WO2014208083A1 - Dispositif de déshumidification et système de déshumidification - Google Patents

Dispositif de déshumidification et système de déshumidification Download PDF

Info

Publication number
WO2014208083A1
WO2014208083A1 PCT/JP2014/003387 JP2014003387W WO2014208083A1 WO 2014208083 A1 WO2014208083 A1 WO 2014208083A1 JP 2014003387 W JP2014003387 W JP 2014003387W WO 2014208083 A1 WO2014208083 A1 WO 2014208083A1
Authority
WO
WIPO (PCT)
Prior art keywords
air
adsorption
heat exchanger
heat exchange
adsorption heat
Prior art date
Application number
PCT/JP2014/003387
Other languages
English (en)
Japanese (ja)
Inventor
尚利 藤田
敏幸 夏目
中山 浩
松井 伸樹
Original Assignee
ダイキン工業株式会社
株式会社ダイキンアプライドシステムズ
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 ダイキン工業株式会社, 株式会社ダイキンアプライドシステムズ filed Critical ダイキン工業株式会社
Priority to BR112015032117A priority Critical patent/BR112015032117A2/pt
Priority to CN201480036707.6A priority patent/CN105358915B/zh
Priority to KR1020167002316A priority patent/KR101630143B1/ko
Priority to US14/897,098 priority patent/US20160146479A1/en
Priority to EP14818067.2A priority patent/EP3015778A4/fr
Publication of WO2014208083A1 publication Critical patent/WO2014208083A1/fr

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F3/1405Air-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 in which the humidity of the air is exclusively affected by contact with the evaporator of a closed-circuit cooling system or heat pump circuit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F3/1411Air-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F3/1411Air-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
    • F24F3/1423Air-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F3/1411Air-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
    • F24F3/1429Air-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 alternatively operating a heat exchanger in an absorbing/adsorbing mode and a heat exchanger in a regeneration mode
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F2003/144Air-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-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
    • F24F3/12Air-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
    • F24F3/14Air-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
    • F24F2003/1458Air-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 using regenerators

Definitions

  • the present invention relates to a dehumidifying apparatus and a dehumidifying system for dehumidifying air and supplying it to a humidity control space, and more particularly to a dehumidifying apparatus having an adsorption heat exchanger carrying an adsorbent.
  • Patent Document 1 describes a humidity control device that includes a refrigerant circuit having two adsorption heat exchangers and adjusts the humidity of air in the adsorption heat exchanger.
  • the first adsorption heat exchanger serves as a condenser and the second adsorption heat exchanger serves as an evaporator
  • the first adsorption heat exchanger serves as an evaporator and the second adsorption heat exchanger serves as a condenser. This operation is repeated alternately.
  • this humidity control apparatus supplies the air dehumidified in the adsorption heat exchanger functioning as an evaporator to the room and discharges the air humidified in the adsorption heat exchanger functioning as a condenser to the outside. Perform dehumidifying operation.
  • an object of the present invention is to provide a dehumidifying device capable of improving the dehumidifying capability while suppressing an increase in power consumption.
  • the first invention has first and second adsorption heat exchangers (101, 102) carrying an adsorbent, and the first adsorption heat exchanger (101) serves as an evaporator to dehumidify the air.
  • the first adsorption heat exchanger (102) serves as a condenser to regenerate the adsorbent
  • the first adsorption heat exchanger (101) serves as a condenser to regenerate the adsorbent and the second heat of adsorption.
  • a refrigerant circuit (100) that alternately performs a second operation of dehumidifying air by using the exchanger (102) as an evaporator, and a first and a second adsorption heat exchanger (101, 102) provided with the first and second adsorption heat exchangers (101, 102), respectively.
  • a heat exchange chamber provided with an adsorption heat exchanger (101, 102) serving as an evaporator (S11, S12)
  • the air that has passed through S11, S12) is supplied to the humidity control space (S0) and adsorbed in the heat exchange chamber (S12, S11) where the adsorption heat exchanger (102, 101), which is a condenser, is installed.
  • a dehumidifying device comprising a second adsorption block (302) provided at a position downstream of the adsorption heat exchanger (102).
  • air to be supplied to the humidity control space (S0) is circulated in the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator.
  • the adsorption heat exchanger (101, 102) serving as an evaporator.
  • moisture in the air can be adsorbed on the adsorbents of the adsorption heat exchanger (101, 102) and the adsorption block (301, 302) to dehumidify the air.
  • Adsorption heat exchange is performed in the air by circulating air to regenerate the adsorbent in the heat exchange chamber (S12, S11) where the adsorption heat exchanger (102, 101), which is a condenser, is provided.
  • the air in the first and second heat exchange chambers (S11, S12) is obtained by adding the first and second adsorption blocks (301, 302) to the first and second heat exchange chambers (S11, S12), respectively.
  • the amount of dehumidification can be increased.
  • the adsorption heat exchanger (101, 102) when the adsorption heat exchanger (101, 102) is an evaporator, the adsorption heat exchanger (101, 102) By disposing the adsorption block (301, 302) at the downstream position, the air dehumidified and cooled by the adsorption heat exchanger (101, 102) can be supplied to the adsorption block (301, 302). Thereby, adsorption
  • the switching mechanism (200) is configured such that the flow direction of air passing through each of the first and second adsorption heat exchangers (101, 102) is the adsorption heat exchanger.
  • a dehumidifier characterized by switching the air flow so that the opposite direction is obtained when the (101,102) is an evaporator and when the adsorption heat exchanger (101,102) is a condenser. is there.
  • the adsorption block (301, 302) is adsorbed when the adsorption heat exchanger (101, 102) is an evaporator.
  • the adsorption heat exchanger (101, 102) is a condenser, it is located on the upstream side of the adsorption heat exchanger (101, 102). That is, in each of the first and second heat exchange chambers (S11, S12), the air supplied to the heat exchange chambers (S11, S12) is the case where the adsorption heat exchanger (101, 102) is an evaporator.
  • the switching mechanism (200) is such that the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) is the adsorption heat exchanger.
  • a dehumidifier characterized by switching the air flow so that the direction is the same when the (101, 102) is an evaporator and when the adsorption heat exchanger (101, 102) is a condenser. is there.
  • the adsorption block (301, 302) in each of the first and second heat exchange chambers (S11, S12), includes the case where the adsorption heat exchanger (101, 102) is an evaporator and the adsorption heat exchange. In either case where the condenser (101, 102) is a condenser, it is located downstream of the adsorption heat exchanger (101, 102).
  • the air dehumidified and cooled by the adsorption heat exchanger (101, 102) can be supplied to the adsorption block (301,302), and when the adsorption heat exchanger (101,102) is a condenser, the air heated by the adsorption heat exchanger (101,102) is supplied to the adsorption block (301,302) can do.
  • the first and second adsorption blocks (301, 302) are respectively connected to the first and second adsorption heat exchangers (101, 102). It is a dehumidifier characterized by being arranged at intervals.
  • the adsorption block (301, 302) is disposed in the first and second heat exchange chambers (S11, S12) at a distance from the adsorption heat exchanger (101, 102). 301, 302) can suppress temperature distribution deviation and air drift.
  • the first and second adsorption blocks (301, 302) are respectively connected to the first and second adsorption heat exchangers (101, 102).
  • the dehumidifying device is arranged so as to be in contact with each other.
  • the adsorption heat exchange is performed by arranging the adsorption block (301, 302) in contact with the adsorption heat exchanger (101, 102) in each of the first and second heat exchange chambers (S11, S12). Heat conduction between the vessel (101, 102) and the adsorption block (301, 302) can be promoted. That is, when the adsorption heat exchanger (101, 102) is an evaporator, the adsorption block (301, 302) can be cooled by the endothermic action of the refrigerant flowing through the adsorption heat exchanger (101, 102). When (101,102) is a condenser, the adsorption block (301,302) can be heated by the heat radiation action of the refrigerant flowing through the adsorption heat exchanger (101,102).
  • a sixth invention includes the dehumidifying device (10) of the second invention and a heater (21) for heating air for regenerating the adsorbent, wherein the switching mechanism (200) is the first device.
  • the air that has passed through the heater (21) enters the heat exchange chamber (S12, S11) in which the adsorption heat exchanger (102, 101) serving as a condenser is provided.
  • It is a dehumidification system characterized by switching the flow of air so that it circulates.
  • the air supplied to the heat exchange chamber (S11, S12) is the evaporator of the adsorption heat exchanger (101, 102). Is passed through the adsorption heat exchanger (101,102) and then through the adsorption block (301,302), and when the adsorption heat exchanger (101,102) is a condenser, the adsorption block (301,302) ) And the adsorption heat exchanger (101, 102).
  • the heat exchange chamber (S11, S12) is circulated.
  • the air heated by the heater (21) can be supplied to the adsorption block (301, 302) located upstream of the adsorption heat exchanger (101, 102) which is the condenser.
  • an adsorption heat exchanger (101, 102) which carries an adsorbent and serves as an evaporator of the first and second heat exchange chambers (S11, S12).
  • An adsorption rotor (70) having a regeneration unit (72) for regenerating the adsorbent is further provided, and the adsorption heat exchanger (101, 102) serving as an evaporator in the first and second heat exchange chambers (S11, S12).
  • the air that has passed through the heat exchange chambers (S11, S12) provided with a) passes through the adsorption portion (71) of the adsorption rotor (70) and is supplied to the humidity control space (S0), and the switching mechanism ( 200) is a heat exchange provided with an adsorption heat exchanger (102, 101) which is a condenser in the first and second heat exchange chambers (S11, S12).
  • a dehumidification system that switches the flow of air so that the air that has passed through the heater (21) and the regeneration section (72) of the adsorption rotor (70) flows in sequence to the chambers (S12, S11) It is.
  • the air to be supplied to the humidity control space (S0) is dehumidified in the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator. Later, it is further dehumidified in the adsorption part (71) of the adsorption rotor (70).
  • the air heated by the heater (21) passes through the regeneration section (72) of the adsorption rotor (70), and then is provided with an adsorption heat exchanger (102, 101) serving as a condenser. Pass through (S12, S11). That is, the air that has passed through the regeneration unit (72) of the adsorption rotor (70) can be used for regeneration of the adsorbent of the adsorption heat exchanger (102, 101) and the adsorption block (302, 301).
  • the first and second inventions it is possible to increase the amount of air dehumidified in the first and second heat exchange chambers (S11, S12), and further, Since adsorption
  • the air heated by the adsorption heat exchanger (101, 102) can be supplied to the adsorption block (301, 302).
  • the regeneration of the adsorbent of the adsorption block (301, 302) can be promoted.
  • the temperature distribution bias and air drift in the adsorption block (301, 302) can be suppressed, the decrease in adsorption capacity and regeneration capacity in the adsorption block (301, 302) can be suppressed.
  • heat conduction between the adsorption heat exchanger (101,102) and the adsorption block (301,302) can be promoted, so that moisture is adsorbed and adsorbed on the adsorbent in the adsorption block (301,302).
  • the regeneration of the agent can be promoted.
  • the adsorption block (301, 302) located upstream of the adsorption heat exchanger (101, 102) serving as a condenser in the heat exchange chamber (S11, S12) is provided with a heater (21). Therefore, the regeneration of the adsorbent of the adsorption block (301, 302) can be promoted.
  • the dehumidifying capacity of the dehumidifying system (1) can be improved by adding the adsorption rotor (70).
  • the air that has passed through the regeneration unit (72) of the adsorption rotor (70) can be used for regeneration of the adsorbent of the adsorption heat exchanger (102, 101) and the adsorption block (302, 301), the heater (21) The air heated by can be used effectively.
  • FIG. Schematic for demonstrating the structure of the dehumidification apparatus of Embodiment 1, and the flow of the air in 1st dehumidification operation
  • FIG. Schematic for demonstrating the structure of the dehumidification apparatus of Embodiment 2, and the flow of the air in 1st dehumidification operation
  • FIG. The piping system figure for demonstrating the structural example of the dehumidification system of Embodiment 3.
  • FIG. The piping system diagram for demonstrating the structural example of the dehumidification system of Embodiment 4.
  • FIG. 1 shows a configuration example of a dehumidification system (1) according to the first embodiment.
  • This dehumidification system (1) dehumidifies air (in this example, outdoor air (OA)) and supplies it to the humidity control space (S0).
  • the humidity control space (S0) is configured by an indoor space (S1).
  • the indoor space (S1) is a space where supply of air having a low dew point temperature (for example, air having a dew point temperature of about ⁇ 30 ° C. to ⁇ 50 ° C.) is required, and is provided, for example, in a lithium battery production line It is a dry clean room.
  • the dehumidification system (1) includes a dehumidifier (10) and a controller (20).
  • the dehumidifier (10) is provided with an air supply passage (P1) and a regeneration passage (P2).
  • the dehumidifier (10) includes first and second heat exchange chambers (S11, S12), a refrigerant circuit (100), a switching mechanism (200), and first and second adsorption blocks (301, 302). Yes.
  • Air to be supplied to the humidity control space (S0) (in this example, air to be supplied to the indoor space (S1)) flows through the air supply passage (P1).
  • the air supply passage (P1) is configured to take outdoor air (OA) from the outdoor space and supply supply air (RA) to the indoor space (S1).
  • the air supply passage (P1) includes a first air supply passage portion (P11) whose inflow end is connected to the outdoor space, and a second air supply passage whose outflow end is connected to the indoor space (S1). Part (P12).
  • a cooler (11) is provided in the first air supply passage (P1) of the air supply passage (P1), and a drain pan (12) is provided in the vicinity of the cooler (11). Yes.
  • Air for regenerating the adsorbent flows through the regeneration passage (P2).
  • the regeneration passage (P2) is configured to take in indoor air (RA) from the indoor space (S1) and discharge exhaust air (EA) to the outdoor space.
  • the regeneration passage (P2) includes a first regeneration passage portion (P21) whose inflow end is connected to the indoor space (S1) and a second regeneration passage portion (P22) whose outflow end is connected to the outdoor space. ).
  • part of the air in the indoor space (S1) is discharged to the outdoor space as exhaust air (EA) without passing through the regeneration passage (P2).
  • the first and second heat exchange chambers (S11, S12) incorporate one heat exchange chamber into the supply passage (P1) as a part of the supply passage (P1) and the other heat exchange chamber as a regeneration passage (P2). ) Can be incorporated into the regeneration passage (P2) as a part of. Specifically, each of the first and second heat exchange chambers (S11, S12) is between the outflow end of the first supply passage portion (P11) and the inflow end of the second supply passage portion (P12).
  • the cooler (11) cools and dehumidifies outdoor air (OA).
  • the cooler (11) may be configured by a heat exchanger (specifically, a fin-and-tube heat exchanger) that functions as an evaporator of a refrigerant circuit (not shown).
  • the drain pan (12) collects the water condensed in the cooler (11).
  • the drain pan (12) is configured by a container having an open upper surface and disposed below the cooler (11) so that water condensed in the cooler (11) can be received.
  • the cooler (11) is provided in the first air supply passage portion (P11) of the air supply passage (P1).
  • the refrigerant circuit (100) circulates refrigerant to execute a refrigeration cycle operation.
  • Each of the first and second adsorption heat exchangers (101, 102) is configured by supporting an adsorbent on the surface of a heat exchanger (for example, a cross fin type fin-and-tube heat exchanger).
  • the first and second adsorption heat exchangers (101, 102) are provided in the first and second heat exchange chambers (S11, S12), respectively.
  • As the adsorbent zeolite, silica gel, activated carbon, an organic polymer material having a hydrophilic functional group may be used, or a material having not only a function of adsorbing moisture but also a function of absorbing moisture (so-called “concentration”). Adhesive) may be used.
  • the generic name of the first and second adsorption heat exchangers (101, 102) is simply referred to as “adsorption heat exchanger (101, 102)”.
  • the compressor (103) compresses and discharges the refrigerant. Moreover, the compressor (103) is comprised so that a rotation speed (operation frequency) can be changed by control of a controller (20).
  • the compressor (103) is configured by a variable capacity compressor (rotary, swing, scroll, etc. compressor) whose rotation speed can be adjusted by an inverter circuit (not shown).
  • the expansion valve (104) adjusts the pressure of the refrigerant.
  • the expansion valve (104) is configured by an electronic expansion valve that can change the opening degree in response to control by the controller (20).
  • the four-way switching valve (105) has first to fourth ports, the first port is connected to the discharge side of the compressor (103), and the second port is connected to the suction side of the compressor (103).
  • the third port is connected to the end of the second adsorption heat exchanger (102), and the fourth port is connected to the end of the first adsorption heat exchanger (101).
  • the four-way switching valve (105) is in a first connection state (a state indicated by a solid line in FIG. 1) and a second connection state (a state indicated by a broken line in FIG. 1). ) And can be set.
  • the refrigerant circuit (100) uses the first adsorption heat exchanger (101) as an evaporator to dehumidify the air and to remove the second adsorption heat exchanger ( 102) becomes a condenser and performs a first refrigeration cycle operation (first operation) that humidifies air (that is, regenerates the adsorbent).
  • the refrigerant circuit (100) serves as the first adsorption heat exchanger (102) for dehumidifying the air by using the evaporator as the second adsorption heat exchanger (102).
  • the second refrigeration cycle operation (second operation) is performed in which the vessel (101) becomes a condenser to humidify the air (that is, regenerate the adsorbent).
  • the refrigerant circuit (100) is configured to be able to execute the first and second refrigeration cycle operations in response to the control by the controller (20).
  • the refrigerant circuit (100) is configured to alternately perform the first and second refrigeration cycle operations.
  • the refrigerant that dissipates heat and condenses in the second adsorption heat exchanger (102) is decompressed by the expansion valve (104), and then flows into the first adsorption heat exchanger (101).
  • the first adsorption heat exchanger (101) an adsorption operation in which moisture in the air is adsorbed by the adsorbent is performed, and the adsorption heat generated at that time is imparted to the refrigerant.
  • the refrigerant that has absorbed heat and evaporated in the first adsorption heat exchanger (101) is sucked into the compressor (103) and compressed.
  • the second adsorption heat exchanger (102) an adsorption operation in which moisture in the air is adsorbed by the adsorbent is performed, and adsorption heat generated at that time is imparted to the refrigerant.
  • the refrigerant that has absorbed heat and evaporated in the second adsorption heat exchanger (102) is sucked into the compressor (103) and compressed.
  • the switching mechanism (200) changes the connection state between the first and second heat exchange chambers (S11, S12), the supply passage (P1), and the regeneration passage (P2),
  • the first passage state (state indicated by the solid line in FIG. 1) and the second passage state (state indicated by the broken line in FIG. 1) can be set.
  • First passage state When the connection state of the first and second heat exchange chambers (S11, S12) becomes the first passage state, the first heat exchange chamber (S11) is located between the first and second air supply passage portions (P11, P12). Is connected to the intake passage (P1) and the second heat exchange chamber (S12) is connected between the first and second regeneration passage portions (P21, P22) and incorporated into the regeneration passage (P2). It is.
  • the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the first passage state when the four-way switching valve (105) is in the first connection state, When the four-way switching valve (105) is in the second connection state, the connection state of the first and second heat exchange chambers (S11, S12) is set to the second passage state.
  • the switching mechanism (200) is configured such that the heat exchange chamber provided with the adsorption heat exchanger serving as an evaporator of the first and second heat exchange chambers (S11, S12) is provided in the supply passage (P1).
  • the switching mechanism (200) has the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator among the first and second heat exchange chambers (S11, S12).
  • Passed air is supplied to the humidity control space (S0), and air for regenerating the adsorbent flows in the heat exchange chamber (S12, S11) where the adsorption heat exchanger (102, 101), which is a condenser, is installed. The air flow is switched.
  • connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (that is, the first heat exchange chamber (S11) is a part of the air supply passage (P1).
  • the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state.
  • the flow direction is the same as the flow direction of the air passing through the first adsorption heat exchanger (101). (So-called parallel flow).
  • the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) is switched from the evaporator to the condenser (or from the condenser to the evaporator). It doesn't change. That is, the switching mechanism (200) has a case where the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) is the same as when the adsorption heat exchanger (101, 102) is an evaporator. The air flow is switched so that the adsorption heat exchanger (101, 102) is in the same direction as the condenser.
  • Each of the first and second adsorption blocks (301, 302) is configured to carry an adsorbent and bring air into contact with the adsorbent.
  • each of the first and second adsorption blocks (301, 302) is configured by supporting an adsorbent on the surface of a structure (specifically, a structure having a honeycomb structure).
  • the first and second adsorption blocks (301, 302) are provided in the first and second heat exchange chambers (S11, S12), respectively.
  • the generic name of the first and second adsorption blocks (301, 302) is simply referred to as “adsorption block (301, 302)”.
  • the first adsorption block (301) is located downstream of the first adsorption heat exchanger (101) when the first adsorption heat exchanger (101) is an evaporator in the first heat exchange chamber (S11) ( Air dehumidified by the first adsorption heat exchanger (101) passes when the position becomes the leeward side (that is, when the first heat exchange chamber (S11) is incorporated as a part of the air supply passage (P1)) Position).
  • the connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (shown by the solid line in FIG. 1). In this case, it is disposed at a position downstream of the first adsorption heat exchanger (101).
  • the second adsorption heat exchanger (102) when the second adsorption heat exchanger (102) is an evaporator in the second heat exchange chamber (S12), the second adsorption block (302) has the second adsorption heat exchanger (102).
  • the second adsorption heat exchanger (102) On the downstream side (leeward side) (that is, when the second heat exchange chamber (S12) is incorporated as a part of the air supply passage (P1), the second adsorption heat exchanger (102) removes the moisture. At a position where the generated air passes).
  • the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state (indicated by the broken line in FIG. 1).
  • the second adsorption heat exchanger (102) is disposed at a position downstream of the second adsorption heat exchanger (102).
  • the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) depends on whether the adsorption heat exchanger (101, 102) is an evaporator or the adsorption heat exchange.
  • the direction is the same as when the condenser (101, 102) is a condenser. Therefore, when the connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (the state indicated by the solid line in FIG.
  • the downstream side of the first adsorption heat exchanger (101) Is located downstream of the first adsorption heat exchanger (101) when the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state (shown by the broken line in FIG. 1). It is the same position as the side position.
  • the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state (the state indicated by the broken line in FIG. 1)
  • the second adsorption heat exchanger (102) The position on the downstream side is the second adsorption heat exchanger (102 when the connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (the state shown by the solid line in FIG. 1).
  • the adsorption block (301, 302) includes an adsorption heat exchanger (101, 102) as an evaporator and an adsorption heat exchanger (101, 102). In either case of a condenser, it is located downstream of the adsorption heat exchanger (101, 102).
  • the controller (20) controls the dehumidifier (10) based on detection values of various sensors (for example, a temperature sensor, a humidity sensor, etc.).
  • the controller (20) is constituted by a CPU and a memory.
  • the dehumidifier (10) repeats the first and second dehumidifying operations alternately at a predetermined time interval (for example, every 10 minutes).
  • First dehumidifying operation In the first dehumidifying operation, the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the first connection state (the state shown by the solid line in FIG. 1). .
  • the refrigerant circuit (100) performs a first refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as an evaporator and the second adsorption heat exchanger (102) serves as a condenser. Further, the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the first passage state (the state indicated by the solid line in FIG. 1).
  • the air taken into the supply passage (P1) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11), and then supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption heat exchanger (101) functioning as an evaporator. At this time, moisture in the air passing through the first adsorption heat exchanger (101) is adsorbed by the adsorbent of the first adsorption heat exchanger (101). Further, the heat of adsorption generated during the adsorption is absorbed by the refrigerant flowing through the first adsorption heat exchanger (101).
  • the first adsorption heat exchanger (101) functioning as an evaporator is deprived of moisture by the adsorbent of the first adsorption heat exchanger (101), the humidity decreases, It is cooled by the endothermic action of the refrigerant flowing through the first adsorption heat exchanger (101), and the temperature also decreases.
  • the air dehumidified and cooled by the first adsorption heat exchanger (101) passes through the first adsorption block (301). At this time, moisture in the air is adsorbed on the adsorbent of the first adsorption block (301).
  • the air dehumidified by the first adsorption heat exchanger (101) is further dehumidified by the first adsorption block (301).
  • the air dehumidified after passing through the first adsorption heat exchanger (101) and the first adsorption block (301) is supplied to the indoor space (S1) as supply air (SA).
  • the second adsorption heat exchanger (102) functioning as a condenser is given moisture from the adsorbent of the second adsorption heat exchanger (102), the humidity rises, It is heated by the heat radiation action of the refrigerant flowing through the second adsorption heat exchanger (102), and the temperature also rises.
  • the air humidified and heated by the second adsorption heat exchanger (102) passes through the second adsorption block (302).
  • the moisture of the adsorbent of the second adsorption block (302) is released to the air passing through the second adsorption block (302).
  • the adsorbent of the second adsorption block (302) is regenerated.
  • the air that has passed through the second adsorption heat exchanger (102) and the second adsorption block (302) is exhausted to the outdoor space as exhaust air (EA).
  • the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the second connection state (the state indicated by the broken line in FIG. 1). .
  • the refrigerant circuit (100) performs a second refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as a condenser and the second adsorption heat exchanger (102) serves as an evaporator.
  • the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the second passage state (the state indicated by the broken line in FIG. 1).
  • the air taken into the supply passage (P1) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11), and then supplied to the second heat exchange chamber (S12).
  • the air supplied to the second heat exchange chamber (S12) passes through the second adsorption heat exchanger (102) functioning as an evaporator.
  • the air passing through the second adsorption heat exchanger (102) functioning as an evaporator is deprived of moisture by the adsorbent of the second adsorption heat exchanger (102), and the humidity decreases.
  • the refrigerant is cooled by the endothermic action of the refrigerant flowing through the two-adsorption heat exchanger (102), and the temperature also decreases.
  • the air dehumidified and cooled by the second adsorption heat exchanger (102) passes through the second adsorption block (302). At this time, moisture in the air is adsorbed to the adsorbent of the second adsorption block (302). Thereby, the air dehumidified by the second adsorption heat exchanger (102) is further dehumidified by the second adsorption block (302).
  • the air dehumidified after passing through the second adsorption heat exchanger (102) and the second adsorption block (302) is supplied to the indoor space (S1) as supply air (SA).
  • the -Air flow in the regeneration passage- Air (in this example, room air (RA)) taken into the regeneration passage (P2) is supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption heat exchanger (101) functioning as a condenser.
  • the air passing through the first adsorption heat exchanger (101) functioning as a condenser is given moisture from the adsorbent of the first adsorption heat exchanger (101), and the humidity rises.
  • the air humidified and heated by the first adsorption heat exchanger (101) passes through the first adsorption block (301).
  • the moisture of the adsorbent of the first adsorption block (301) is released to the air passing through the first adsorption block (301).
  • the adsorbent of the first adsorption block (301) is regenerated.
  • the air that has passed through the first adsorption heat exchanger (101) and the first adsorption block (301) is exhausted to the outdoor space as exhaust air (EA).
  • the central view is a plan view of the dehumidifying device (10)
  • the right view is a right side view of the dehumidifying device (10)
  • the left view is a left side view of the dehumidifying device (10). It is.
  • the dehumidifier (10) includes a casing (41) that houses the components of the refrigerant circuit (100).
  • the casing (41) is formed in a substantially flat and relatively low rectangular parallelepiped shape, and has a front panel (42), a rear panel (43), a left side panel (44), and a right side panel (45). ing.
  • the longitudinal direction of the casing (41) is the front-rear direction.
  • the casing (41) has an adsorption side suction port (51), a regeneration side suction port (52), an air supply port (53), and an exhaust port (54).
  • the suction side suction port (51) is provided in the upper part of the back panel (43), and the regeneration side suction port (52) is provided in the lower part of the back panel (43).
  • the air supply port (53) is provided near the end of the right side panel (45) on the front panel (42) side, and the exhaust port (54) is provided on the left side panel (44) on the front panel (42) side. It is provided near the end.
  • a first partition plate (46), a second partition plate (47), and a central partition plate (48) are provided in the internal space of the casing (41). These partition plates (46, 47, 48) are installed upright on the bottom plate of the casing (41) and partition the internal space of the casing (41) from the bottom plate of the casing (41) to the top plate. Yes.
  • the first and second partition plates (46, 47) are arranged at a predetermined interval in the front-rear direction of the casing (41) in a posture parallel to the front panel (42) and the rear panel (43).
  • the first partition plate (46) is disposed closer to the rear panel (43), and the second partition plate (47) is disposed closer to the front panel (42).
  • the arrangement of the central partition plate (48) will be described later.
  • the space between the first partition plate (46) and the back panel (43) is partitioned into two upper and lower spaces, and the lower space is the first adsorption side internal passage (S21).
  • the upper space constitutes the first reproduction side internal passage (S22).
  • the first adsorption side internal passage (S21) communicates with the outdoor space via a duct (corresponding to the first air supply passage portion (P11) in FIG. 1) connected to the adsorption side suction port (51).
  • the first regeneration side internal passage (S22) communicates with the indoor space (S1) via a duct (corresponding to the first regeneration passage portion (P21) in FIG. 1) connected to the regeneration side suction port (52). Yes.
  • An adsorption side filter (63) is installed in the first adsorption side internal passage (S21), and a regeneration side filter (64) is installed in the first regeneration side internal passage (S22).
  • the space between the first partition plate (46) and the second partition plate (47) is partitioned on the left and right by the center partition plate (48).
  • the space on the left side constitutes the first heat exchange chamber (S11), and the space on the right side of the central partition plate (48) constitutes the second heat exchange chamber (S12).
  • a first adsorption heat exchanger (101) is accommodated in the first heat exchange chamber (S11), and a second adsorption heat exchanger (102) is accommodated in the second heat exchange chamber (S12).
  • the second heat exchange chamber (S12) accommodates an expansion valve (104) (not shown) of the refrigerant circuit (100).
  • Each of the first and second adsorption heat exchangers (101, 102) is formed into a rectangular thick plate shape or flat rectangular parallelepiped shape as a whole, and two main surfaces (wide side surfaces) facing each other are surfaces through which air passes. It has become.
  • the 1st adsorption heat exchanger (101) stood up in the 1st heat exchange room (S11) with the posture where the two principal surfaces became parallel to the 1st and 2nd partition plates (46, 47). It is installed in a state.
  • the second adsorptive heat exchanger (102) has a configuration in which the two main surfaces thereof are parallel to the first and second partition plates (46, 47) and in the second heat exchange chamber (S12). It is installed in a standing state.
  • Each of the first and second adsorption blocks (301, 302) is formed in a rectangular thick plate shape or flat rectangular parallelepiped shape as a whole, and two main surfaces (wide side surfaces) facing each other serve as surfaces through which air passes. ing.
  • each of the first and second adsorption blocks (301, 302) is a honeycomb-like structure having a large number of holes penetrating from one main surface to the other main surface.
  • the first adsorption block (301) stands up in the first heat exchange chamber (S11) with its two main surfaces parallel to the first and second partition plates (46, 47). is set up.
  • the second adsorption block (302) stands up in the second heat exchange chamber (S12) with its two main surfaces parallel to the first and second partition plates (46, 47). Installed.
  • the first adsorption block (301) is disposed between the first adsorption heat exchanger (101) and the second partition plate (47) in the first heat exchange chamber (S11), and the second The adsorption block (302) is disposed between the second adsorption heat exchanger (102) and the second partition plate (47) in the second heat exchange chamber (S12).
  • the first adsorption block (301) is spaced apart from the first adsorption heat exchanger (101) in the front-rear direction
  • the second adsorption block (302) is arranged in the second adsorption heat exchanger (101) in the front-rear direction. 102) and spaced apart.
  • the space along the front surface of the second partition plate (47) is vertically partitioned, and the upper part of the vertically partitioned space is the second suction side interior.
  • the passage (S23) is configured, and the lower part configures the second regeneration side internal passage (S24).
  • the first partition plate (46) is provided with first to fourth dampers (D1 to D4), and the second partition plate (47) is provided with fifth to eighth dampers (D5 to D8). Yes.
  • Each of the first to eighth dampers (D1 to D8) is configured to be switchable between an open state and a closed state in response to control by the controller (20).
  • These first to eighth dampers (D1 to D8) constitute a switching mechanism (200).
  • the first damper (D1) is attached to the right side of the central partition plate (48) in the upper portion of the first partition plate (46) (the portion facing the first regeneration side internal passage (S22)), and the second damper (D2) is attached to the left side of the central partition plate (48) in the upper part of the first partition plate (46).
  • the third damper (D3) is attached to the right side of the central partition plate (48) in the lower portion of the first partition plate (46) (the portion facing the first suction side internal passage (S21)).
  • the damper (D4) is attached to the left side of the central partition plate (48) in the lower portion of the first partition plate (46).
  • the fifth damper (D5) is attached to the right side of the central partition plate (48) in the upper portion of the second partition plate (47) (the portion facing the second suction side internal passage (S23)).
  • (D6) is attached to the left side of the central partition plate (48) in the upper part of the second partition plate (47).
  • the seventh damper (D7) is attached to the right side of the central partition plate (48) in the lower portion of the second partition plate (47) (the portion facing the second regeneration side internal passage (S24)),
  • the damper (D8) is attached to the left side of the central partition plate (48) in the lower portion of the second partition plate (47).
  • the space between the second adsorption side internal passage (S23) and the second regeneration side internal passage (S24) and the front panel (42) is partitioned left and right by the partition plate (49).
  • the space on the right side of the partition plate (49) constitutes an air supply fan chamber (S25), and the space on the left side of the partition plate (49) constitutes an exhaust fan chamber (S26).
  • the air supply fan chamber (S25) communicates with the indoor space (S1) through a duct (corresponding to the second air supply passage portion (P12) in FIG. 1) connected to the air supply port (53).
  • the exhaust fan chamber (S26) communicates with the outdoor space via a duct (corresponding to the second regeneration passage portion (P22) in FIG. 1) connected to the exhaust port (54).
  • the supply fan chamber (S25) accommodates the supply fan (61), and the exhaust fan chamber (S26) accommodates the exhaust fan (62).
  • the air supply fan (61) has an air outlet connected to the air supply port (53), and blows air sucked in from the second partition (47) side to the air supply port (53).
  • the exhaust fan (62) has an outlet connected to the exhaust outlet (54), and blows out air sucked from the second partition (47) side to the exhaust outlet (54).
  • each of the air supply fan (61) and the exhaust fan (62) is constituted by a centrifugal multiblade fan (so-called sirocco fan).
  • the compressor fan (103) and the four-way switching valve (105) (not shown) of the refrigerant circuit (100) are accommodated in the air supply fan chamber (S25).
  • the first adsorption heat exchanger (101) serves as an evaporator
  • the second adsorption heat exchanger (102) serves as a condenser.
  • the first, fourth, sixth and seventh dampers (D1, D4, D6, D7) are opened
  • the second, third, fifth and eighth dampers (D2, D3) are opened.
  • D5, D8) are closed.
  • connection state of the first and second heat exchange chambers (S11, S12) is set to the first passage state (the state shown by the solid line in FIG. 1), and the first heat exchange chamber (S11) is set to the air supply passage. (P1) and the second heat exchange chamber (S12) is incorporated into the regeneration passage (P2).
  • the air (in this example, outdoor air (OA)) supplied to the first adsorption side internal passage (S21) via the adsorption side suction port (51) passes through the adsorption side filter (63), It passes through 4 dampers (D4) and is supplied to the first heat exchange chamber (S11).
  • OA outdoor air
  • the dehumidified air that has passed through the first adsorption heat exchanger (101) and the first adsorption block (301) passes through the sixth damper (D6) and flows into the second adsorption side internal passage (S23).
  • the air passes through the air fan chamber (S25) and the air supply port (53) and is supplied to the indoor space (S1) as supply air (SA).
  • RA room air
  • Air flow in the second dehumidifying operation by the dehumidifying device (10) of the first embodiment will be described with reference to FIG.
  • the first adsorption heat exchanger (101) serves as a condenser
  • the second adsorption heat exchanger (102) serves as an evaporator.
  • the second, third, fifth, and eighth dampers (D2, D3, D5, and D8) are opened, and the first, fourth, sixth, and seventh dampers (D1, D4) are opened. , D6, D7) are closed.
  • connection state of the first and second heat exchange chambers (S11, S12) is set to the second passage state (the state indicated by the broken line in FIG. 1), and the first heat exchange chamber (S11) is set to the regeneration passage ( P2) and the second heat exchange chamber (S12) is incorporated into the air supply passage (P1).
  • OA outdoor air
  • the dehumidified air that has passed through the second adsorption heat exchanger (102) and the second adsorption block (302) passes through the fifth damper (D5) and flows into the second adsorption side internal passage (S23).
  • the air passes through the air fan chamber (S25) and the air supply port (53) and is supplied to the indoor space (S1) as supply air (SA).
  • RA room air
  • the first and second heat exchange chambers (301, 302) are added to the first and second heat exchange chambers (S11, S12).
  • the amount of dehumidified air in S11 and S12) can be increased.
  • the first adsorption block (301) is located at a position where the air dehumidified by the first adsorption heat exchanger (101) passes.
  • the air dehumidified and cooled by the first adsorption heat exchanger (101) can be supplied to the first adsorption block (301).
  • moisture content to adsorption agent can be accelerated
  • the air dehumidified and cooled by the second adsorption heat exchanger (102) is transferred to the second adsorption block. Since it can be supplied to (302), the adsorption of moisture to the adsorbent can be promoted in the second adsorption block (302). That is, in each of the first and second heat exchange chambers (S11, S12), when the adsorption heat exchanger (101, 102) is an evaporator, the adsorption is performed at a position downstream of the adsorption heat exchanger (101, 102).
  • the air dehumidified and cooled by the adsorption heat exchanger (101,102) can be supplied to the adsorption block (301,302), so that the moisture to the adsorbent of the adsorption block (301,302) can be supplied. Adsorption can be promoted.
  • the amount of air dehumidified in the first and second heat exchange chambers (S11, S12) can be increased, and further, the adsorption of moisture to the adsorbent of the adsorption block (301, 302) can be promoted. Therefore, the dehumidifying capacity of the dehumidifying device (10) can be improved.
  • the increase in power consumption of the dehumidifying device (10) is suppressed. can do.
  • the adsorption block (301, 302) includes the case where the adsorption heat exchanger (101, 102) is an evaporator and the adsorption heat exchange.
  • the condenser (101, 102) is a condenser, it is located downstream of the adsorption heat exchanger (101, 102). Therefore, in the first heat exchange chamber (S11), when the first adsorption heat exchanger (101) is a condenser (that is, the first heat exchange chamber (S11) is incorporated in the regeneration passage (P2)).
  • the air heated by the first adsorption heat exchanger (101) can be supplied to the first adsorption block (301).
  • the first adsorption block (301) at a distance from the first adsorption heat exchanger (101), it is possible to suppress temperature distribution deviation and air drift in the first adsorption block (301). .
  • the temperature distribution and air drift can be suppressed in the first and second adsorption blocks (301, 302), the decrease in adsorption capacity and regeneration capacity in the first and second adsorption blocks (301, 302) is suppressed. can do.
  • the regeneration passage (P2) may be configured to take in outdoor air (OA) and discharge exhaust air (EA) to the outdoor space.
  • the inflow end of the first regeneration passage portion (P21) is connected to an intermediate portion of the first air supply passage portion (P11) (specifically, downstream of the cooler (11)).
  • Other configurations are the same as those shown in FIG.
  • the indoor air (RA) does not return from the indoor space (S1) toward the dehumidifier (10). Therefore, even if the indoor space (S1) is contaminated with chemical substances, etc., the indoor air (S1) is dehumidified by the dehumidifier (10) with the outdoor air (OA) that is cleaner than the indoor air (RA). Therefore, the cleanliness of the indoor space (S1) can be maintained.
  • the air supply passage (P1) may be configured to take in indoor air (RA) and supply supply air (SA) to the indoor space (S1).
  • the regeneration passage (P2) may be configured to take in outdoor air (OA) and discharge exhaust air (EA) to the outdoor space.
  • the inflow end of the first supply passage portion (P11) is connected to the indoor space (S1)
  • the inflow end of the first regeneration passage portion (P21) is connected to the outdoor space.
  • the cooler (11) is provided in the first regeneration passage portion (P21).
  • Other configurations are the same as those shown in FIG.
  • the indoor air (RA) with a low dew point is further dehumidified by the dehumidifier (10) and supplied to the indoor space (S1). ) Can be set to a lower dew point.
  • the dehumidification system (1) may include a pretreatment dehumidifier (30) in addition to the dehumidifier (10) and the controller (20) shown in FIG.
  • the humidity control space (S0) includes an indoor space (S1) and a chamber (S2) provided in the indoor space (S1).
  • the indoor space (S1) is a space where supply of air having a low dew point temperature (for example, air having a dew point temperature of about ⁇ 30 ° C.) is required, and the chamber (S2) has a dew point higher than that of the indoor space (S1).
  • the dehumidification system (1) is provided with a pretreatment passage (P3) and a posttreatment passage (P4). And in this dehumidification system (1), the air (in this example, outdoor air (OA)) dehumidified by the pretreatment dehumidifier (30) is supplied to the indoor space (S1) as supply air (SA0), Air dehumidified by the dehumidifier (10) (in this example, room air (RA)) is supplied to the chamber (S2) as supply air (SA).
  • the controller (20) controls the dehumidifier (10) and the pretreatment dehumidifier (30) based on the detection values of the various sensors.
  • Pretreatment passage Air to be supplied to the humidity control space (S0) (in this example, air to be supplied to the indoor space (S1)) flows through the pretreatment passage (P3).
  • the pretreatment passage (P3) is configured to take outdoor air (OA) from the outdoor space and supply supply air (SA0) to the indoor space (S1).
  • the pretreatment passage (P3) includes a first pretreatment passage portion (P31) whose inflow end is connected to the outdoor space and a second pretreatment passage whose outflow end is connected to the indoor space (S1). Part (P32).
  • the cooler (11) is provided in the first pretreatment passage portion (P31).
  • the post-processing passage (P4) air for regenerating the adsorbent (in this example, air supplied from the regeneration passage (P2)) flows.
  • the post-processing passage (P4) is configured to take in air from the outflow end of the regeneration passage (P2) and discharge the exhaust air (EA) to the outdoor space.
  • the post-processing passage (P4) includes a first post-processing passage portion (P41) whose inflow end is connected to the outflow end of the regeneration passage (P2) and a second outflow end connected to the outdoor space. And a post-processing passage portion (P42).
  • part of the air in the chamber (S2) is discharged to the outdoor space as exhaust air (EA) without passing through the indoor space (S1), and is a part of the air in the indoor space (S1).
  • the section is discharged into the outdoor space as exhaust air (EA) without passing through the regeneration path (P2) and the post-processing path (P4).
  • the supply passage (P1) is configured to take in indoor air (RA) from the indoor space (S1) and supply supply air (SA) to the chamber (S2).
  • the inflow end of the first supply passage portion (P11) is connected to the indoor space (S1)
  • the outflow end of the second supply passage portion (P12) is connected to the chamber (S2).
  • the regeneration passage (P2) is configured to take in indoor air (RA) from the indoor space (S1) and discharge the regeneration air (air for regenerating the adsorbent) to the post-treatment passage (P4). Yes.
  • the inflow end of the first regeneration passage portion (P21) is connected to the intermediate portion of the first supply air passage portion (P11), and the outflow end of the second regeneration passage portion (P22) is the first rear passage. It is connected to the inflow end of the processing passage (P41).
  • the pretreatment dehumidifier (30) has the same configuration as the dehumidifier (10).
  • the structure of the pretreatment dehumidifier (30) is the same as the structure of the dehumidifier (10) shown in FIG.
  • the refrigerant circuit (100) of the pretreatment dehumidifying device (30) responds to the control by the controller (20) in response to the first adsorption heat exchanger (101).
  • the air is dehumidified, and the first adsorption heat exchanger (101) serves as a condenser to alternately perform the second refrigeration cycle operation for regenerating the adsorbent.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) is responsive to the control by the controller (20) to the first and second heat exchange chambers (S11, S12) of the pretreatment dehumidifier (30).
  • the connection state between the pre-processing passage (P3) and the post-processing passage (P4) includes a third passage state (state shown by a solid line in FIG. 6) and a fourth passage state (state shown by a broken line in FIG. 6). It is configured to be configurable.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) is connected to the first and second heat exchange chambers (S11, S12) when the four-way switching valve (105) is in the first connection state. Is set to the third passage state, and when the four-way switching valve (105) is in the second connection state, the connection state of the first and second heat exchange chambers (S11, S12) is set to the third passage state. That is, the switching mechanism (200) of the pretreatment dehumidifier (30) is the same as the switching mechanism (200) of the dehumidifier (10) in the first and second heat exchange chambers (S11, S12).
  • the air that has passed through the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as a chamber is supplied to the humidity control space (S0) (in this example, the indoor space (S1)), Air for regenerating the adsorbent in the heat exchange chamber (S12, S11) provided with the adsorption heat exchanger (102, 101) serving as a condenser (in this example, the first and second dehumidifiers (10))
  • the flow of air is circulated so that the air passing through the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) that is the condenser in the heat exchange chamber (S11, S12) is circulated. Switch.
  • the connection state of the first and second heat exchange chambers (S11, S12) is the third passage state (that is, the first heat exchange chamber (S11). ) Is incorporated as part of the pretreatment passage (P3)), the flow direction of the air passing through the first adsorption heat exchanger (101) is the first and second heat exchange chambers (S11, S12).
  • the connection state is the fourth passage state (that is, when the first heat exchange chamber (S11) is incorporated as a part of the post-treatment passage (P4))
  • the first adsorption heat exchanger (101) is installed. It is the same direction as the flow direction of the passing air.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) passes through each of the first and second adsorption heat exchangers (101, 102), similarly to the switching mechanism (200) of the dehumidifier (10).
  • the air flow direction is the same when the adsorption heat exchanger (101,102) is an evaporator and when the adsorption heat exchanger (101,102) is a condenser. Switch the flow.
  • the pretreatment dehumidifier (30) repeats the third and fourth dehumidifying operations alternately at predetermined time intervals (for example, every 10 minutes).
  • the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the first connection state (the state shown by the solid line in FIG. 6).
  • the refrigerant circuit (100) performs a first refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as an evaporator and the second adsorption heat exchanger (102) serves as a condenser.
  • the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the third passage state (the state indicated by the solid line in FIG. 6).
  • the air taken into the pretreatment passage (P3) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11) and then supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption heat exchanger (101) and the first adsorption block (301) in order, the first adsorption heat exchanger (101) and Moisture is taken away by the adsorbent of the first adsorption block (301) and dehumidified.
  • the air dehumidified in the first heat exchange chamber (S11) is supplied to the indoor space (S1) as supply air (SA0).
  • the air taken into the post-processing passage (P4) (in this example, air supplied from the regeneration passage (P2)) is supplied to the second heat exchange chamber (S12).
  • the air supplied to the second heat exchange chamber (S12) sequentially passes through the second adsorption heat exchanger (102) and the second adsorption block (302), the second adsorption heat exchanger (102) and Water is applied from the adsorbent of the second adsorption block (302). Thereby, the adsorbent of the second adsorption heat exchanger (102) and the second adsorption block (302) is regenerated.
  • the air that has passed through the second heat exchange chamber (S12) is exhausted to the outdoor space as exhaust air (EA).
  • ⁇ 4th dehumidifying action In the fourth dehumidifying operation, the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the second connection state (the state indicated by the broken line in FIG. 6). .
  • the refrigerant circuit (100) performs a second refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as a condenser and the second adsorption heat exchanger (102) serves as an evaporator. Further, the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the fourth passage state (the state indicated by the broken line in FIG. 6).
  • the air taken into the pretreatment passage (P3) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11) and then supplied to the second heat exchange chamber (S12).
  • the air supplied to the second heat exchange chamber (S12) sequentially passes through the second adsorption heat exchanger (102) and the second adsorption block (302), the second adsorption heat exchanger (102) and Moisture is taken away by the adsorbent of the second adsorption block (302) and dehumidified.
  • the air dehumidified in the second heat exchange chamber (S12) is supplied to the indoor space (S1) as supply air (SA0).
  • the air taken into the post-processing passage (P4) (in this example, air supplied from the regeneration passage (P2)) is supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption heat exchanger (101) and the first adsorption block (301) in order, the first adsorption heat exchanger (101) and Water is applied from the adsorbent of the first adsorption block (301). Thereby, the adsorbent of the first adsorption heat exchanger (101) and the first adsorption block (301) is regenerated.
  • the air that has passed through the first heat exchange chamber (S11) is exhausted to the outdoor space as exhaust air (EA).
  • the air to be supplied to the indoor space (S1) (in this example, the outdoor air (OA)) is dehumidified by the pretreatment dehumidifier (30) and supplied to the indoor space (S1).
  • the indoor air (RA) supplied from the indoor space (S1) is dehumidified by the dehumidifier (10) and supplied to the chamber (S2) as the supply air (SA).
  • the dew point temperature of the air can be made lower than the dew point temperature of the air in the indoor space (S1).
  • the dehumidification system (1) can be operated more than when the entire indoor space (S1) is set to a low dew point. The power consumption required can be reduced.
  • FIG. 7 shows a configuration example of the dehumidification system (1) according to the second embodiment.
  • the dehumidifying system (1) includes a dehumidifying device (10), a controller (20), and a heater (21).
  • the structure of the dehumidification apparatus (10) of Embodiment 2 differs from the structure (FIG. 2) of the dehumidification apparatus (10) of Embodiment 1.
  • FIG. Specifically, the flow direction of the air passing through the first and second adsorption heat exchangers (101, 102) and the arrangement of the first and second adsorption blocks (301, 302) are different from those in the first embodiment. Other configurations are the same as those of the first embodiment.
  • the heater (21) is provided in the regeneration passage (P2) and is upstream of the heat exchange chamber in which the adsorption heat exchanger serving as a condenser is provided among the first and second heat exchange chambers (S11, S12). It is arranged on the side (windward side). That is, the heater (21) is configured to heat air for regenerating the adsorbent.
  • the heater (21) is disposed in the first regeneration passage portion (P21).
  • the heater (21) is constituted by a sensible heat exchanger that exchanges heat between the air flowing through the first regeneration passage (P21) and the air flowing through the second regeneration passage (P22).
  • a heat exchanger specifically, a fin-and-tube heat exchanger that functions as a condenser of a refrigerant circuit (not shown) may be used.
  • the refrigerant circuit (100) responds to the control by the controller (20), and the first adsorption heat exchanger (101) serves as an evaporator to dehumidify the air and the second adsorption heat exchanger.
  • the second refrigeration cycle operation for regenerating the adsorbent as a condenser is performed alternately.
  • the switching mechanism (200) changes the connection state of the first and second heat exchange chambers (S11, S12) to the first passage state (state shown by the solid line in FIG. 7). And a second passage state (state shown by a broken line in FIG. 7). Further, the switching mechanism (200) connects the first and second heat exchange chambers (S11, S12) when the four-way switching valve (105) is in the first connection state (the state shown by the solid line in FIG. 7). When the state is set to the first passage state and the four-way switching valve (105) is in the second connection state (the state indicated by the broken line in FIG.
  • the switching mechanism (200) includes a heat exchange chamber (S11, S12) provided with an adsorption heat exchanger (101, 102) serving as an evaporator among the first and second heat exchange chambers (S11, S12).
  • the air passing through the air is supplied to the humidity control space (S0), and the air for regenerating the adsorbent in the heat exchange chamber (S12, S11) provided with the adsorption heat exchanger (102, 101) serving as a condenser (
  • the air flow is switched so that the air passing through the heater (21) flows.
  • connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (that is, the first heat exchange chamber (S11) is a part of the air supply passage (P1).
  • the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state.
  • the flow direction of the air passing through the first adsorption heat exchanger (101) is opposite. (So-called counter flow).
  • the switching mechanism (200) has a case where the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) is the same as when the adsorption heat exchanger (101, 102) is an evaporator. The air flow is switched so that the adsorption heat exchanger (101, 102) is in the opposite direction to the case where it is a condenser.
  • the first adsorption block (301) is located downstream of the first adsorption heat exchanger (101) when the first adsorption heat exchanger (101) is an evaporator in the first heat exchange chamber (S11) ( Air dehumidified by the first adsorption heat exchanger (101) passes when the position becomes the leeward side (that is, when the first heat exchange chamber (S11) is incorporated as a part of the air supply passage (P1)) Position).
  • the second adsorption block (302) is located downstream of the second adsorption heat exchanger (102) when the second adsorption heat exchanger (102) is an evaporator in the second heat exchange chamber (S12). Air dehumidified by the second adsorption heat exchanger (102) passes when the position becomes the leeward side (that is, when the second heat exchange chamber (S12) is incorporated as a part of the air supply passage (P1)) Position).
  • the flow direction of the air passing through each of the first and second adsorption heat exchangers (101, 102) depends on whether the adsorption heat exchanger (101, 102) is an evaporator or the adsorption heat exchange.
  • the direction is opposite to the case where the condenser (101, 102) is a condenser. Therefore, when the connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (the state indicated by the solid line in FIG.
  • the downstream side of the first adsorption heat exchanger (101) Is located upstream of the first adsorption heat exchanger (101) when the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state (the state indicated by the broken line in FIG. 7). This is the same position as the position (in this example, the position between the heater (21) and the first adsorption heat exchanger (101)). Similarly, when the connection state of the first and second heat exchange chambers (S11, S12) is the second passage state (the state indicated by the broken line in FIG.
  • the second adsorption heat exchanger (102) The position on the downstream side is the second adsorption heat exchanger (102 when the connection state of the first and second heat exchange chambers (S11, S12) is the first passage state (the state shown by the solid line in FIG. 1). ) On the upstream side (in this example, the position between the heater (21) and the second adsorption heat exchanger (102)). That is, in each of the first and second heat exchange chambers (S11, S12), the adsorption block (301, 302) has an adsorption heat exchanger (101, 102) when the adsorption heat exchanger (101, 102) is an evaporator. When the adsorption heat exchanger (101, 102) is a condenser, it is located upstream of the adsorption heat exchanger (101, 102).
  • the dehumidifying operation of the dehumidifying device (10) of the second embodiment will be described with reference to FIG. Similar to the dehumidifying device (10) of the first embodiment, the dehumidifying device (10) of the second embodiment alternately repeats the first and second dehumidifying operations at predetermined time intervals (for example, every 10 minutes).
  • First dehumidifying operation In the first dehumidifying operation, the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the first connection state (the state shown by the solid line in FIG. 7). .
  • the refrigerant circuit (100) performs a first refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as an evaporator and the second adsorption heat exchanger (102) serves as a condenser. Further, the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the first passage state (the state indicated by the solid line in FIG. 7).
  • the air taken into the supply passage (P1) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11), and then supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption heat exchanger (101) functioning as an evaporator.
  • the air passing through the first adsorption heat exchanger (101) functioning as an evaporator is deprived of moisture by the adsorbent of the first adsorption heat exchanger (101), and the humidity decreases. It is cooled by the endothermic action of the refrigerant flowing through the one adsorption heat exchanger (101), and the temperature also decreases.
  • the air dehumidified and cooled by the first adsorption heat exchanger (101) passes through the first adsorption block (301). At this time, moisture in the air is adsorbed on the adsorbent of the first adsorption block (301). Thereby, the air dehumidified by the first adsorption heat exchanger (101) is further dehumidified by the first adsorption block (301).
  • the air dehumidified after passing through the first adsorption heat exchanger (101) and the first adsorption block (301) is supplied to the indoor space (S1) as supply air (SA).
  • the air (in this example, room air (RA)) taken into the regeneration passage (P2) is heated by the heater (21) and then supplied to the second heat exchange chamber (S12).
  • the air supplied to the second heat exchange chamber (S12) passes through the second adsorption block (302).
  • the moisture of the adsorbent of the second adsorption block (302) is released to the air passing through the second adsorption block (302).
  • the adsorbent of the second adsorption block (302) is regenerated.
  • the air humidified by the second adsorption block (302) passes through the second adsorption heat exchanger (102) functioning as a condenser.
  • the air passing through the second adsorption heat exchanger (102) functioning as a condenser is given moisture from the adsorbent of the second adsorption heat exchanger (102) to increase the humidity and the second adsorption heat. It is heated by the heat radiation action of the refrigerant flowing through the exchanger (102), and the temperature also rises. Thereby, the adsorbent of the second adsorption heat exchanger (102) is regenerated.
  • the air that has passed through the second adsorption heat exchanger (102) and the second adsorption block (302) is exhausted to the outdoor space as exhaust air (EA).
  • the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the second connection state (the state indicated by the broken line in FIG. 7).
  • the refrigerant circuit (100) performs a second refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as a condenser and the second adsorption heat exchanger (102) serves as an evaporator.
  • the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the second passage state (the state indicated by the broken line in FIG. 7).
  • the air taken into the supply passage (P1) (in this example, outdoor air (OA)) is cooled and dehumidified by the cooler (11), and then supplied to the second heat exchange chamber (S12).
  • the air supplied to the second heat exchange chamber (S12) passes through the second adsorption heat exchanger (102) functioning as an evaporator.
  • the air passing through the second adsorption heat exchanger (102) functioning as an evaporator is deprived of moisture by the adsorbent of the second adsorption heat exchanger (102), and the humidity decreases.
  • the refrigerant is cooled by the endothermic action of the refrigerant flowing through the two-adsorption heat exchanger (102), and the temperature also decreases.
  • the air dehumidified and cooled by the second adsorption heat exchanger (102) passes through the second adsorption block (302). At this time, moisture in the air is adsorbed to the adsorbent of the second adsorption block (302). Thereby, the air dehumidified by the second adsorption heat exchanger (102) is further dehumidified by the second adsorption block (302).
  • the air dehumidified after passing through the second adsorption heat exchanger (102) and the second adsorption block (302) is supplied to the indoor space (S1) as supply air (SA).
  • the air taken into the regeneration passage (P2) (in this example, room air (RA)) is heated by the heater (21) and then supplied to the first heat exchange chamber (S11).
  • the air supplied to the first heat exchange chamber (S11) passes through the first adsorption block (301).
  • the moisture of the adsorbent of the first adsorption block (301) is released to the air passing through the first adsorption block (301).
  • the adsorbent of the first adsorption block (301) is regenerated.
  • the air humidified by the first adsorption block (301) passes through the first adsorption heat exchanger (101) functioning as a condenser.
  • the air passing through the first adsorption heat exchanger (101) functioning as a condenser is given moisture from the adsorbent of the first adsorption heat exchanger (101), and the humidity rises.
  • the adsorbent of the first adsorption heat exchanger (101) is regenerated.
  • the air that has passed through the first adsorption heat exchanger (101) and the first adsorption block (301) is exhausted to the outdoor space as exhaust air (EA).
  • FIG. 8 ⁇ Structure of dehumidifier>
  • a center figure is a top view of a dehumidification apparatus (10)
  • an upper figure is a rear view of a dehumidification apparatus (10)
  • a lower figure is a front view of a dehumidification apparatus (10).
  • the dehumidifier (10) includes a casing (41) that houses the components of the refrigerant circuit (100).
  • the casing (41) is formed in a substantially flat and relatively low rectangular parallelepiped shape, and has a front panel (42), a rear panel (43), a left side panel (44), and a right side panel (45). ing.
  • the longitudinal direction of the casing (41) is the left-right direction.
  • the casing (41) has an adsorption side suction port (51), a regeneration side suction port (52), an air supply port (53), and an exhaust port (54).
  • the suction side suction port (51) is provided at a position on the right side of the back panel (43), and the reproduction side suction port (52) is provided at a position on the left side of the back panel (43).
  • the air supply port (53) is provided on the left side of the front panel (42), and the exhaust port (54) is provided on the right side of the front panel (42).
  • a first partition plate (46), a second partition plate (47), and a central partition plate (48) are provided in the internal space of the casing (41). These partition plates (46, 47, 48) are installed upright on the bottom plate of the casing (41) and partition the internal space of the casing (41) from the bottom plate of the casing (41) to the top plate. Yes.
  • the first and second partition plates (46, 47) are arranged at a predetermined interval in the left-right direction of the casing (41) in a posture parallel to the left side panel (44) and the right side panel (45). Yes.
  • the first partition plate (46) is disposed closer to the left side panel (44), and the second partition plate (47) is disposed closer to the right side panel (45).
  • the space on the left side of the first partition plate (46) becomes the left space (S31), the space between the first partition plate (46) and the second partition plate (47) becomes the central space (S32), and the second space
  • the space on the right side of the partition plate (47) is the right space (S33).
  • the arrangement of the central partition plate (48) will be described later.
  • the left space (S31) is partitioned into a left side panel (44) side portion and a first partition (46) side portion.
  • the space on the left side of the casing (41) in the left space (S31) is partitioned into two front and rear spaces, the front space forms the supply fan chamber (S25), and the back space is the regeneration side It constitutes the suction chamber (S28).
  • the space on the first partition (46) side in the left space (S31) is partitioned into two upper and lower spaces, and the upper space constitutes the second suction side internal passage (S23), and the lower space. Respectively constitutes the first regeneration-side internal passage (S22).
  • the air supply fan chamber (S25) communicates with the indoor space (S1) via a duct (corresponding to the second air supply passage portion (P12) in FIG. 7) connected to the air supply port (53).
  • An air supply fan (61) is housed in the air supply fan chamber (S25).
  • the air outlet of the air supply fan (61) is connected to the air supply port (53).
  • the compressor fan (103) and the four-way switching valve (105) (not shown) of the refrigerant circuit (100) are accommodated in the air supply fan chamber (S25).
  • the regeneration side suction chamber (S28) communicates with the indoor space (S1) via a duct (corresponding to the first regeneration passage portion (P21) in FIG. 7) connected to the regeneration side suction port (52). Yes.
  • the second adsorption side internal passage (S23) is separated from the regeneration side suction chamber (S28) by a partition plate extending in the front-rear direction, and communicates with the air supply fan chamber (S25).
  • the first regeneration side internal passage (S22) communicates with the regeneration side suction chamber (S28).
  • the right space (S33) is divided into a right side portion of the casing (41) and a second partition plate (47) side portion.
  • the front space constitutes the exhaust fan chamber (S26).
  • the inner space is partitioned vertically, the lower space constitutes the suction side suction chamber (S27) partitioned from the exhaust fan chamber (S26), and the upper space is the exhaust fan chamber (S26).
  • the space on the second partition (47) side in the right space (S33) is partitioned into two upper and lower spaces, and the upper space constitutes the second reproduction-side internal passage (S24), and the lower space Constitutes the first suction side internal passage (S21).
  • the exhaust fan chamber (S26) communicates with the outdoor space via a duct (corresponding to the second regeneration passage portion (P22) in FIG. 7) connected to the exhaust port (54).
  • An exhaust fan (62) is housed in the exhaust fan chamber (S26).
  • the outlet of the exhaust fan (62) is connected to the exhaust outlet (54).
  • the suction side suction chamber (S27) communicates with the outdoor space via a duct (corresponding to the first air supply passage portion (P11) in FIG. 7) connected to the suction side suction port (51).
  • the second regeneration side internal passage (S24) communicates with the exhaust fan chamber (S26).
  • the first suction side internal passage (S21) communicates with the suction side suction chamber (S27).
  • the central space (S32) is divided forward and backward by a central partition plate (48), and the space behind the central partition plate (48) constitutes the first heat exchange chamber (S11), and the central partition plate (48 ) In front of the second heat exchange chamber (S12).
  • a first adsorption heat exchanger (101) is accommodated in the first heat exchange chamber (S11), and a second adsorption heat exchanger (102) is accommodated in the second heat exchange chamber (S12).
  • the second heat exchange chamber (S12) accommodates an expansion valve (104) (not shown) of the refrigerant circuit (100).
  • Each of the first and second adsorption heat exchangers (101, 102) is formed into a rectangular thick plate shape or flat rectangular parallelepiped shape as a whole, and two main surfaces (wide side surfaces) facing each other are surfaces through which air passes. It has become.
  • the 1st adsorption heat exchanger (101) stood up in the 1st heat exchange room (S11) with the posture where the two principal surfaces became parallel to the 1st and 2nd partition plates (46, 47). It is installed in a state.
  • the second adsorptive heat exchanger (102) has a configuration in which the two main surfaces thereof are parallel to the first and second partition plates (46, 47) and in the second heat exchange chamber (S12). It is installed in a standing state.
  • Each of the first and second adsorption blocks (301, 302) is formed in a rectangular thick plate shape or flat rectangular parallelepiped shape as a whole, and two main surfaces (wide side surfaces) facing each other serve as surfaces through which air passes. ing.
  • each of the first and second adsorption blocks (301, 302) is a honeycomb-like structure having a large number of holes penetrating from one main surface to the other main surface.
  • the first adsorption block (301) stands up in the first heat exchange chamber (S11) with its two main surfaces parallel to the first and second partition plates (46, 47). is set up.
  • the second adsorption block (302) stands up in the second heat exchange chamber (S12) with its two main surfaces parallel to the first and second partition plates (46, 47). Installed.
  • the first adsorption block (301) is disposed between the first adsorption heat exchanger (101) and the first partition plate (46) in the first heat exchange chamber (S11), and the second The adsorption block (302) is disposed between the second adsorption heat exchanger (102) and the first partition plate (46) in the second heat exchange chamber (S12).
  • the first adsorption block (301) is spaced apart from the first adsorption heat exchanger (101) in the left-right direction, and the second adsorption block (302) is arranged in the second adsorption heat exchanger (101) in the left-right direction. 102) and spaced apart.
  • the first partition plate (46) is provided with first to fourth dampers (D1 to D4), and the second partition plate (47) is provided with fifth to eighth dampers (D5 to D8). Yes.
  • Each of the first to eighth dampers (D1 to D8) is configured to be switchable between an open state and a closed state in response to control by the controller (20).
  • These first to eighth dampers (D1 to D8) constitute a switching mechanism (200).
  • the first damper (D1) is attached to the front side of the central partition plate (48) in the upper portion of the first partition plate (46) (the portion facing the second suction side internal passage (S23)).
  • the damper (D2) is attached to the back side of the central partition plate (48) in the upper part of the first partition plate (46).
  • the third damper (D3) is attached to the front side of the central partition plate (48) in the lower portion of the first partition plate (46) (the portion facing the first regeneration-side internal passage (S22)).
  • the 4 damper (D4) is attached to the back side of the central partition plate (48) in the lower portion of the first partition plate (46).
  • the first damper (D1) When the first damper (D1) is opened, the second adsorption side internal passage (S23) and the second heat exchange chamber (S12) communicate with each other.
  • the second damper (D2) When the second damper (D2) is opened, the second adsorption side internal passage (S23) and the first heat exchange chamber (S11) communicate with each other.
  • the third damper (D3) When the third damper (D3) is opened, the first regeneration side internal passage (S22) and the second heat exchange chamber (S12) communicate with each other.
  • the fourth damper (D4) When the fourth damper (D4) is opened, the first regeneration side internal passage (S22) and the first heat exchange chamber (S11) communicate with each other.
  • the fifth damper (D5) is attached to the front side of the central partition plate (48) in the upper portion of the second partition plate (47) (the portion facing the second regeneration-side internal passage (S24)).
  • the damper (D6) is attached to the back side of the central partition plate (48) in the upper part of the second partition plate (47).
  • the seventh damper (D7) is attached to the front side of the central partition plate (48) in the lower portion of the second partition plate (47) (the portion facing the first suction side internal passage (S21)).
  • the 8 damper (D8) is attached to the back side of the central partition plate (48) in the lower portion of the second partition plate (47).
  • the first adsorption heat exchanger (101) serves as an evaporator
  • the second adsorption heat exchanger (102) serves as a condenser.
  • the second, third, fifth, and eighth dampers (D2, D3, D5, and D8) are opened, and the first, fourth, sixth, and seventh dampers (D1, D4) are opened. , D6, D7) are closed.
  • connection state of the first and second heat exchange chambers (S11, S12) is set to the first passage state (the state indicated by the solid line in FIG. 7), and the first heat exchange chamber (S11) is set to the air supply passage. (P1) and the second heat exchange chamber (S12) is incorporated into the regeneration passage (P2).
  • OA outdoor air
  • the dehumidified air that has passed through the first adsorption heat exchanger (101) and the first adsorption block (301) passes through the second damper (D2) and flows into the second adsorption side internal passage (S23).
  • the air passes through the air fan chamber (S25) and the air supply port (53) and is supplied to the indoor space (S1) as supply air (SA).
  • RA room air
  • the first adsorption heat exchanger (101) serves as a condenser
  • the second adsorption heat exchanger (102) serves as an evaporator.
  • the first, fourth, sixth and seventh dampers (D1, D4, D6, D7) are opened
  • the second, third, fifth and eighth dampers (D2, D3) are opened.
  • D5, D8) are closed.
  • connection state of the first and second heat exchange chambers (S11, S12) is set to the second passage state (the state indicated by the broken line in FIG. 7), and the first heat exchange chamber (S11) is set to the regeneration passage ( P2) and the second heat exchange chamber (S12) is incorporated into the air supply passage (P1).
  • OA outdoor air
  • the air that has been dehumidified after passing through the second adsorption heat exchanger (102) and the second adsorption block (302) passes through the first damper (D1) and flows into the second adsorption side internal passage (S23).
  • the air passes through the air fan chamber (S25) and the air supply port (53) and is supplied to the indoor space (S1) as supply air (SA).
  • the air in this example, room air (RA) supplied to the first regeneration side internal passage (S22) via the regeneration side suction port (52) and the regeneration side suction chamber (S28) D4) is supplied to the first heat exchange chamber (S11).
  • RA room air
  • the first adsorption block (301) is located at a position where the air dehumidified by the first adsorption heat exchanger (101) passes.
  • the air dehumidified and cooled by the first adsorption heat exchanger (101) can be supplied to the first adsorption block (301).
  • moisture content to adsorption agent can be accelerated
  • the air dehumidified and cooled by the second adsorption heat exchanger (102) is transferred to the second adsorption block. Since it can be supplied to (302), the adsorption of moisture to the adsorbent can be promoted in the second adsorption block (302). That is, in each of the first and second heat exchange chambers (S11, S12), when the adsorption heat exchanger (101, 102) is an evaporator, the adsorption is performed at a position downstream of the adsorption heat exchanger (101, 102).
  • the air dehumidified and cooled by the adsorption heat exchanger (101,102) can be supplied to the adsorption block (301,302), so that the moisture to the adsorbent of the adsorption block (301,302) can be supplied. Adsorption can be promoted.
  • the amount of air dehumidified in the first and second heat exchange chambers (S11, S12) can be increased, and the adsorption of moisture to the adsorbent can be promoted in the adsorption block (301, 302). Therefore, the dehumidifying capacity of the dehumidifying device (10) can be improved.
  • the increase in power consumption of the dehumidifying device (10) is suppressed. can do.
  • the adsorption block (301, 302) is adsorbed when the adsorption heat exchanger (101, 102) is an evaporator.
  • the heater (21) is placed in the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as a condenser among the first and second heat exchange chambers (S1, S12).
  • the first adsorption block (301) is the first adsorption heat exchanger (S11) in the first heat exchange chamber (S11). 101), the air that has passed through the first adsorption heat exchanger (101) is supplied to the first adsorption block (301). In this case, the air that passes through the first adsorption heat exchanger (101) and is supplied to the first adsorption block (301) is not only heated but also humidified by the first adsorption heat exchanger (101). It will be. The same applies to the second adsorption block (302).
  • the first adsorption block (301) is the first adsorption heat exchanger (S11) in the first heat exchange chamber (S11). 101), the air heated by the heater (21) is supplied to the first adsorption block (301). In this case, the air that passes through the heater (21) and is supplied to the first adsorption block (301) is heated by the heater (21) but is not humidified. Therefore, the regeneration of the adsorbent in the first adsorption block (301) can be promoted more than in the first embodiment, and the adsorption capacity in the first adsorption block (301) can be further improved. The same applies to the second adsorption block (302).
  • the first adsorption block (301) at a distance from the first adsorption heat exchanger (101), it is possible to suppress temperature distribution deviation and air drift in the first adsorption block (301). .
  • the temperature distribution and air drift can be suppressed in the first and second adsorption blocks (301, 302), the decrease in adsorption capacity and regeneration capacity in the first and second adsorption blocks (301, 302) is suppressed. can do.
  • the dehumidification system (1) includes a pretreatment dehumidifier (30) in addition to the dehumidifier (10), controller (20), and heater (21) shown in FIG. It may be.
  • the humidity control space (S0) includes an indoor space (S1) and a chamber (S2) provided in the indoor space (S1).
  • the dehumidification system (1) is provided with a pretreatment passage (P3) and a posttreatment passage (P4).
  • the air (in this example, outdoor air (OA)) dehumidified by the pretreatment dehumidifier (30) is supplied to the indoor space (S1) as supply air (SA0)
  • Air dehumidified by the dehumidifier (10) (in this example, room air (RA)) is supplied to the chamber (S2) as supply air (SA).
  • the controller (20) controls the dehumidifier (10) and the pretreatment dehumidifier (30) based on the detection values of the various sensors.
  • the pretreatment passage (P3) is configured to take outdoor air (OA) from the outdoor space and supply supply air (SA0) to the indoor space (S1).
  • the post-processing passage (P4) is configured to take air from the outflow end of the regeneration passage (P2) and discharge the exhaust air (EA) to the outdoor space.
  • the supply passage (P1) is configured to take in indoor air (RA) from the indoor space (S1) and supply supply air (SA) to the chamber (S2).
  • the inflow end of the first supply passage portion (P11) is connected to the indoor space (S1)
  • the outflow end of the second supply passage portion (P12) is connected to the chamber (S2).
  • the regeneration passage (P2) is configured to take indoor air (RA) from the indoor space (S1) and discharge processed air to the post-treatment passage (P4).
  • the inflow end of the first regeneration passage portion (P21) is connected to the intermediate portion of the first supply air passage portion (P11), and the outflow end of the second regeneration passage portion (P22) is the first rear passage. It is connected to the inflow end of the processing passage (P41).
  • the pretreatment dehumidifier (30) has the same configuration as the dehumidifier (10).
  • the structure of the pretreatment dehumidifier (30) is the same as the structure of the dehumidifier (10) shown in FIG.
  • the refrigerant circuit (100) of the pretreatment dehumidifying device (30) responds to the control by the controller (20) in response to the first adsorption heat exchanger (101).
  • the air is dehumidified, and the first adsorption heat exchanger (101) serves as a condenser to alternately perform the second refrigeration cycle operation for regenerating the adsorbent.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) is responsive to the control by the controller (20) to the first and second heat exchange chambers (S11, S12) of the pretreatment dehumidifier (30).
  • the connection state between the pre-processing passage (P3) and the post-processing passage (P4) includes a third passage state (state shown by a solid line in FIG. 10) and a fourth passage state (state shown by a broken line in FIG. 10). It is configured to be configurable.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) is connected to the first and second heat exchange chambers (S11, S12) when the four-way switching valve (105) is in the first connection state. Is set to the third passage state, and when the four-way switching valve (105) is in the second connection state, the connection state of the first and second heat exchange chambers (S11, S12) is set to the third passage state. That is, the switching mechanism (200) of the pretreatment dehumidifier (30) is the same as the switching mechanism (200) of the dehumidifier (10) in the first and second heat exchange chambers (S11, S12).
  • the air that has passed through the heat exchange chambers (S11, S12) in which the adsorption heat exchangers (101, 102) are installed is supplied to the humidity control space (S0), and the adsorption heat exchanger (condenser) Air for regenerating the adsorbent in the heat exchange chambers (S12, S11) provided with 102, 101) (in this example, the first and second heat exchange chambers (S11, S12) of the dehumidifier (10) are condensed).
  • the air flow is switched so that the air passing through the heat exchange chambers (S11, S12) provided with the adsorption heat exchangers (101, 102) serving as a container flows.
  • the connection state of the first and second heat exchange chambers (S11, S12) is the third passage state (that is, the first heat exchange chamber (S11). ) Is incorporated as part of the pretreatment passage (P3)), the flow direction of the air passing through the first adsorption heat exchanger (101) is the first and second heat exchange chambers (S11, S12).
  • the connection state is the fourth passage state (that is, when the first heat exchange chamber (S11) is incorporated as a part of the post-treatment passage (P4))
  • the first adsorption heat exchanger (101) is installed. It is the direction opposite to the flow direction of the passing air.
  • the switching mechanism (200) of the pretreatment dehumidifier (30) passes through each of the first and second adsorption heat exchangers (101, 102), similarly to the switching mechanism (200) of the dehumidifier (10).
  • the air flow direction is opposite between when the adsorption heat exchanger (101,102) is an evaporator and when the adsorption heat exchanger (101,102) is a condenser. Switch the flow.
  • the pretreatment dehumidifying device (30) of the third modification of the first embodiment performs the third and fourth dehumidifying operations at predetermined time intervals ( For example, it is repeated alternately at intervals of 10 minutes.
  • the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the first connection state (the state shown by the solid line in FIG. 10).
  • the refrigerant circuit (100) performs a first refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as an evaporator and the second adsorption heat exchanger (102) serves as a condenser.
  • the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the third passage state (the state shown by the solid line in FIG. 10).
  • ⁇ 4th dehumidifying action In the fourth dehumidifying operation, the compressor (103) is driven, the opening degree of the expansion valve (104) is adjusted, and the four-way switching valve (105) is in the second connection state (the state indicated by the broken line in FIG. 10). .
  • the refrigerant circuit (100) performs a second refrigeration cycle operation in which the first adsorption heat exchanger (101) serves as a condenser and the second adsorption heat exchanger (102) serves as an evaporator. Further, the switching mechanism (200) sets the connection state of the first and second heat exchange chambers (S11, S12) to the fourth passage state (the state indicated by the broken line in FIG. 10).
  • the air to be supplied to the indoor space (S1) (in this example, the outdoor air (OA)) is dehumidified by the pretreatment dehumidifier (30) and supplied to the indoor space (S1).
  • the indoor air (RA) supplied from the indoor space (S1) is dehumidified by the dehumidifier (10) and supplied to the chamber (S2) as the supply air (SA).
  • the dew point temperature of the air can be made lower than the dew point temperature of the air in the indoor space (S1).
  • the dehumidification system (1) can be operated more than when the entire indoor space (S1) is set to a low dew point. The power consumption required can be reduced.
  • FIG. 11 shows a configuration example of the dehumidification system (1) according to the third embodiment.
  • This dehumidification system (1) includes the pretreatment dehumidifier (30) shown in FIG. 10 instead of the pretreatment dehumidifier (30) shown in FIG.
  • Other configurations are the same as those in FIG. Even when configured in this manner, the same effects as those of Modification 3 (FIG. 6) of Embodiment 1 and Modification (FIG. 10) of Embodiment 2 can be obtained.
  • FIG. 12 shows a configuration example of the dehumidification system (1) according to the fourth embodiment.
  • the dehumidifying system (1) includes a heater (21), an adsorption rotor (70), and an auxiliary cooler (80) in addition to the dehumidifying device (10) and the controller (20) shown in FIG. .
  • the dehumidification system (1) is provided with a rotor air supply passage (P71), a rotor regeneration passage (P72), a purge passage (P73), and a cooling air passage (P80).
  • Air to be supplied to the humidity control space (S0) (in this example, air to be supplied to the indoor space (S1)) flows through the rotor air supply passage (P71).
  • the rotor air supply passage (P71) is configured to take in air from the outflow end of the air supply passage (P1) and supply the supply air (SA) to the indoor space (S1).
  • the inflow end of the rotor air supply passage (P71) is connected to the outflow end of the air supply passage (P1), and the outflow end is connected to the indoor space (S1).
  • Air for regenerating the adsorbent flows through the rotor regeneration passage (P72).
  • the rotor regeneration passage (P72) is configured to take air from the outflow end of the purge passage (P73) and supply regeneration air (air for regenerating the adsorbent) to the regeneration passage (P2). ing.
  • the rotor regeneration passage (P72) has an inflow end connected to the outflow end of the purge passage (P73), and an outflow end connected to the inflow end of the regeneration passage (P2).
  • ⁇ Purge passage> In the purge passage (P72), air to be supplied to the rotor regeneration passage (P72) (in this example, air supplied from the air supply passage (P1)) flows.
  • the purge passage (P73) is configured to take in air from the outflow end of the supply passage (P1) and supply the regeneration air to the rotor regeneration passage (P72).
  • the purge passage (P73) has an inflow end connected to the outflow end of the air supply passage (P1), and an outflow end connected to the inflow end of the rotor regeneration passage (P72).
  • the cooled and dehumidified air flows through the cooling air passage (P80).
  • the cooling air passage (P80) takes in the indoor air (RA) from the indoor space (S1) and passes the air into the intermediate portion of the air supply passage (P1) (specifically, the adsorption heat acting as an evaporator). It is configured to supply to the heat exchange chamber (S11, S12) in which the exchanger (101, 102) is provided.
  • the cooling air passage (P80) has an inflow end connected to the indoor space (S1) and an outflow end connected to a midway portion of the air supply passage (P1).
  • the heater (21) is provided in the rotor regeneration passage (P72) and heats air for regenerating the adsorbent (in this example, air supplied from the purge passage (P73) to the rotor regeneration passage (P72)). Is configured to do.
  • the heating temperature in the heater (21) is set to a temperature (for example, 60 ° C.) lower than the upper limit value of the condensation temperature of the adsorption heat exchanger (101, 102).
  • the adsorption rotor (70) is configured by carrying an adsorbent on the surface of a disk-shaped porous base material, and includes a rotor supply passage (P71), a rotor regeneration passage (P72), a purge passage (P73), It is arranged across.
  • the adsorption rotor (70) is driven by a drive mechanism (not shown), and rotates about the axis between the rotor supply passage (P71), the rotor regeneration passage (P72), and the purge passage (P73). It is configured as follows.
  • the adsorption rotor (70) includes an adsorption portion (71) disposed in the rotor air supply passage (P71), a regeneration portion (72) disposed in the rotor regeneration passage (P72), and a purge passage ( P73) and a purge section (73).
  • the adsorbent carried on the adsorption rotor (70) sequentially moves through the adsorption unit (71), the regeneration unit (72), and the purge unit (73) as the adsorption rotor (70) rotates.
  • the portion located in the adsorption portion (71) moves to the regeneration portion (72), the portion located in the regeneration portion (72) moves to the purge portion (73), and the purge portion ( Rotate so that the part located at 73) moves to the suction part (71).
  • the adsorbing part (71) is an adsorbing air that flows through the rotor air supply passage (P71) (in this example, the first and second heat exchange chambers (S11, S12) of the dehumidifying device (10) are evaporators).
  • the air that has passed through the heat exchange chamber (S11, S12) where the heat exchanger (101, 102) is provided and the air that has passed through the cooling air passage (P80) are brought into contact with the adsorbent to dehumidify the air. It is a part to do.
  • the air that has been dehumidified after passing through the adsorption section (71) is supplied to the indoor space (S1) as supply air (SA).
  • the regenerator (72) is arranged at a position downstream of the heater (21) in the rotor regeneration passage (P72) and flows through the rotor regeneration passage (P72) (in this example, passes through the heater (21)). This is a part for regenerating the adsorbent by bringing it into contact with the adsorbent.
  • the air that has passed through the regeneration unit (72) is supplied to the regeneration passage (P2).
  • the purge unit (73) supplies the regeneration unit (72) using the exhaust heat of the regeneration unit (72) (specifically, exhaust heat not used for regeneration of the adsorbent in the regeneration unit (72)). It is a part for preheating the air to be used. More specifically, in the purge section (73), the air flowing through the purge passage (P73) comes into contact with the adsorbent and is dehumidified. Further, the portion located in the regeneration unit (72) (that is, the portion heated by the air that has passed through the heater (21)) moves to the purge unit (73) as the adsorption rotor (70) rotates.
  • the air flowing through the purge passage (P73) is preheated by being given heat from the purge section (73) (that is, exhaust heat of the regeneration section (72)).
  • the portion located in the purge section (73) is cooled by applying heat to the air passing through the purge passage (P73), and then moved to the adsorption section (71) as the adsorption rotor (70) rotates. To do.
  • the auxiliary cooler (80) is provided in the cooling air passage (P80), and cools the air flowing through the cooling air passage (P80) (in this example, room air (RA)).
  • the auxiliary cooler (80) may be configured by a heat exchanger (specifically, a fin-and-tube heat exchanger) that functions as an evaporator of a refrigerant circuit (not shown).
  • the air cooled in the cooling air passage (P80) is the air flowing through the air supply passage (P1) (in this example, the evaporator of the first and second heat exchange chambers (S11, S12) of the dehumidifying device (10)). And the air that has passed through the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102).
  • the air that has passed through the air supply passage (P1) passes through the rotor air supply passage (P71) and is supplied to the indoor space (S1). That is, it passes through the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator among the first and second heat exchange chambers (S11, S12) of the dehumidifier (10).
  • the air that has passed through the suction rotor (70) of the suction rotor (70) is supplied to the indoor space (S1).
  • the air that has passed through the rotor regeneration passage (P72) passes through the regeneration passage (P2) and is discharged to the outdoor space.
  • the switching mechanism (200) of the dehumidifier (10) includes a heat exchange chamber provided with an adsorption heat exchanger (102, 101) serving as a condenser among the first and second heat exchange chambers (S11, S12).
  • the air flow is switched so that the air that has passed through the heater (21) and the regenerating unit (72) of the adsorption rotor (70) in turn flows.
  • the air to be supplied to the humidity control space (S0) (in this example, the air to be supplied to the indoor space (S1)) is supplied by the adsorption heat exchanger (101, 102) serving as an evaporator. After being dehumidified in the provided heat exchange chambers (S11, S12), it is further dehumidified in the adsorption part (71) of the adsorption rotor (70).
  • the dehumidification capability of the dehumidification system (1) can be improved by adding the adsorption rotor (70).
  • the air heated by the heater (21) passes through the regeneration unit (72) of the adsorption rotor (70), and then is provided with an adsorption heat exchanger (102, 101) serving as a condenser. Pass through (S12, S11). That is, the air that has passed through the regeneration unit (72) of the adsorption rotor (70) can be used for regeneration of the adsorbent of the adsorption heat exchanger (102, 101) and the adsorption block (302, 301). Thereby, the air heated by the heater (21) can be used effectively.
  • the adsorption heat that is the evaporator using the air cooled in the cooling air passage (P80) can be reduced. That is, it is possible to reduce the temperature of the air that has increased in temperature due to the residual heat remaining in the adsorption block (101, 102) during regeneration or the adsorption heat in the adsorption block (101, 102).
  • a part of the air supplied from the supply passage (P1) passes through the purge passage (P73), the rotor regeneration passage (P72), and the regeneration passage (P2) in this order, so that the adsorption heat acting as an evaporator Part of the air (that is, the air dehumidified in the dehumidifier (10)) that has passed through the heat exchange chambers (S11, S12) in which the exchangers (101, 102) are provided, is adsorbed and condensed in the adsorption rotor (70). It can be used for the regeneration of the adsorbent of the adsorption heat exchanger (102, 101) serving as a vessel. Thereby, regeneration of adsorbent can be promoted.
  • the first adsorption block (301) is spaced from the first adsorption heat exchanger (101), and the second adsorption block (302) is spaced from the second adsorption heat exchanger (102).
  • the first adsorption block (301) may be arranged in contact with the first adsorption heat exchanger (101), and the second adsorption block (302) may be disposed.
  • Heat conduction with the adsorption block (302) can be promoted.
  • the first heat exchange chamber (S11) is incorporated in the air supply passage (P1)
  • the first adsorption block (301) is removed by the heat absorption action of the refrigerant flowing through the first adsorption heat exchanger (101).
  • the first adsorption block (101) can be cooled by the heat radiation action of the refrigerant flowing through the first adsorption heat exchanger (101).
  • 301) can be heated.
  • the first and second adsorption blocks (301, 302) it is possible to promote the adsorption of moisture to the adsorbent and the regeneration of the adsorbent.
  • one dehumidifying unit may be configured by connecting a plurality of dehumidifying devices (10) in parallel with each other.
  • the dehumidifiers (10) shown in FIG. 2 (or FIG. 7) are stacked in a plurality of stages and opened in each dehumidifier (10) (specifically, suction side suction port (51), regeneration side suction)
  • One dehumidifying unit may be configured by commonly connecting the mouth (52), the air inlet (53), and the air outlet (54) for each type.
  • the dehumidifier (10) is dehumidified by increasing the size of the first and second adsorption heat exchangers (101,102) without adding the first and second adsorption blocks (301,302) to the dehumidifier (10). It is possible to improve ability. That is, by increasing the size of the adsorption heat exchanger, the heat absorption effect of the refrigerant can be increased in the adsorption heat exchanger functioning as an evaporator. Thereby, while the temperature of the air in an adsorption heat exchanger can be reduced, the temperature rise of the air by the adsorption heat of adsorption agent can be controlled.
  • the adsorption of moisture from the air to the adsorbent can be promoted by the endothermic action of the refrigerant.
  • the air temperature and the amount of moisture in the air decrease from the upstream side toward the downstream side. That is, inside the adsorption heat exchanger, air dehumidified and cooled on the upstream side is supplied to the downstream side. Therefore, on the downstream side in the adsorption heat exchanger, even if the temperature of the air decreases due to the endothermic action of the refrigerant and the amount of saturated water vapor in the air decreases, the amount of moisture in the air decreases. It is difficult to promote the adsorption of moisture to the adsorbent. Further, the amount of heat of adsorption in the adsorbent decreases as the amount of moisture in the air decreases. Therefore, on the downstream side of the adsorption heat exchanger, the adsorbent is excessively cooled by the endothermic action of the refrigerant.
  • the adsorption block at the position downstream of the adsorption heat exchanger functioning as an evaporator (the position where the air dehumidified and cooled by the adsorption heat exchanger passes), the adsorption heat exchanger Since the contact area between the air and the adsorbent can be increased on the downstream side, the dehumidifying ability of the dehumidifying device (10) can be effectively improved as compared with the case of increasing the size of the adsorption heat exchanger.
  • the adsorbent regeneration operation release of moisture from the adsorbent into the air
  • the adsorbent adsorption operation adsorption of moisture from the air into the adsorbent.
  • the air volume of the air passing through the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator among the first and second heat exchange chambers (S11, S12) is:
  • the amount of air passing through the heat exchange chamber (S12, S11) provided with the adsorption heat exchanger (102, 101) serving as a condenser may be larger or the same.
  • the temperature of the air supplied to the regeneration passage (P2) (that is, the air supplied to the heat exchange chamber (S12, S11) provided with the adsorption heat exchanger (102, 101) serving as a condenser) is Higher than the temperature of the air supplied to the supply passage (P1) (that is, the air supplied to the heat exchange chamber (S11, S12) provided with the adsorption heat exchanger (101, 102) serving as an evaporator)
  • a predetermined temperature difference specifically, a temperature difference at which the adsorbent can be regenerated
  • the above dehumidifying apparatus is useful as a dehumidifying apparatus for dehumidifying a humidity control space such as a dry clean room.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Central Air Conditioning (AREA)
  • Air Conditioning Control Device (AREA)
  • Drying Of Gases (AREA)

Abstract

Selon l'invention, des premier et second échangeurs de chaleur par adsorption (101, 102) sont respectivement agencés dans des première et seconde chambres d'échange de chaleur (S11, S12) et sont chacun commutés afin de servir d'évaporateur et de condenseur. Un premier bloc d'adsorption (301) est agencé à l'intérieur de la première chambre d'échange de chaleur (S11) en aval du premier échangeur de chaleur par adsorption (101) lorsque le premier échangeur de chaleur par adsorption (101) a été commuté pour servir d'évaporateur et le second bloc d'adsorption (302) est agencé à l'intérieur de la seconde chambre d'échange de chaleur (S12) en aval du second échangeur de chaleur par adsorption (102) lorsque le second échangeur de chaleur par adsorption (102) a été commuté afin de servir d'évaporateur. Du fait de la configuration ci-dessus, un dispositif de déshumidification peut atteindre une haute performance de déshumidification alors qu'une augmentation de la consommation électrique est réduite au minimum.
PCT/JP2014/003387 2013-06-28 2014-06-24 Dispositif de déshumidification et système de déshumidification WO2014208083A1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
BR112015032117A BR112015032117A2 (pt) 2013-06-28 2014-06-24 dispositivo de desumidificação, e sistema de desumidificação
CN201480036707.6A CN105358915B (zh) 2013-06-28 2014-06-24 除湿装置和除湿系统
KR1020167002316A KR101630143B1 (ko) 2013-06-28 2014-06-24 제습장치 및 제습 시스템
US14/897,098 US20160146479A1 (en) 2013-06-28 2014-06-24 Dehumidification device and dehumidification system
EP14818067.2A EP3015778A4 (fr) 2013-06-28 2014-06-24 Dispositif de déshumidification et système de déshumidification

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2013-137166 2013-06-28
JP2013137166 2013-06-28

Publications (1)

Publication Number Publication Date
WO2014208083A1 true WO2014208083A1 (fr) 2014-12-31

Family

ID=52141442

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2014/003387 WO2014208083A1 (fr) 2013-06-28 2014-06-24 Dispositif de déshumidification et système de déshumidification

Country Status (7)

Country Link
US (1) US20160146479A1 (fr)
EP (1) EP3015778A4 (fr)
JP (1) JP5885781B2 (fr)
KR (1) KR101630143B1 (fr)
CN (1) CN105358915B (fr)
BR (1) BR112015032117A2 (fr)
WO (1) WO2014208083A1 (fr)

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101667979B1 (ko) * 2015-06-19 2016-10-21 한국생산기술연구원 제습 및 가습 기능을 갖는 공기조화기와 이를 이용한 제습냉방 및 가습난방 방법
US11859835B2 (en) * 2016-06-27 2024-01-02 Daikin Industries, Ltd. Humidity control apparatus with dual heat exchangers and bypass passage
KR101898592B1 (ko) * 2016-11-07 2018-09-13 엘지전자 주식회사 천장형 공기조화기장치
KR101973648B1 (ko) * 2017-08-07 2019-04-29 엘지전자 주식회사 환기장치의 제어방법
BE1027506B1 (nl) * 2019-08-16 2021-03-15 Atlas Copco Airpower Nv Droger voor samengeperst gas, compressorinstallatie voorzien van droger en werkwijze voor het drogen van samengeperst gas
WO2021005771A1 (fr) * 2019-07-10 2021-01-14 三菱電機株式会社 Dispositif de traitement d'air
CN112361639B (zh) * 2019-07-26 2022-04-19 青岛海尔空调器有限总公司 空调
BR112021025733A2 (pt) * 2019-08-16 2022-04-19 Atlas Copco Airpower Nv Secador para gás comprimido, instalação de compres-sor provida com um secador, e método para secar gás comprimido
CN110925902B (zh) * 2019-11-22 2021-02-19 珠海格力电器股份有限公司 低露点复合除湿机
KR20210112155A (ko) * 2020-03-04 2021-09-14 엘지전자 주식회사 공기조화기
WO2022038721A1 (fr) * 2020-08-19 2022-02-24 三菱電機株式会社 Dispositif de traitement d'air
CN112327975B (zh) * 2020-11-03 2022-06-17 张勇 一种高效多级烘干系统的控制方法
US20220205654A1 (en) * 2020-12-28 2022-06-30 Guangdong Broan IAQ Systems Co., Ltd. Dehumidification system

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4398927A (en) * 1980-07-30 1983-08-16 Exxon Research And Engineering Co. Cyclic adsorption process
JPH07275642A (ja) * 1994-04-06 1995-10-24 Matsushita Electric Ind Co Ltd 除湿装置
US5826434A (en) * 1995-11-09 1998-10-27 Novelaire Technologies, L.L.C. High efficiency outdoor air conditioning system
JP2000146220A (ja) * 1998-11-02 2000-05-26 Nissan Motor Co Ltd 空気調和手段及び空気調和装置
JP2006264490A (ja) * 2005-03-23 2006-10-05 Mazda Motor Corp 車両用空調装置
JP2006349294A (ja) 2005-06-17 2006-12-28 Daikin Ind Ltd 調湿装置
JP2008247305A (ja) * 2007-03-30 2008-10-16 Mitsubishi Chemicals Corp 車両用除加湿装置
JP2010190495A (ja) * 2009-02-18 2010-09-02 Daikin Ind Ltd 調湿装置
JP2013092290A (ja) * 2011-10-25 2013-05-16 Daikin Industries Ltd 除湿システム

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003097825A (ja) * 2001-07-18 2003-04-03 Daikin Ind Ltd 空気調和装置
JP3695417B2 (ja) * 2002-02-04 2005-09-14 ダイキン工業株式会社 調湿装置
JP3624910B2 (ja) * 2003-05-27 2005-03-02 ダイキン工業株式会社 調湿装置
AU2005227438B2 (en) * 2004-03-31 2009-07-09 Daikin Industries, Ltd. Heat exchanger
KR101174556B1 (ko) * 2007-10-05 2012-08-16 다이킨 고교 가부시키가이샤 조습장치
JP4360434B2 (ja) * 2007-10-05 2009-11-11 ダイキン工業株式会社 空気調和装置
WO2010134284A1 (fr) * 2009-05-22 2010-11-25 ダイキン工業株式会社 Procédé pour le traitement d'un fluide, appareil pour le traitement d'un fluide et fluide
JP5786646B2 (ja) * 2011-10-27 2015-09-30 ダイキン工業株式会社 調湿装置
JP5452565B2 (ja) * 2011-10-27 2014-03-26 三菱電機株式会社 除湿装置
JP5906708B2 (ja) * 2011-12-13 2016-04-20 ダイキン工業株式会社 調湿装置

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4398927A (en) * 1980-07-30 1983-08-16 Exxon Research And Engineering Co. Cyclic adsorption process
JPH07275642A (ja) * 1994-04-06 1995-10-24 Matsushita Electric Ind Co Ltd 除湿装置
US5826434A (en) * 1995-11-09 1998-10-27 Novelaire Technologies, L.L.C. High efficiency outdoor air conditioning system
JP2000146220A (ja) * 1998-11-02 2000-05-26 Nissan Motor Co Ltd 空気調和手段及び空気調和装置
JP2006264490A (ja) * 2005-03-23 2006-10-05 Mazda Motor Corp 車両用空調装置
JP2006349294A (ja) 2005-06-17 2006-12-28 Daikin Ind Ltd 調湿装置
JP2008247305A (ja) * 2007-03-30 2008-10-16 Mitsubishi Chemicals Corp 車両用除加湿装置
JP2010190495A (ja) * 2009-02-18 2010-09-02 Daikin Ind Ltd 調湿装置
JP2013092290A (ja) * 2011-10-25 2013-05-16 Daikin Industries Ltd 除湿システム

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3015778A4

Also Published As

Publication number Publication date
EP3015778A1 (fr) 2016-05-04
KR101630143B1 (ko) 2016-06-13
CN105358915B (zh) 2016-10-19
BR112015032117A2 (pt) 2017-07-25
EP3015778A4 (fr) 2017-02-22
JP2015028415A (ja) 2015-02-12
CN105358915A (zh) 2016-02-24
JP5885781B2 (ja) 2016-03-15
KR20160025012A (ko) 2016-03-07
US20160146479A1 (en) 2016-05-26

Similar Documents

Publication Publication Date Title
JP5885781B2 (ja) 除湿装置および除湿システム
JP5695752B2 (ja) 除湿システム
JP7104339B2 (ja) 空気質の調整システム
JP5521106B1 (ja) 除湿システム
JP5218135B2 (ja) 調湿装置
JP2017044387A (ja) 除湿システム
JP2015068599A (ja) 除湿システム
JP6054734B2 (ja) 除湿システム
JP2015087070A (ja) 除湿システム
JP2016084982A (ja) 除湿装置
JP6051039B2 (ja) 除湿システム
JP5624185B1 (ja) 除湿システム
JP6009531B2 (ja) 除湿システム
JP2017044386A (ja) 除湿システム
JP2005140372A (ja) 空気調和装置
JP6050107B2 (ja) 除湿システム
JP2005164220A (ja) 空気調和装置
JP3712001B2 (ja) 空気調和機および空気調和機の制御方法
JP2017138078A (ja) 除湿システム
JP6235942B2 (ja) 除湿システム
JP2016031208A (ja) 除湿システム
JP6085468B2 (ja) 除湿システム
JP2017227355A (ja) 調湿装置
JP2015175566A (ja) 除湿装置
JP2015020080A (ja) 除湿システム

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201480036707.6

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14818067

Country of ref document: EP

Kind code of ref document: A1

WWE Wipo information: entry into national phase

Ref document number: 14897098

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: 2014818067

Country of ref document: EP

NENP Non-entry into the national phase

Ref country code: DE

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112015032117

Country of ref document: BR

ENP Entry into the national phase

Ref document number: 20167002316

Country of ref document: KR

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: 112015032117

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20151221