative humidity of the air is as shown in Fig. 2. The equilibrium adsorption amount is increased when the relative humidity of the air becomes high. Used by the moisture adsorption means 16 The adsorbent uses an adsorbent having a difference in equilibrium adsorption amount of 80% or more and a relative adsorption amount of 40 to 60% relative humidity. Thereby, the adsorption and desorption capacity of the moisture adsorbing means 16 can be improved.
溫濕度感測器1a~1e係檢測出風路內之乾球溫度、相對濕度、露出溫度、絕對濕度、濕球溫度的感測器。 The temperature and humidity sensors 1a to 1e are sensors for detecting dry bulb temperature, relative humidity, exposed temperature, absolute humidity, and wet bulb temperature in the air passage.
溫濕度感測器1a係檢測出被取入除濕裝置300並在通過第1熱交換器11a之前之空氣的溫濕度。溫濕度感測器1b係檢測出通過第1熱交換器11a後之溫濕度。溫濕度感測器1c係檢測出通過水分吸附手段16後之空氣的溫濕度。溫濕度感測器1d係檢測出通過第2熱交換器11b後之溫濕度。溫濕度感測器1e係檢測出通過第3熱交換器11c後之溫濕度。而且，這些溫濕度感測器1a~1e係與控制除濕裝置300的控制電路4連接。 The temperature and humidity sensor 1a detects the temperature and humidity of the air taken into the dehumidifying apparatus 300 and before passing through the first heat exchanger 11a. The temperature and humidity sensor 1b detects the temperature and humidity after passing through the first heat exchanger 11a. The temperature and humidity sensor 1c detects the temperature and humidity of the air after passing through the moisture adsorbing means 16. The temperature and humidity sensor 1d detects the temperature and humidity after passing through the second heat exchanger 11b. The temperature and humidity sensor 1e detects the temperature and humidity after passing through the third heat exchanger 11c. Further, these temperature and humidity sensors 1a to 1e are connected to a control circuit 4 that controls the dehumidifying device 300.
風速感測器2係設置於除濕裝置300的第1風路50，並檢測出第1風路50內的通過空氣風量。風速感測器2係如第1圖所示，作為配置於送風手段12之下游側者說明，但是未限定如此，只要可檢測出通過第1風路50之風量，配置於第1風路50之任一位置都可。而且，風速感測器2係與控制除濕裝置300的控制電路4連接。 The wind speed sensor 2 is installed in the first air passage 50 of the dehumidifying device 300, and detects the passing air volume in the first air passage 50. As shown in FIG. 1 , the wind speed sensor 2 is described as being disposed on the downstream side of the air blowing means 12, but is not limited thereto, and is disposed in the first air path 50 as long as the air volume passing through the first air passage 50 can be detected. Any position is fine. Further, the wind speed sensor 2 is connected to the control circuit 4 that controls the dehumidifying device 300.
溫度感測器3a~3h係檢測出冷媒的溫度。 The temperature sensors 3a to 3h detect the temperature of the refrigerant.
溫度感測器3a係在壓縮機13的排出側所具有，並檢測出 從壓縮機13所排出之冷媒的溫度。溫度感測器3b係在壓縮機13的吸入側所具有，並檢測出壓縮機13所吸入之冷媒的溫度。 The temperature sensor 3a is provided on the discharge side of the compressor 13, and is detected The temperature of the refrigerant discharged from the compressor 13. The temperature sensor 3b is provided on the suction side of the compressor 13, and detects the temperature of the refrigerant sucked by the compressor 13.
溫度感測器3c係在第3熱交換器11c之冷媒流入側的配管所具有，並檢測出流入第3熱交換器11c之冷媒的溫度。溫度感測器3d係在第3熱交換器11c之冷媒流出側的配管所具有，並檢測出在第3熱交換器11c所流出之冷媒的溫度。 The temperature sensor 3c is provided in the piping on the refrigerant inflow side of the third heat exchanger 11c, and detects the temperature of the refrigerant flowing into the third heat exchanger 11c. The temperature sensor 3d is provided in the piping on the refrigerant outflow side of the third heat exchanger 11c, and detects the temperature of the refrigerant flowing out of the third heat exchanger 11c.
溫度感測器3e係在第2熱交換器11b之一側的配管所具有，並檢測出在第2熱交換器11b所流入、流出之冷媒的溫度。溫度感測器3f係在第2熱交換器11b之另一側的配管所具有，並檢測出在第2熱交換器11b所流入、流出之冷媒的溫度。 The temperature sensor 3e is provided in a pipe on one side of the second heat exchanger 11b, and detects the temperature of the refrigerant flowing in and out of the second heat exchanger 11b. The temperature sensor 3f is provided in a pipe on the other side of the second heat exchanger 11b, and detects the temperature of the refrigerant flowing in and out of the second heat exchanger 11b.
溫度感測器3g係在第1熱交換器11a之一側的配管所具有，並檢測出在第1熱交換器11a所流入、流出之冷媒的溫度。溫度感測器3h係在第1熱交換器11a之另一側的配管所具有，並檢測出在第1熱交換器11a所流入、流出之冷媒的溫度。 The temperature sensor 3g is provided in a pipe on one side of the first heat exchanger 11a, and detects the temperature of the refrigerant flowing in and out of the first heat exchanger 11a. The temperature sensor 3h is provided in a pipe on the other side of the first heat exchanger 11a, and detects the temperature of the refrigerant flowing into and out of the first heat exchanger 11a.
而且，這些溫度感測器3a~3h係與控制除濕裝置300的控制電路4連接。 Further, these temperature sensors 3a to 3h are connected to the control circuit 4 that controls the dehumidifying device 300.
控制電路4係根據溫濕度感測器1a~1e、風速感測器2及溫度感測器3a~3h的檢測結果，控制四通閥15的切換、壓縮機13的頻率、送風手段12的轉速及節流手段14之開口大小等。 The control circuit 4 controls the switching of the four-way valve 15, the frequency of the compressor 13, and the rotational speed of the air blowing means 12 based on the detection results of the temperature and humidity sensors 1a to 1e, the wind speed sensor 2, and the temperature sensors 3a to 3h. And the opening size of the throttling means 14 and the like.
依此方式，除濕裝置300係將系統構成為空氣的溫濕度及風速、冷媒溫度的資訊被輸出至控制電路4，並可控制節流手段14、送風手段12及四通閥15等之動作。 In this manner, the dehumidifying apparatus 300 is configured to output information on the temperature and humidity of the air, the wind speed, and the temperature of the refrigerant to the control circuit 4, and to control the operations of the throttle means 14, the air blowing means 12, the four-way valve 15, and the like.
冷媒迴路A所使用之冷媒係例如有R410A、R407A、R404A等之HFC冷媒、R22、R134a等之HCFC冷媒、或如碳化氫、氦之自然冷媒。 The refrigerant used in the refrigerant circuit A is, for example, an HFC refrigerant such as R410A, R407A or R404A, an HCFC refrigerant such as R22 or R134a, or a natural refrigerant such as hydrocarbon or hydrazine.
冷媒迴路之運轉模式係根據四通閥15的切換而有2種，在第1運轉模式，冷媒按照壓縮機13、第3熱交換器11c、四通閥15、第2熱交換器11b、節流手段14、第1熱交換器11a及四通閥15的順序流動，再流入壓縮機。即，在第1運轉模式，冷媒沿著實線流動。 The operation mode of the refrigerant circuit is two depending on the switching of the four-way valve 15. In the first operation mode, the refrigerant is in accordance with the compressor 13, the third heat exchanger 11c, the four-way valve 15, the second heat exchanger 11b, and the section. The flow means 14, the first heat exchanger 11a, and the four-way valve 15 flow in order and flow into the compressor. That is, in the first operation mode, the refrigerant flows along the solid line.
在第2運轉模式，冷媒按照壓縮機13、第3熱交換器11c、四通閥15、第1熱交換器11a、節流手段14、第2熱交換器11b及四通閥15的順序流動，再流入壓縮機。即，在第2運轉模式，冷媒沿著虛線流動。 In the second operation mode, the refrigerant flows in the order of the compressor 13, the third heat exchanger 11c, the four-way valve 15, the first heat exchanger 11a, the throttle means 14, the second heat exchanger 11b, and the four-way valve 15. Then flow into the compressor. That is, in the second operation mode, the refrigerant flows along the broken line.
從壓縮機13所排出的冷媒係向第3熱交換器11c流動。在此時，第3熱交換器11c係作用為凝結器，冷媒係在與空氣進行熱交換時一部分凝結成液體。在通過第3熱交換器11c後，冷媒係通過四通閥15，向第2熱交換器11b流動。第2熱交換器11b係作用為凝結器，冷媒係在與空氣進行熱交換時凝結成液體後，向節流手段14流動。冷媒係在節流手段14被降壓後，流至第1熱交換器11a。第1熱交換器11a係作為蒸發器發揮功能，冷媒係在與空氣進行熱交換而蒸發後，通過四通閥15，再被壓縮機13吸入。 The refrigerant discharged from the compressor 13 flows into the third heat exchanger 11c. At this time, the third heat exchanger 11c functions as a condenser, and the refrigerant partially condenses into a liquid when it exchanges heat with air. After passing through the third heat exchanger 11c, the refrigerant passes through the four-way valve 15 and flows into the second heat exchanger 11b. The second heat exchanger 11b functions as a condenser, and the refrigerant condenses into a liquid when it exchanges heat with air, and then flows to the throttle means 14. The refrigerant is depressurized by the throttle means 14, and then flows to the first heat exchanger 11a. The first heat exchanger 11a functions as an evaporator, and the refrigerant evaporates by exchanging heat with air, passes through the four-way valve 15, and is sucked by the compressor 13.
從壓縮機13所排出的冷媒係向第3熱交換器11c流動。在此時，第3熱交換器11c係作用為凝結器，冷媒係在與空氣進行熱交換時一部分凝結成液體。在通過第3熱交換器11c後，冷媒係通過四通閥15，向第1熱交換器11a流動。第1熱交換器11a係作用為凝結器，冷媒係在與空氣進行熱交換時凝結成液體後，向節流手段14流動。冷媒係在節流手段14被降壓後，流至第2熱交換器11b。第2熱交換器11b係作為蒸發器發揮功能，冷媒係在與空氣進行熱交換而蒸發後，通過四通閥15，再被壓縮機13吸入。 The refrigerant discharged from the compressor 13 flows into the third heat exchanger 11c. At this time, the third heat exchanger 11c functions as a condenser, and the refrigerant partially condenses into a liquid when it exchanges heat with air. After passing through the third heat exchanger 11c, the refrigerant passes through the four-way valve 15 and flows into the first heat exchanger 11a. The first heat exchanger 11a functions as a condenser, and the refrigerant condenses into a liquid when it exchanges heat with air, and then flows to the throttle means 14. The refrigerant is depressurized by the throttle means 14, and then flows to the second heat exchanger 11b. The second heat exchanger 11b functions as an evaporator, and the refrigerant is evaporated by heat exchange with air, and then passed through the four-way valve 15 and sucked by the compressor 13.
依此方式，本第1實施形態的除濕裝置300係使第1熱交換器11a及第2熱交換器11b選擇性地作為凝結器及蒸發器發揮功能。即，在第1運轉模式時，使第1熱交換器11a作為蒸發器發揮功能，並使第2熱交換器11b作為凝結器發揮功能。又，在第2運轉模式時，使第1熱交換器11a作為凝結器發揮功能，並使第2熱交換器11b作為蒸發器發揮功能。 In the dehumidifier 300 of the first embodiment, the first heat exchanger 11a and the second heat exchanger 11b selectively function as a condenser and an evaporator. In other words, in the first operation mode, the first heat exchanger 11a functions as an evaporator, and the second heat exchanger 11b functions as a condenser. Moreover, in the second operation mode, the first heat exchanger 11a functions as a condenser, and the second heat exchanger 11b functions as an evaporator.
第4圖係表示第1實施形態的除濕裝置300之在各模式之溫濕度轉移的濕空氣線圖。此外，第4圖(a)係在第1運轉模式的濕空氣線圖，第4圖(b)係在第2運轉模式的濕空氣線圖。 Fig. 4 is a wet air diagram showing the temperature and humidity shift of each mode of the dehumidifying apparatus 300 of the first embodiment. In addition, Fig. 4(a) is a wet air diagram in the first operation mode, and Fig. 4(b) is a wet air diagram in the second operation mode.
又，第4圖(a)中之(1-1)~(1-5)係表示在第1運轉模式之通過第1熱交換器11a之前的空氣(1-1)、通過第1熱交換器11a後的空氣(1-2)、通過水分吸附手段16後的空氣(1- 3)、通過第2熱交換器11b後的空氣(1-4)、通過第3熱交換器11c後的空氣(1-5)。 Further, (1-1) to (1-5) in Fig. 4(a) show the air (1-1) before passing through the first heat exchanger 11a in the first operation mode, and the first heat exchange is performed. Air (1-2) after the device 11a, air after passing through the moisture adsorbing means 16 (1- 3) Air (1-4) passing through the second heat exchanger 11b and air (1-5) passing through the third heat exchanger 11c.
又，第4圖(b)中之(2-1)~(2-5)係表示在第2運轉模式之通過第1熱交換器11a之前的空氣(2-1)、通過第1熱交換器11a後的空氣(2-2)、通過水分吸附手段16後的空氣(2-3)、通過第2熱交換器11b後的空氣(2-4)、通過第3熱交換器11c後之空氣(2-5)的狀態。 Further, (2-1) to (2-5) in Fig. 4(b) show the air (2-1) before passing through the first heat exchanger 11a in the second operation mode, and the first heat exchange is performed. Air (2-2) after the device 11a, air (2-3) after passing through the moisture adsorbing means 16, air (2-4) passing through the second heat exchanger 11b, and passing through the third heat exchanger 11c The state of the air (2-5).
參照第4圖，說明在第1運轉模式及第2運轉模式之空氣的狀態。 The state of the air in the first operation mode and the second operation mode will be described with reference to Fig. 4 .
此外，在第4圖(a)，表示水分吸附手段16之水分保持量變少，而對高濕之空氣(例如相對濕度70%以上)進行吸附反應之情況的例子。又，在第4圖(b)，表示水分吸附手段16之水分保持量變多，而對低濕之空氣(例如相對濕度60%以下)進行脫附反應之情況的例子。 In addition, in the fourth diagram (a), an example in which the amount of moisture retained by the moisture adsorbing means 16 is small and the high-humidity air (for example, a relative humidity of 70% or more) is subjected to an adsorption reaction is shown. In addition, in the case of FIG. 4(b), an example in which the moisture retention amount of the moisture adsorbing means 16 is increased and the dehumidification reaction is performed on low-humidity air (for example, a relative humidity of 60% or less) is shown.
在第1運轉模式，自吸入口被取入風路內的空氣(1-1)係被送入第1熱交換器11a。 In the first operation mode, the air (1-1) taken into the air passage from the suction port is sent to the first heat exchanger 11a.
在此，被取入風路內的空氣係藉作用為蒸發器之第1熱交換器11a所冷卻。通過第1熱交換器11a後的空氣係因被冷卻至露點溫度以下，而成為除濕空氣(1-2)後，被送入水分吸附手段16。 Here, the air taken into the air passage is cooled by the first heat exchanger 11a functioning as an evaporator. The air that has passed through the first heat exchanger 11a is cooled to a dew point temperature or lower, and is dehumidified air (1-2), and then sent to the moisture adsorbing means 16.
因為冷卻除濕後之空氣的相對濕度係高達約70~90%RH，所以水分吸附手段16的吸附劑易吸附水分。冷卻後的空氣被水分吸附手段16之吸附劑吸附水分而除濕後，變成高溫低濕， 並流入第2熱交換器11b(1-3)。 Since the relative humidity of the air after cooling and dehumidification is as high as about 70 to 90% RH, the adsorbent of the moisture adsorbing means 16 easily adsorbs moisture. The cooled air is adsorbed by the adsorbent of the moisture adsorbing means 16 and dehumidified, and becomes high temperature and low humidity. The second heat exchanger 11b (1-3) flows into the second heat exchanger 11b.
因為第2熱交換器11b係作為凝結器發揮功能，所以被加熱，而使通過空氣的溫度上升(1-4)。 Since the second heat exchanger 11b functions as a condenser, it is heated to raise the temperature of the passing air (1-4).
通過第2熱交換器11b後的空氣係流入第3熱交換器11c。因為第3熱交換器11c係作為凝結器發揮功能，所以使通過空氣的溫度上升(1-5)，並自排出口被排出至除濕對象空間。 The air that has passed through the second heat exchanger 11b flows into the third heat exchanger 11c. Since the third heat exchanger 11c functions as a condenser, the temperature of the passing air is raised (1-5), and is discharged to the dehumidification target space from the discharge port.
在第2運轉模式，自吸入口被取入風路內的空氣(2-1)係被送入第1熱交換器11a。 In the second operation mode, the air (2-1) taken into the air passage from the suction port is sent to the first heat exchanger 11a.
在此，被取入風路內的空氣係藉作用為凝結器之第1熱交換器11a所加熱，而通過空氣的溫度上升(2-2)後，被送入水分吸附手段16。 Here, the air taken into the air passage is heated by the first heat exchanger 11a serving as a condenser, and the temperature of the passing air rises (2-2), and then sent to the moisture adsorbing means 16.
因為加熱後之空氣的相對濕度係比流入空氣更低，所以水分吸附手段16的吸附劑易脫附水分。加熱後的空氣被水分吸附手段16之吸附劑脫附水分而加濕後，變成低溫高濕，並流入第2熱交換器11b(2-3)。 Since the relative humidity of the heated air is lower than that of the inflowing air, the adsorbent of the moisture adsorbing means 16 tends to desorb moisture. The heated air is desorbed by the adsorbent of the moisture adsorbing means 16 and humidified, and then becomes low temperature and high humidity, and flows into the second heat exchanger 11b (2-3).
因為第2熱交換器11b係作為蒸發器發揮功能，所以冷卻通過空氣，而在冷卻後之通過空氣的溫度被冷卻至露點溫度以下的情況，成為水分被除濕的除濕空氣(2-4)。 Since the second heat exchanger 11b functions as an evaporator, the air is cooled and passed through the air, and the temperature of the passing air after cooling is cooled to a temperature equal to or lower than the dew point temperature, thereby dehumidifying the air (2-4).
通過第2熱交換器11b後的空氣係流入第3熱交換器11c。因為第3熱交換器11c係作為凝結器發揮功能，所以使通過空氣的溫度上升(2-5)，並自排出口被排出至除濕對象空間。 The air that has passed through the second heat exchanger 11b flows into the third heat exchanger 11c. Since the third heat exchanger 11c functions as a condenser, the temperature of the passing air is raised (2-5), and is discharged from the discharge port to the dehumidification target space.
此外，如以下之說明所示，第1熱交換器11a及第3熱交換器11c係藉由調整導熱面積之比，可抑制除濕效率降低。 Further, as described below, the first heat exchanger 11a and the third heat exchanger 11c can suppress the decrease in the dehumidification efficiency by adjusting the ratio of the heat transfer area.
例如，在設想除濕對象空間是夏季之室內的情況(溫度27℃、濕度約60%)。在執行第2運轉模式時，若第1熱交換器11a的加熱量大，則水分吸附手段16之放濕量成為第2熱交換器11b之除濕容量以上，而除濕效率降低。 For example, it is assumed that the dehumidification target space is in the summer room (temperature: 27 ° C, humidity: about 60%). When the heating amount of the first heat exchanger 11a is large, the amount of moisture released by the moisture adsorbing means 16 becomes equal to or higher than the dehumidifying capacity of the second heat exchanger 11b, and the dehumidifying efficiency is lowered.
因此，藉由使第3熱交換器11c之導熱面積比第1熱交換器11a的大，抑制第1熱交換器11a的凝結熱量，而抑制流入空氣的過加熱，可抑制除濕效率降低。 Therefore, by making the heat transfer area of the third heat exchanger 11c larger than that of the first heat exchanger 11a, the heat of condensation of the first heat exchanger 11a is suppressed, and overheating of the inflowing air is suppressed, and the deterioration of the dehumidification efficiency can be suppressed.
又，在除濕對象空間之空氣的相對濕度比上述之說明更高的情況(溫度27℃、濕度約80%)，可如以下所示調整導熱面積之比。 Further, in the case where the relative humidity of the air in the dehumidification target space is higher than the above description (temperature: 27 ° C, humidity: about 80%), the ratio of the heat transfer area can be adjusted as shown below.
在執行第2運轉模式時，若未使流入水分吸附手段16之空氣的相對濕度降低，則脫附反應所造成之放濕量變少。依此方式，在水分吸附手段16放濕量變少，意指無法使流入下游側的第2熱交換器11b之空氣的濕度提高對應的量。即，在第2熱交換器11b之除濕量減少了無法使流入第2熱交換器11b之空氣的濕度提高的量，而除濕效率降低。 When the second operation mode is executed, if the relative humidity of the air flowing into the moisture adsorption means 16 is not lowered, the amount of moisture released by the desorption reaction is reduced. In this way, the amount of moisture released by the moisture adsorbing means 16 is small, which means that the humidity of the air flowing into the second heat exchanger 11b on the downstream side cannot be increased by a corresponding amount. In other words, the amount of dehumidification in the second heat exchanger 11b is reduced by an amount that prevents the humidity of the air flowing into the second heat exchanger 11b from increasing, and the dehumidification efficiency is lowered.
因此，藉由使第1熱交換器11a之導熱面積比第3熱交換器11c的大，可使流入第1熱交換器11a之空氣的加熱量增加。藉此，因為相對濕度降低後之乾燥空氣流入水分吸附手段16，所以脫附量增加，而相對濕度變高、焓亦高的空氣流入第2熱交換器11b，而可抑制除濕效率降低。 Therefore, by making the heat transfer area of the first heat exchanger 11a larger than that of the third heat exchanger 11c, the amount of heating of the air flowing into the first heat exchanger 11a can be increased. By this means, since the dry air having a reduced relative humidity flows into the moisture adsorbing means 16, the amount of desorption increases, and the air having a high relative humidity and high helium flows into the second heat exchanger 11b, thereby suppressing a decrease in the dehumidifying efficiency.
因為本第1實施形態之除濕裝置300係在水分吸附手段16未設置如乾燥劑轉子等之馬達者，所以製造費用增加、或耗電力增加、或機器構成變得複雜等不存在。 The dehumidifier 300 of the first embodiment is not provided with a motor such as a desiccant rotor in the moisture adsorbing means 16, so that the manufacturing cost is increased, the power consumption is increased, or the machine configuration is complicated.
因為本第1實施形態之除濕裝置300係不是配置成乾燥劑轉子跨在所劃分之2條風路者，所以不會阻礙風路間之空氣的洩漏所造成之吸附反應或脫附反應。又，可防止劃分風路之部分與乾燥劑轉子之滑動所造成的耗電力增大及因滑動而受損之構件的維修所造成的耗費增大。 Since the dehumidifying apparatus 300 according to the first embodiment is not disposed so that the desiccant rotor straddles the two divided air passages, the adsorption reaction or the desorption reaction caused by the leakage of air between the air passages is not hindered. Further, it is possible to prevent an increase in power consumption caused by the sliding of the portion of the air passage and the drying of the desiccant rotor, and an increase in the cost of maintenance of the member damaged by the sliding.
因為本第1實施形態之除濕裝置300係將凝結熱的一部分用作乾燥劑之脫附反應的熱源，所以在不需要劃分之2條風路上，機器構成變得比較簡單。又，可防止因2條風路而壓力損失增大而提高送風手段12之轉速所伴隨之耗電力的增大。 Since the dehumidifier 300 of the first embodiment uses a part of the heat of condensation as a heat source for the desorption reaction of the desiccant, the machine configuration is relatively simple on the two air passages that do not need to be divided. Further, it is possible to prevent an increase in power consumption accompanying an increase in the pressure loss of the air blowing means 12 due to an increase in pressure loss due to the two air passages.
本第1實施形態之除濕裝置300係在熱交換器11發生著霜的情況，可切換四通閥15而實施除霜運轉，但是在該除霜運轉時亦可對除濕對象空間提供除濕空氣，而可抑制每小時之除濕量降低。 In the dehumidifier 300 of the first embodiment, when the heat exchanger 11 is frosted, the four-way valve 15 can be switched to perform the defrosting operation. However, during the defrosting operation, dehumidified air can be supplied to the dehumidification target space. It can suppress the decrease in the amount of dehumidification per hour.
在以往之使水分吸附手段轉動的方式，在低溫(例如溫度10℃、濕度60%)下運轉時，以加熱器等對水分吸附手段之脫附前的空氣加熱，使溫度高的空氣流入蒸發器，藉此，使蒸發溫度上升，抑制著霜，但是在更低溫(例如溫度5℃、濕度60%)等，加熱器等之加熱手段的輸入變成過大或發生著霜。在發生著霜的情況，需要每隔固定時間使冷凍循環停止，或藉 加熱器輸入進行除霜運轉，而除濕量降低。 In the conventional method of rotating the moisture adsorbing means, when operating at a low temperature (for example, a temperature of 10 ° C and a humidity of 60%), the air before the desorption of the moisture adsorbing means by a heater or the like is heated to cause the air having a high temperature to flow into the evaporation. In this way, the evaporating temperature is raised to suppress the frost, but at a lower temperature (for example, a temperature of 5 ° C and a humidity of 60%), the input of the heating means such as a heater becomes excessive or frosting occurs. In the case of frost, it is necessary to stop the freezing cycle at regular intervals, or to borrow The heater input performs a defrosting operation, and the amount of dehumidification is lowered.
可是，本第1實施形態之除濕裝置300係使第1熱交換器11a作為蒸發器發揮功能，即使發生著霜，亦藉由切換四通閥15，可一面使第1熱交換器11a作為凝結器發揮功能，進行除霜，一面使第2熱交換器11b作為蒸發器發揮功能，進行除濕。又，使第2熱交換器11b作為蒸發器發揮功能，即使發生著霜，亦藉由切換四通閥15，可一面使第2熱交換器11b作為凝結器發揮功能，進行除霜，一面使第1熱交換器11a作為蒸發器發揮功能，並以水分吸附手段16進行除濕。 In the dehumidifier 300 of the first embodiment, the first heat exchanger 11a functions as an evaporator, and even if frost occurs, the first heat exchanger 11a can be condensed by switching the four-way valve 15. When the defrosting function is performed, the second heat exchanger 11b functions as an evaporator to perform dehumidification. In addition, the second heat exchanger 11b functions as an evaporator, and even if frost is generated, the second heat exchanger 11b can be operated as a condenser and the defrosting can be performed while switching the four-way valve 15. The first heat exchanger 11a functions as an evaporator and is dehumidified by the moisture adsorbing means 16.
依此方式，本第1實施形態之除濕裝置300係在露點溫度為冰點以下的情況，亦藉由切換四通閥15，實施除霜運轉，可一面對除濕對象空間提供除濕空氣一面進行除霜，而可抑制每小時之除濕量降低。 In this way, the dehumidifying apparatus 300 of the first embodiment is configured such that when the dew point temperature is equal to or lower than the freezing point, the defrosting operation is performed by switching the four-way valve 15, and the dehumidifying air can be supplied to the dehumidifying object space. Cream, which can reduce the amount of dehumidification per hour.
因為本第1實施形態之除濕裝置300係在第1運轉模式時可將水分吸附手段16之全部的面用於吸附，所以可使除濕量比使用乾燥劑轉子等之以往的除濕裝置大。即，在使用與乾燥劑轉子同體積之水分吸附手段16的情況，可產生比以往之方式更低濕的空氣，而可使衣服乾燥速度變快。 Since the dehumidifying apparatus 300 according to the first embodiment can use the entire surface of the moisture adsorbing means 16 for adsorption in the first operational mode, the dehumidification amount can be made larger than that of the conventional dehumidifying apparatus using a desiccant rotor or the like. That is, in the case where the moisture adsorbing means 16 having the same volume as the desiccant rotor is used, it is possible to generate air which is lower in humidity than in the conventional method, and the drying speed of the clothes can be made faster.
本第1實施形態之除濕裝置300係可執行第1運轉模式及第2運轉模式。 The dehumidification apparatus 300 according to the first embodiment can execute the first operation mode and the second operation mode.
因此，在執行第2運轉模式時，因水分吸附手段16之脫附反應而空氣溫度降低，進而，通過作為蒸發器發揮功能之第2熱交換器11b而被冷卻的空氣流入配置於第2熱交換器11b之下游側並作為凝結器發揮功能的第3熱交換器11c。 Therefore, when the second operation mode is executed, the air temperature is lowered by the desorption reaction of the moisture adsorption means 16, and the air cooled by the second heat exchanger 11b functioning as an evaporator flows into the second heat. The third heat exchanger 11c functions as a condenser on the downstream side of the exchanger 11b.
藉此，第3熱交換器11c之凝結溫度降低，而冷凍循環變成高效率，可使除濕裝置300之除濕容量增加。 Thereby, the condensation temperature of the third heat exchanger 11c is lowered, and the refrigeration cycle becomes high efficiency, and the dehumidification capacity of the dehumidification apparatus 300 can be increased.
又，在執行第2運轉模式時，第1熱交換器11a作為凝結器發揮功能，將流入水分吸附手段16之空氣加熱，而使相對濕度降低。藉此，可使藉水分吸附手段16之脫附反應的放濕量增加，並對作為蒸發器發揮功能的第2熱交換器11b，供給相對濕度高且焓比吸入空氣更高之狀態的空氣，可使除濕量增加。 Further, when the second operation mode is executed, the first heat exchanger 11a functions as a condenser, and heats the air flowing into the moisture adsorption means 16 to lower the relative humidity. In this way, the amount of moisture released by the desorption reaction of the moisture adsorption means 16 can be increased, and the second heat exchanger 11b functioning as an evaporator can supply air having a relatively high relative humidity and a state in which helium is higher than the intake air. Can increase the amount of dehumidification.
第5圖係本第2實施形態之除濕裝置300的示意構成圖。本第2實施形態係具有：除濕單元100，係具有設置第1熱交換器11a、第2熱交換器11b及水分吸附手段16等的風路；及散熱單元200，係具有設置第3熱交換器11c等的風路；並採用將在第3熱交換器11c所產生之凝結熱排出至除濕對象外的構成。在本第2實施形態，主要說明與第1實施形態的相異點，對共同部分省略說明。 Fig. 5 is a schematic configuration diagram of a dehumidifying apparatus 300 according to the second embodiment. In the second embodiment, the dehumidifying unit 100 includes an air path in which the first heat exchanger 11a, the second heat exchanger 11b, the moisture adsorbing means 16 and the like are provided, and the heat radiating unit 200 has a third heat exchange. The air passage of the device 11c or the like is configured to discharge the heat of condensation generated in the third heat exchanger 11c to the outside of the dehumidification target. In the second embodiment, differences from the first embodiment will be mainly described, and the description of the common portions will be omitted.
在除濕單元100，搭載第1熱交換器11a、第2熱交換器11b、水分吸附手段16、節流手段14及第1送風手段12a。又，在除濕單元100，設置溫濕度感測器1a~1d、風速感測器2及溫度感測器3e、3f、3g、3h。 In the dehumidifying unit 100, the first heat exchanger 11a, the second heat exchanger 11b, the moisture adsorbing means 16, the throttle means 14, and the first air blowing means 12a are mounted. Further, in the dehumidifying unit 100, temperature and humidity sensors 1a to 1d, an air speed sensor 2, and temperature sensors 3e, 3f, 3g, and 3h are provided.
在除濕單元100，具有設置第1熱交換器11a、第2熱交換器11b、水分吸附手段16及第1送風手段12a的第1風路50。 The dehumidifying unit 100 includes a first air passage 50 in which the first heat exchanger 11a, the second heat exchanger 11b, the moisture adsorbing means 16, and the first air blowing means 12a are provided.
而且，在除濕單元100，從除濕對象空間被取入第1風路 50的空氣係按照第1熱交換器11a、水分吸附手段16、第2熱交換器11b的順序通過後，再被供給至除濕對象空間。 Further, in the dehumidifying unit 100, the first air path is taken from the dehumidification object space. The air of 50 is passed through the first heat exchanger 11a, the moisture adsorbing means 16, and the second heat exchanger 11b, and is then supplied to the dehumidification target space.
此外，除濕單元100之空氣的流動係對應於第5圖中的箭號X。 Further, the flow of the air of the dehumidifying unit 100 corresponds to the arrow X in FIG.
在散熱單元200，搭載第3熱交換器11c、及將散熱單元200內之空氣排出至除濕對象空間外的第2送風手段12b。又，在散熱單元200，設置溫濕度感測器1e、與除濕單元100之風速感測器2另外地設置的風速感測器2及檢測出第3熱交換器11c之空氣流動方向上游側之溫度及濕度的溫濕度感測器1f。 In the heat radiating unit 200, the third heat exchanger 11c and the second air blowing means 12b that discharges the air in the heat radiating unit 200 to the outside of the dehumidifying target space are mounted. Further, in the heat radiating unit 200, the temperature and humidity sensor 1e, the wind speed sensor 2 separately provided to the wind speed sensor 2 of the dehumidifying unit 100, and the upstream side of the air flow direction in which the third heat exchanger 11c is detected are provided. Temperature and humidity temperature and humidity sensor 1f.
在散熱單元200，具有設置第3熱交換器11c及第2送風手段12b的第2風路51。 The heat radiating unit 200 has a second air passage 51 in which the third heat exchanger 11c and the second air blowing means 12b are provided.
而且，在散熱單元200，從除濕對象空間或除濕對象空間以外之空間被取入第2風路51的空氣係通過第3熱交換器11c後，再排出至除濕對象空間外。 In the heat dissipation unit 200, the air taken into the second air passage 51 from the space other than the dehumidification target space or the dehumidification target space passes through the third heat exchanger 11c, and is then discharged to the outside of the dehumidification target space.
此外，散熱單元200之空氣的流動係對應於第5圖中的箭號Y。 Further, the flow of the air of the heat radiating unit 200 corresponds to the arrow Y in FIG.
在此，在第5圖，關於四通閥15、壓縮機13及溫度感測器3a、3b、3c、3d，當作設置於除濕單元100之外側及散熱單元200之外側者來說明，但是未限定如此。亦可壓縮機13、節流手段14及四通閥15係配置於除濕單元100及散熱單元200之任一個。又，關於溫度感測器3c、3d，例如亦可設置於散熱單元200內。 Here, in the fifth diagram, the four-way valve 15, the compressor 13, and the temperature sensors 3a, 3b, 3c, and 3d are described as being disposed outside the dehumidifying unit 100 and outside the heat radiating unit 200, but Not limited to this. The compressor 13, the throttle means 14, and the four-way valve 15 may be disposed in any one of the dehumidifying unit 100 and the heat radiating unit 200. Further, the temperature sensors 3c and 3d may be provided, for example, in the heat dissipation unit 200.
第6圖係表示第2實施形態的除濕裝置300之在各模式之溫濕度轉移的濕空氣線圖。此外，第6圖(a)係在第1運轉模式的濕空氣線圖，第6圖(b)係在第2運轉模式的濕空氣線圖。 Fig. 6 is a wet air diagram showing the temperature and humidity shift of each mode of the dehumidifying apparatus 300 of the second embodiment. In addition, Fig. 6(a) is a wet air diagram in the first operation mode, and Fig. 6(b) is a wet air diagram in the second operation mode.
又，第6圖(a)中之(1-1a)~(1-4a)、(1-1b)及(1-2b)係表示在第1運轉模式之通過第1熱交換器11a之前的空氣(1-1a)、通過第1熱交換器11a後的空氣(1-2a)、通過水分吸附手段16後的空氣(1-3a)、通過第2熱交換器11b後的空氣(1-4a)、通過第3熱交換器11c之前的空氣(1-1b)及通過第3熱交換器11c後的空氣(1-2b)。 Further, (1-1a) to (1-4a), (1-1b), and (1-2b) in Fig. 6(a) indicate before the first heat exchanger 11a passes through the first operation mode. Air (1-1a), air (1-2a) passing through the first heat exchanger 11a, air (1-3a) passing through the moisture adsorbing means 16, and air passing through the second heat exchanger 11b (1- 4a), the air (1-1b) before passing through the third heat exchanger 11c and the air (1-2b) passing through the third heat exchanger 11c.
又，第6圖(b)中之(2-1a)~(2-4a)、(2-1b)及(2-2b)係表示在第2運轉模式之通過第1熱交換器11a之前的空氣(2-1a)、通過第1熱交換器11a後的空氣(2-2a)、通過水分吸附手段16後的空氣(2-3a)、通過第2熱交換器11b後的空氣(2-4a)、通過第3熱交換器11c之前的空氣(2-1b)及通過第3熱交換器11c後的空氣(2-2b)。 Further, (2-1a) to (2-4a), (2-1b), and (2-2b) in Fig. 6(b) show before the first heat exchanger 11a passes through the second operation mode. Air (2-1a), air (2-2a) passing through the first heat exchanger 11a, air (2-3a) after passing through the moisture adsorbing means 16, and air passing through the second heat exchanger 11b (2- 4a), the air (2-1b) before passing through the third heat exchanger 11c and the air (2-2b) passing through the third heat exchanger 11c.
此外，在第6圖(a)，表示水分吸附手段16之水分保持量變少，而對高濕之空氣(例如相對濕度70%以上)進行吸附反應之情況的例子。又，在第6圖(b)，表示水分吸附手段16之水分保持量變多，而對低濕之空氣(例如相對濕度60%以下)進行脫附反應之情況的例子。 In addition, (a) of FIG. 6 shows an example in which the amount of moisture retained by the moisture adsorbing means 16 is small, and the high-humidity air (for example, a relative humidity of 70% or more) is subjected to an adsorption reaction. In addition, FIG. 6(b) shows an example in which the moisture retention amount of the moisture adsorbing means 16 is increased, and the dehumidifying reaction is performed on low-humidity air (for example, a relative humidity of 60% or less).
在第1運轉模式時的除濕單元100，自吸入口被取入第1風路50的空氣(1-1a)係被送入第1熱交換器11a。 In the dehumidifying unit 100 in the first operation mode, the air (1-1a) taken into the first air passage 50 from the suction port is sent to the first heat exchanger 11a.
在此，被取入第1風路50的空氣係藉作用為蒸發器之第1熱交換器11a所冷卻。在通過空氣被冷卻至露點溫度以下的情況，成為水分被除濕的除濕空氣(1-2a)後，被送入水分吸附手段16。 Here, the air taken into the first air passage 50 is cooled by the first heat exchanger 11a functioning as an evaporator. When the air is cooled to a temperature equal to or lower than the dew point temperature, the dehumidified air (1-2a) in which the moisture is dehumidified is sent to the moisture adsorbing means 16.
因為冷卻除濕後之空氣的相對濕度係高達約70~90%RH，所以水分吸附手段16的吸附劑易吸附水分。冷卻後的空氣被水分吸附手段16之吸附劑吸附水分而除濕後，變成高溫低濕，並流入第2熱交換器11b(1-3a)。 Since the relative humidity of the air after cooling and dehumidification is as high as about 70 to 90% RH, the adsorbent of the moisture adsorbing means 16 easily adsorbs moisture. The air after cooling is dehumidified by the adsorbent of the moisture adsorbing means 16 and dehumidified, and then becomes high temperature and low humidity, and flows into the second heat exchanger 11b (1-3a).
因為第2熱交換器11b係作為凝結器發揮功能，所以通過第2熱交換器11b之空氣被加熱，而溫度上升(1-4a)。 Since the second heat exchanger 11b functions as a condenser, the air passing through the second heat exchanger 11b is heated, and the temperature rises (1-4a).
通過第2熱交換器11b後的空氣係自空氣排出口被排出至空調對象空間。 The air that has passed through the second heat exchanger 11b is discharged from the air discharge port to the air-conditioned space.
在第1運轉模式時的散熱單元200，自吸入口被取入第2風路51的空氣(1-1b)係被送入第3熱交換器11c。 In the heat dissipation unit 200 in the first operation mode, the air (1-1b) taken into the second air passage 51 from the suction port is sent to the third heat exchanger 11c.
在此，因為第3熱交換器11c係作為凝結器發揮功能，所以通過第3熱交換器11c後之空氣的溫度上升(1-2b)。 Here, since the third heat exchanger 11c functions as a condenser, the temperature of the air passing through the third heat exchanger 11c rises (1-2b).
通過第3熱交換器11c後的空氣係自散熱單元200的空氣排出口被排出。 The air that has passed through the third heat exchanger 11c is discharged from the air discharge port of the heat radiating unit 200.
在第2運轉模式時的除濕單元100，自吸入口被取入第2風路51的空氣(2-1a)係被送入第1熱交換器11a。 In the dehumidifying unit 100 in the second operation mode, the air (2-1a) taken into the second air passage 51 from the suction port is sent to the first heat exchanger 11a.
在此，被取入第2風路51的空氣係藉作用為凝結器之第1熱交換器11a所加熱，而通過之空氣的溫度上升(2-2a)後，被 送入水分吸附手段16。 Here, the air taken in the second air passage 51 is heated by the first heat exchanger 11a serving as a condenser, and the temperature of the air passing therethrough is increased (2-2a). The moisture adsorption means 16 is sent.
因為加熱後之空氣的相對濕度係變成比流入空氣低，所以藉水分吸附手段16的吸附劑易脫附水分。加熱後之空氣被水分吸附手段16的吸附劑脫附水分並加濕，變成低溫高濕，並流入第2熱交換器11b(2-3a)。 Since the relative humidity of the heated air becomes lower than that of the inflowing air, the adsorbent by the moisture adsorbing means 16 tends to desorb moisture. The heated air is desorbed by the adsorbent of the moisture adsorbing means 16 and humidified to become low temperature and high humidity, and flows into the second heat exchanger 11b (2-3a).
因為第2熱交換器11b係作為蒸發器發揮功能冷卻通過空氣，所以通過第2熱交換器11b之冷卻後的空氣係被冷卻至露點溫度以下，而成為除濕空氣(2-4a)。 Since the second heat exchanger 11b functions as an evaporator to cool the passing air, the air cooled by the second heat exchanger 11b is cooled to a temperature equal to or lower than the dew point temperature to become dehumidified air (2-4a).
通過第2熱交換器11b後的空氣係自空氣排出口被排出至空調對象空間。 The air that has passed through the second heat exchanger 11b is discharged from the air discharge port to the air-conditioned space.
在第2運轉模式時的散熱單元200，自吸入口被取入第2風路51的空氣(2-1b)係被送入第3熱交換器11c。 In the heat dissipation unit 200 in the second operation mode, the air (2-1b) taken into the second air passage 51 from the suction port is sent to the third heat exchanger 11c.
因為第3熱交換器11c係作為凝結器發揮功能，所以通過第3熱交換器11c後之空氣的溫度上升(2-2b)。 Since the third heat exchanger 11c functions as a condenser, the temperature of the air passing through the third heat exchanger 11c rises (2-2b).
通過第3熱交換器11c後的空氣係自散熱單元200的空氣排出口被排出。 The air that has passed through the third heat exchanger 11c is discharged from the air discharge port of the heat radiating unit 200.
本第2實施形態之除濕裝置300係除了第1實施形態之除濕裝置300所具有的效果以外，還具有如下之效果。 In addition to the effects of the dehumidifying apparatus 300 of the first embodiment, the dehumidifying apparatus 300 of the second embodiment has the following effects.
在以往之需要冷卻與除濕的空間(例如穀倉等)，設置再熱除濕機及冷氣裝置，一面抑制除濕對象空間之溫升一面除濕，但是節能性減少了設置再熱除濕機及冷氣裝置之2台裝置的量。 In the space where cooling and dehumidification are required in the past (for example, a barn, etc.), a reheat dehumidifier and a cooling device are provided, and the dehumidification of the dehumidification space is suppressed while the dehumidification is performed, but the energy saving property is reduced by the reheat dehumidifier and the air conditioner. The amount of the device.
可是，因為本第2實施形態之除濕裝置300係將凝結熱排出至除濕對象外，所以可抑制除濕對象空間之溫升，或可冷卻，而可抑制節能性降低。 However, since the dehumidifying apparatus 300 of the second embodiment discharges the heat of condensation to the object to be dehumidified, it is possible to suppress the temperature rise of the space to be dehumidified or to cool, and it is possible to suppress a decrease in energy saving performance.
本第2實施形態之除濕裝置300係藉由控制第2送風手段12b的轉速，來調整在散熱單元200流動的風速，因為可控制除濕單元100的除濕量，所以可易於達成因應於目的的除濕量。 The dehumidifier 300 of the second embodiment adjusts the wind speed flowing through the heat radiating unit 200 by controlling the number of revolutions of the second air blowing means 12b. Since the dehumidifying amount of the dehumidifying unit 100 can be controlled, it is easy to achieve dehumidification according to the purpose. the amount.
此外，本第2實施形態之除濕裝置300亦可應用在第1實施形態所說明的變形例。 Further, the dehumidifying apparatus 300 according to the second embodiment can be applied to the modification described in the first embodiment.
第7圖係第3實施形態之除濕裝置300的示意構成例圖。第8圖係表示第3實施形態的除濕裝置300之冷媒壓力與焓之變動的莫理爾線圖。 Fig. 7 is a view showing an exemplary configuration of a dehumidifying apparatus 300 according to a third embodiment. Fig. 8 is a Mollier diagram showing changes in the refrigerant pressure and enthalpy of the dehumidifying apparatus 300 of the third embodiment.
在本第3實施形態，主要說明與第1、第2實施形態的相異點，關於共同部分省略說明。 In the third embodiment, differences from the first and second embodiments will be mainly described, and the description of the common portions will be omitted.
第3實施形態之除濕裝置300係在第1、第2實施形態的第3熱交換器11c與四通閥15之間新設置第2節流手段14a。 In the dehumidifier 300 of the third embodiment, the second throttle means 14a is newly provided between the third heat exchanger 11c and the four-way valve 15 of the first and second embodiments.
此外，在本第3實施形態，將在第1、第2實施形態的第2熱交換器11b與第1熱交換器11a之間的節流手段14稱為第1節流手段14b。 In the third embodiment, the throttle means 14 between the second heat exchanger 11b and the first heat exchanger 11a of the first and second embodiments is referred to as a first throttle means 14b.
參照第7圖及第8圖，說明在第1運轉模式之冷媒的流動。 The flow of the refrigerant in the first operation mode will be described with reference to Figs. 7 and 8.
從壓縮機13所排出的冷媒係向第3熱交換器11c流動。在此時，第3熱交換器11c係作用為凝結器，冷媒係在與空氣進行熱交換時一部分凝結成液體。在通過第3熱交換器11c後，冷媒係在第2節流手段14a降壓後，通過四通閥15，向第2熱交換器11b流動。第2熱交換器11b係作用為凝結器，冷媒係在與空氣進行熱交換時凝結成液體後，向第1節流手段14b流動。冷媒係在第1節流手段14b被降壓後，流至第1熱交換器11a。第1熱交換器11a係作為蒸發器發揮功能，冷媒係在與空氣進行熱交換而蒸發後，通過四通閥15，再被壓縮機13吸入。 The refrigerant discharged from the compressor 13 flows into the third heat exchanger 11c. At this time, the third heat exchanger 11c functions as a condenser, and the refrigerant partially condenses into a liquid when it exchanges heat with air. After passing through the third heat exchanger 11c, the refrigerant is depressurized by the second throttle means 14a, and then flows through the four-way valve 15 to the second heat exchanger 11b. The second heat exchanger 11b functions as a condenser, and the refrigerant condenses into a liquid when it exchanges heat with air, and then flows to the first throttle means 14b. The refrigerant is depressurized by the first throttle means 14b, and then flows to the first heat exchanger 11a. The first heat exchanger 11a functions as an evaporator, and the refrigerant evaporates by exchanging heat with air, passes through the four-way valve 15, and is sucked by the compressor 13.
參照第7圖及第8圖，說明在第2運轉模式之冷媒的流動。 The flow of the refrigerant in the second operation mode will be described with reference to Figs. 7 and 8.
從壓縮機13所排出的冷媒係向第3熱交換器11c流動。在此時，第3熱交換器11c係作用為凝結器，冷媒係在與空氣進行熱交換時一部分凝結成液體。在通過第3熱交換器11c後，冷媒係在第2節流手段14a被降壓後，通過四通閥15，向第1熱交換器11a流動。第1熱交換器11a係作用為凝結器，冷媒係在與空氣進行熱交換時凝結成液體後，向第1節流手段14b流動。冷媒係在第1節流手段14b被降壓後，流至第2熱交換器11b。第2熱交換器11b係作為蒸發器發揮功能，冷媒係在與空氣進行熱交換而蒸發後，通過四通閥15，再被壓縮機13吸入。 The refrigerant discharged from the compressor 13 flows into the third heat exchanger 11c. At this time, the third heat exchanger 11c functions as a condenser, and the refrigerant partially condenses into a liquid when it exchanges heat with air. After passing through the third heat exchanger 11c, the refrigerant is depressurized by the second throttle means 14a, and then flows through the four-way valve 15 to the first heat exchanger 11a. The first heat exchanger 11a functions as a condenser, and the refrigerant condenses into a liquid when it exchanges heat with air, and then flows to the first throttle means 14b. The refrigerant is depressurized by the first throttle means 14b, and then flows to the second heat exchanger 11b. The second heat exchanger 11b functions as an evaporator, and the refrigerant is evaporated by heat exchange with air, and then passed through the four-way valve 15 and sucked by the compressor 13.
本第3實施形態之除濕裝置300係除了第1實施形態之除濕裝置300所具有的效果以外，還具有如下之效果。 In addition to the effects of the dehumidifying apparatus 300 of the first embodiment, the dehumidifying apparatus 300 of the third embodiment has the following effects.
藉由調整第2節流手段14a的孔口，可控制第3熱交換器11c的凝結熱量，不必變更熱交換器11的導熱面積，就可實現配合流入空氣之溫度及濕度的運轉狀態。 By adjusting the orifice of the second throttle means 14a, the heat of condensation of the third heat exchanger 11c can be controlled, and the operating state of the temperature and humidity of the inflowing air can be realized without changing the heat transfer area of the heat exchanger 11.
例如，在濕度比第1值低的低濕空氣(例如溫度26℃、濕度40%)，藉由使第2節流手段14a的孔口變小，在第2運轉模式時使第3熱交換器11c的凝結壓力上升，而使凝結熱量增加，第1熱交換器11a之凝結熱量降低，藉此，可避免對流入水分吸附手段16之空氣過度加熱。 For example, in the low-humidity air (for example, the temperature of 26 ° C and the humidity of 40%) whose humidity is lower than the first value, the third heat exchange is performed in the second operation mode by reducing the orifice of the second throttle means 14a. The condensation pressure of the device 11c rises, and the heat of condensation increases, and the heat of condensation of the first heat exchanger 11a is lowered, whereby excessive heating of the air flowing into the moisture adsorbing means 16 can be avoided.
反之，在濕度比第2值高的高濕空氣(例如溫度26℃、濕度80%)，藉由使第2節流手段14a的孔口變大，在第2運轉模式時使第3熱交換器11c的凝結壓力降低，而使凝結熱量減少，第1熱交換器11a之凝結熱量增加，藉此，可使流入水分吸附手段16之空氣的相對濕度降低，使放濕量增加。 On the other hand, in the high-humidity air (for example, the temperature of 26 ° C and the humidity of 80%) whose humidity is higher than the second value, the third heat exchange is performed in the second operation mode by increasing the orifice of the second throttle means 14a. The condensation pressure of the device 11c is lowered, and the amount of heat of condensation is reduced, and the amount of heat of condensation in the first heat exchanger 11a is increased, whereby the relative humidity of the air flowing into the moisture adsorbing means 16 can be lowered to increase the amount of moisture released.
此外，在上述，說明是(1)第2值比第1值大、(2)第1值是比40大且比80小的值、(3)第2值是比80小且比40大的值之情況的例子，但是未限定如此，亦可因應於除濕對象空間之溫度等來變更。 In addition, in the above description, (1) the second value is larger than the first value, (2) the first value is larger than 40 and smaller than 80, and (3) the second value is smaller than 80 and larger than 40. An example of the case of the value is not limited thereto, and may be changed depending on the temperature of the dehumidification target space or the like.
第9圖係第4實施形態之除濕裝置300的示意構成例圖。在本第4實施形態，主要說明與第1~第3實施形態的相異點，關於共同部分省略說明。 Fig. 9 is a view showing a schematic configuration of a dehumidifying apparatus 300 according to a fourth embodiment. In the fourth embodiment, differences from the first to third embodiments will be mainly described, and the description of the common portions will be omitted.
在本第4實施形態，第1熱交換器11a與第2熱 交換器11b並聯。又，與第1~第3實施形態相異，拆下四通閥15。又，第3熱交換器11c的下游側係與第1熱交換器11a及第2熱交換器11b的上游側連接。進而，替代第1~第2實施形態的節流手段14及第3實施形態的第2節流手段14a與第1節流手段14b，設置第3節流手段14c與第4節流手段14d。 In the fourth embodiment, the first heat exchanger 11a and the second heat The exchangers 11b are connected in parallel. Further, unlike the first to third embodiments, the four-way valve 15 is removed. Further, the downstream side of the third heat exchanger 11c is connected to the upstream side of the first heat exchanger 11a and the second heat exchanger 11b. Further, the third throttle means 14c and the fourth throttle means 14d are provided instead of the throttle means 14 of the first to second embodiments and the second throttle means 14a and the first throttle means 14b of the third embodiment.
第4實施形態之除濕裝置300係在第1運轉模式時冷媒按照壓縮機13、第3熱交換器11c、第3節流手段14c及第1熱交換器11a的順序流動。此外，在第1運轉模式時，第4節流手段14d係全閉。 In the dehumidifier 300 of the fourth embodiment, the refrigerant flows in the order of the compressor 13, the third heat exchanger 11c, the third throttle means 14c, and the first heat exchanger 11a in the first operation mode. Further, in the first operation mode, the fourth throttle means 14d is fully closed.
又，在第2運轉模式時，冷媒按照壓縮機13、第3熱交換器11c、第4節流手段14d及第2熱交換器11b的順序流動。此外，在第2運轉模式時，第3節流手段14c係全閉。 Further, in the second operation mode, the refrigerant flows in the order of the compressor 13, the third heat exchanger 11c, the fourth throttle means 14d, and the second heat exchanger 11b. Further, in the second operation mode, the third throttle means 14c is fully closed.
第10圖係表示第4實施形態的除濕裝置300之在各模式之溫濕度轉移的濕空氣線圖。此外，第10圖(a)係在第1運轉模式的濕空氣線圖，第10圖(b)係在第2運轉模式的濕空氣線圖。 Fig. 10 is a wet air diagram showing the temperature and humidity shift of each mode of the dehumidifying apparatus 300 of the fourth embodiment. Further, Fig. 10(a) is a wet air diagram in the first operation mode, and Fig. 10(b) is a wet air diagram in the second operation mode.
又，第10圖(a)中之(1-1c)~(1-5c)係表示在第1運轉模式之通過第1熱交換器11a之前的空氣(1-1c)、通過第1熱交換器11a後的空氣(1-2c)、通過水分吸附手段16後的空氣(1-3c)、通過第2熱交換器11b後的空氣(1-4c)、通過第3熱交換器11c後的空氣(1-5c)。 Further, (1-1c) to (1-5c) in Fig. 10(a) show the air (1-1c) before passing through the first heat exchanger 11a in the first operation mode, and the first heat exchange is performed. Air (1-2c) after the device 11a, air (1-3c) after passing through the moisture adsorbing means 16, air (1-4c) after passing through the second heat exchanger 11b, and after passing through the third heat exchanger 11c Air (1-5c).
又，第10圖(b)中之(2-1c)~(2-5c)係表示在第2運轉模式之通過第1熱交換器11a之前的空氣(2-1c)、通過第1熱交 換器11a後的空氣(2-2c)、通過水分吸附手段16後的空氣(2-3c)、通過第2熱交換器11b後的空氣(2-4c)、通過第3熱交換器11c後之空氣(2-5c)的狀態。 Further, (2-1c) to (2-5c) in Fig. 10(b) show the air (2-1c) before passing through the first heat exchanger 11a in the second operation mode, and the first heat is passed. Air (2-2c) after the inverter 11a, air (2-3c) after passing through the moisture adsorbing means 16, air (2-4c) after passing through the second heat exchanger 11b, and after passing through the third heat exchanger 11c The state of the air (2-5c).
參照第10圖，說明在第1運轉模式及第2運轉模式之空氣的狀態。 The state of the air in the first operation mode and the second operation mode will be described with reference to Fig. 10 .
此外，在第10圖(a)，表示水分吸附手段16之水分保持量變少，而對高濕之空氣(例如相對濕度70%以上)進行吸附反應之情況的例子。又，在第10圖(b)，表示水分吸附手段16之水分保持量變多，而對低濕之空氣(例如相對濕度60%以下)進行脫附反應之情況的例子。 In addition, (a) of FIG. 10 shows an example in which the moisture retention amount of the moisture adsorbing means 16 is small, and the high-humidity air (for example, a relative humidity of 70% or more) is subjected to an adsorption reaction. In addition, in the figure (b) of FIG. 10, an example in which the moisture retention amount of the moisture adsorbing means 16 is increased and the dehumidification reaction is performed on low-humidity air (for example, a relative humidity of 60% or less) is shown.
在第1運轉模式，自吸入口被取入風路內的空氣(1-1c)係被送入第1熱交換器11a。 In the first operation mode, the air (1-1c) taken into the air passage from the suction port is sent to the first heat exchanger 11a.
在此，被取入風路內的空氣係藉作用為蒸發器之第1熱交換器11a所冷卻，在通過空氣被冷卻至露點溫度以下的情況，成為水分被除濕的除濕空氣(1-2c)後，被送入水分吸附手段16。 Here, the air taken into the air passage is cooled by the first heat exchanger 11a serving as the evaporator, and when it is cooled to a temperature equal to or lower than the dew point by the air, the dehumidified air is dehumidified (1-2c). After that, it is sent to the moisture adsorption means 16.
因為冷卻除濕後之空氣的相對濕度係高達約70~90%RH，所以水分吸附手段16的吸附劑易吸附水分。冷卻後的空氣被水分吸附手段16之吸附劑吸附水分而除濕後，變成高溫低濕，並流入第2熱交換器11b(1-3c)。 Since the relative humidity of the air after cooling and dehumidification is as high as about 70 to 90% RH, the adsorbent of the moisture adsorbing means 16 easily adsorbs moisture. The air after cooling is desorbed by the adsorbent of the moisture adsorbing means 16 and dehumidified, and then becomes high temperature and low humidity, and flows into the second heat exchanger 11b (1-3c).
第2熱交換器11b係因為第4節流手段14d全閉，所以不會作為熱交換器發揮功能，而不發生溫濕度變化(1-4c)。通過第2熱交換器11b後的空氣係流入第3熱交換器11c(1-4c)。 Since the fourth heat exchanger 11b is fully closed, the fourth throttle means 14b does not function as a heat exchanger, and does not cause temperature and humidity changes (1-4c). The air that has passed through the second heat exchanger 11b flows into the third heat exchanger 11c (1-4c).
因為第3熱交換器11c係作為凝結器發揮功能，所以使通過空氣的溫度上升，並自空氣的排出口被排出至除濕對象空間(1-5c)。 Since the third heat exchanger 11c functions as a condenser, the temperature of the passing air rises and is discharged from the air discharge port to the dehumidification target space (1-5c).
在第2運轉模式時，自吸入口被取入風路內的空氣(2-1c)係被送入第1熱交換器11a。 In the second operation mode, the air (2-1c) taken into the air passage from the suction port is sent to the first heat exchanger 11a.
在此，第1熱交換器11a係因為第3節流手段14c是全閉，所以不會作為熱交換器發揮功能，而不發生溫濕度變化(2-2c)，並被送入水分吸附手段16。 In the first heat exchanger 11a, since the third throttle means 14c is fully closed, it does not function as a heat exchanger, and does not change in temperature and humidity (2-2c), and is sent to the moisture adsorption means. 16.
因應於流入空氣的相對濕度，水分吸附手段16的吸附劑易脫附水分。流入空氣被水分吸附手段16的吸附劑脫附水分並加濕，變成低溫高濕，並流入第2熱交換器11b(2-3c)。 The adsorbent of the moisture adsorbing means 16 easily desorbs moisture in response to the relative humidity of the inflowing air. The inflowing air is desorbed by the adsorbent of the moisture adsorbing means 16 and humidified to become low temperature and high humidity, and flows into the second heat exchanger 11b (2-3c).
因為第2熱交換器11b係作為蒸發器發揮功能，所以冷卻通過空氣，而在冷卻後之通過空氣的溫度被冷卻至露點溫度以下的情況，成為水分被除濕的除濕空氣(2-4c)。 Since the second heat exchanger 11b functions as an evaporator, the air is cooled and passed through the air, and the temperature of the passing air after cooling is cooled to a temperature equal to or lower than the dew point temperature, and the dehumidified air (2-4c) is dehumidified.
因為第3熱交換器11c係作為凝結器發揮功能，所以使通過空氣的溫度上升，並自空氣的排出口被排出至除濕對象空間(2-5c)。 Since the third heat exchanger 11c functions as a condenser, the temperature of the passing air rises and is discharged from the air discharge port to the dehumidification target space (2-5c).
本第4實施形態之除濕裝置300係除了第1實施形態之除濕裝置300所具有的效果以外，還具有如下之效果。 In addition to the effects of the dehumidifying apparatus 300 of the first embodiment, the dehumidifying apparatus 300 of the fourth embodiment has the following effects.
本第4實施形態之除濕裝置300係對低濕的空氣(例如溫度26℃、濕度30%)，可抑制在第2運轉模式時流入水分吸附手段16之空氣的過加熱。 The dehumidifying apparatus 300 according to the fourth embodiment is capable of suppressing overheating of the air flowing into the moisture adsorbing means 16 in the second operational mode in the case of low-humidity air (for example, a temperature of 26 ° C and a humidity of 30%).
又，可減少在第1運轉模式與第2運轉模式之間之模式切換時的切換損失(從凝結器切換成蒸發器時之熱交換器的熱容量等)，使除濕量增加。 Further, it is possible to reduce the switching loss (the heat capacity of the heat exchanger when switching from the condenser to the evaporator) between the first operation mode and the second operation mode, and to increase the amount of dehumidification.
此外，本第4實施形態之除濕裝置300亦可應用在第1實施形態所說明之變形例。 Further, the dehumidifying apparatus 300 of the fourth embodiment can be applied to the modification described in the first embodiment.
14‧‧‧節流手段 14‧‧‧Throttle means
300‧‧‧除濕裝置 300‧‧‧Dehumidification device
A‧‧‧冷媒迴路 A‧‧‧ refrigerant circuit
1a~1e‧‧‧溫濕度感測器 1a~1e‧‧‧temperature and humidity sensor
3a~3h‧‧‧溫度感測器 3a~3h‧‧‧temperature sensor
2‧‧‧風速感測器 2‧‧‧Wind speed sensor
11a‧‧‧第1熱交換器 11a‧‧‧1st heat exchanger
11b‧‧‧第2熱交換器 11b‧‧‧2nd heat exchanger
11c‧‧‧第3熱交換器 11c‧‧‧3rd heat exchanger
12‧‧‧送風手段 12‧‧‧Air supply means
13‧‧‧壓縮機 13‧‧‧Compressor
15‧‧‧四通閥 15‧‧‧ four-way valve
16‧‧‧水分吸附手段 16‧‧‧Water adsorption means
50‧‧‧第1風路 50‧‧‧1st wind road
4‧‧‧控制電路 4‧‧‧Control circuit
Claims (12)
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| PCT/JP2013/051821 WO2014118871A1 (en) | 2013-01-29 | 2013-01-29 | Dehumidifier |
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| TW201430294A TW201430294A (en) | 2014-08-01 |
| TWI528001B true TWI528001B (en) | 2016-04-01 |
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| CN (2) | CN106799117B (en) |
| DE (1) | DE112013006529B4 (en) |
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- 2013-01-29 WO PCT/JP2013/051821 patent/WO2014118871A1/en active Application Filing
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- 2013-01-29 CN CN201380071680.XA patent/CN104955548B/en active Active
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| TWI671494B (en) * | 2017-01-12 | 2019-09-11 | 日商三菱電機股份有限公司 | Dehumidifier |
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| JP6021953B2 (en) | 2016-11-09 |
| CN104955548B (en) | 2017-07-18 |
| GB2525112B (en) | 2021-02-24 |
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| CN106799117A (en) | 2017-06-06 |
| DE112013006529B4 (en) | 2017-12-14 |
| GB2525112A (en) | 2015-10-14 |
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