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WO2014206441A1 - Sèche-linge à pompe à chaleur - Google Patents

Sèche-linge à pompe à chaleur Download PDF

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Publication number
WO2014206441A1
WO2014206441A1 PCT/EP2013/063160 EP2013063160W WO2014206441A1 WO 2014206441 A1 WO2014206441 A1 WO 2014206441A1 EP 2013063160 W EP2013063160 W EP 2013063160W WO 2014206441 A1 WO2014206441 A1 WO 2014206441A1
Authority
WO
WIPO (PCT)
Prior art keywords
module
header
heat exchanger
refrigerant
air duct
Prior art date
Legal status (The legal status 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 status listed.)
Ceased
Application number
PCT/EP2013/063160
Other languages
English (en)
Inventor
Francesco Cavarretta
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Electrolux Appliances AB
Original Assignee
Electrolux Appliances AB
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 Electrolux Appliances AB filed Critical Electrolux Appliances AB
Priority to CN201380077712.7A priority Critical patent/CN105324529B/zh
Priority to AU2013396776A priority patent/AU2013396776B2/en
Priority to EP13734686.2A priority patent/EP3014011B1/fr
Priority to PCT/EP2013/063160 priority patent/WO2014206441A1/fr
Publication of WO2014206441A1 publication Critical patent/WO2014206441A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00—Domestic laundry dryers
    • D06F58/20—General details of domestic laundry dryers 
    • D06F58/206—Heat pump arrangements
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
    • D06F58/00—Domestic laundry dryers
    • D06F58/20—General details of domestic laundry dryers 
    • D06F58/24—Condensing arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00—Compression machines, plants or systems with non-reversible cycle
    • F25B1/005—Compression machines, plants or systems with non-reversible cycle of the single unit type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05391—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/26—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators
    • F28F9/262—Arrangements for connecting different sections of heat-exchange elements, e.g. of radiators for radiators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/07—Details of compressors or related parts
    • F25B2400/071—Compressor mounted in a housing in which a condenser is integrated
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/007—Condensers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/0071—Evaporators

Definitions

  • the present invention relates to a laundry dryer including a heat pump, in particular to a laundry dryer which optimizes the energy consumption and/or the duration of the drying cycles.
  • tumble dryers consist of a rotating drum called a tumbler, thus called tumble dryer, through which heated air is circulated to evaporate the moisture from the load.
  • the tumbler is rotated around its axis.
  • Known laundry dryers include two categories: condense laundry dryers and vented laundry dryers. Dryers of the first category circulate air exhausted from the drum through a heat exchanger/condenser to cool the air and condense the moisture; they subsequently re-circulate the air back through the drum, after having heated the same using a heater. Dryers of the second category draw air from the surrounding area, heat it, blow it into the drum during operation and then exhaust it through a vent into the outside.
  • dryers of the first category are the most common in the market, due to the fact that they do not require special means for proper installation such as an exhaust duct to exhaust the humid hot air coming from the drum.
  • the drying cycle of a condensed dryer is longer than an equivalent cycle in a vented dryer.
  • the heat pump includes a refrigerant with which the air is in thermal exchange, and the refrigerant is compressed by a compressor, condensed in the condenser laminated in an expansion device and then vaporized in the evaporator.
  • EP 1209277 discloses a heat-pump clothes drying machine in which the motor used to drive the drum holding the clothes to be dried is also connected to a first fan, which circulates the drying air, as well as a second fan that cools the compressor.
  • US 2011/0280736 relates to a control method of a dryer.
  • a control method of a dryer including a heat pump having a variable velocity type compressor the control method includes steps of selecting at least one course supplying air or dried air; increasing an activation velocity of the compressor to a target velocity, as the selected course is implemented; and adjusting an open degree of an expansion valve provided in the heat pump.
  • the present invention is relative to a laundry dryer for drying clothes and other garments including a heat pump having a first and a second heat exchanger.
  • the dryer of the invention may include either a vented or a condense dryer.
  • the configuration and location of the heat exchangers in the laundry dryer of the invention is such that a high ratio between the heat transfer capacity and the heat exchanger volume is achieved. Therefore, in case the heat transfer capacity is kept constant with respect to prior art dryers, in the dryer of the invention more free space is available for the other dryer's components (e.g. compressor, motor, electronic board, etc.). For example, the amount of space occupied by the heat exchanger(s) in the casing of the dryer can be reduced without affecting the amount of exchanged heat. Alternatively, using the same space for the heat exchanger(s) as in the prior art, an improved heat transfer capacity is achieved in the dryer of the invention.
  • a heat pump dryer includes a drying chamber, such as a drum, in which the load, e.g., clothes, to be dried is placed.
  • the drying chamber is part of a process air circuit, in particular a closed-loop circuit in case of a condensed dryer or an open circuit in case of a vented dryer, which in both cases includes an air duct for channeling a stream of air to dry the load.
  • the process air circuit is connected with its two opposite ends to the drying chamber. More specifically, hot dehumidified air is fed into the drying chamber, flowing over the laundry, and the resulting humid cool air exits the same.
  • the humid air stream rich in water vapor is then fed into an evaporator of a heat pump, where the moist warm process air is cooled and the humidity present therein condenses.
  • the resulting cool dehumidified air is then either vented outside the dryer in the ambient where the latter is located or it continues in the closed-loop circuit.
  • the dehumidified air in the process air circuit is then heated up before entering again in the drying chamber by means of a condenser of the heat pump, and the whole loop is repeated till the end of the drying cycle.
  • ambient air enters into the drum from the ambient via an inlet duct and it is heated up by the condenser of the heat pump before entering the drying chamber.
  • the heat pump of the apparatus includes a refrigerant circuit in which a refrigerant can flow and which connects via piping a first heat exchanger or condenser, a second heat exchanger or evaporator, a compressor and a pressure-lowering device.
  • the refrigerant is pressurized and circulated through the system by the compressor.
  • the hot and highly pressurized vapor is cooled in the first heat exchanger, called the condenser, until it condenses into a high pressure, moderate temperature liquid, heating up the process air before the latter is introduced into the drying chamber.
  • the condensed refrigerant then passes through the pressure-lowering device such as an expansion device, e.g., a choke, a valve or a capillary tube.
  • the low pressure liquid refrigerant then enters the second heat exchanger, the evaporator, in which the fluid absorbs heat and evaporates due to the heat exchange with the warm process air exiting the drying chamber.
  • the refrigerant then returns to the compressor and the cycle is repeated.
  • the refrigerant in the first and/or second heat exchanger, may not be subject to a phase transition.
  • downstream a position with reference to the direction of the flow of a fluid inside a conduit is indicated.
  • vertical and “horizontal” are referred to the positions of elements with respect to the dryer in its normal installation or functioning. Indeed, a horizontal plane (X,Y) formed by two horizontal X,Y perpendicular directions is defined, and a vertical direction Z, perpendicular to the horizontal plane, is defined as well in a 3-D space.
  • each module includes two headers, which can be an inlet header to allow the inflow of refrigerant into the module and an outlet header to allow the refrigerant to discharge from the module.
  • the module includes a plurality of heat exchange layers stacked in a stackwise direction (e.g., the layers are disposed one on top of the other along a given direction).
  • Each heat exchange layer includes more than one channel for the refrigerant flow, the channels being located one adjacent to the other(s) within the layer.
  • the channels are in fluid communication with the inlet and/or the outlet header so that the refrigerant is allowed to flow from the inlet to the outlet header and/or vice versa.
  • the plurality of channels is parallel to each other within each heat exchanger layer.
  • Each heat exchange layer defines two opposite ends, one of which is fixed to said either inlet or outlet header, the layers thus departing from the inlet and/or the outlet header.
  • each heat exchange layer includes an upper plate and a lower plate attached to each other, each of which is stamped or otherwise formed to partially define the lower or upper half of a plurality of internal channels, completely formed when the two plates are attached together.
  • the plurality of channels is also substantially parallel to each other, however they can also be angled or they can have an irregular shape.
  • the stackwise direction is a vertical direction and the heat exchange layers are stacked one on top of the other.
  • the heat exchange layers have a given width which depends on the number of channels realizing the heat exchange layer, and a longitudinal extension, which corresponds to the longitudinal extensions of the channels forming the same.
  • the width and the longitudinal extension direction preferably define a plane. This plane might be perpendicular to the vertical stacking direction of the layers, or it can form an angle with the same.
  • the layers may be tilted one with respect to the other or may form arches one on top of the other; the arches could be parallel to each other, e.g., having a constant distance one with respect to the other(s), or tilted.
  • channels of neighboring heat exchange layers in the stacking direction are connected by fins.
  • the inlet and outlet headers may be at a given distance from each other, so that the heat exchange layers are connected at their opposite ends to the inlet and outlet headers, respectively, e.g., the heat exchange layers are interposed between the inlet and the outlet headers, or the inlet and outlet headers can be located one in contact or adjacent to the other for example one on top of the other, so that the heat exchange layers are attached with one end to the inlet or to outlet header and with the opposite end to an intermediate header.
  • the refrigerant flows from the inlet to the outlet header bridging a single heat exchange layer, while in the second case from the inlet header the refrigerant has to flow through at least two heat exchange layers, one flowing in one direction and one flowing in substantially the opposite direction, in order to reach the outlet header.
  • the plurality of channels is subjected to, at least in part, the process air stream so that there is heat exchange between the refrigerant flowing within the channels and the process air.
  • the channels of the heat exchange layers of the modules of the first and/or second heat exchanger are located within the air duct, part of the process air circuit.
  • the headers have the function of holding the various heat exchange layers and as an inlet and/or outlet for the refrigerant into the module.
  • the headers occupy "useful space" within the air duct of the dryer, without providing any benefit from this positioning.
  • the headers to not contribute in a relevant way to the heat exchange between refrigerant and process air.
  • the headers of the modules of either the first or the second - or of both - heat exchanger can be placed, at least partially, outside the air duct where the process air stream flows.
  • the inventions relates to a laundry dryer comprising:
  • a heat pump having a heat pump circuit in which a refrigerant can flow, said heat pump circuit including a first heat exchanger where the refrigerant is cooled off and the process air stream is heated up, and a second heat exchanger where the refrigerant is heated up and the process air is cooled off; said first and/or second heat exchanger being thermally coupled to the process air conduit to perform heat exchange between said refrigerant flowing in said heat pump circuit and said process air stream; said first and/or second heat exchanger further comprising a heat exchanger module, said module including
  • a plurality of heat exchange layers fluidly connecting said inlet to said outlet header to enable said refrigerant to flow from said inlet to said outlet header and/or vice versa; said heat exchange layers being stacked one on top of the others and each layer including a plurality of channels; characterized in that said plurality of heat exchange layers is at least partially arranged inside said air duct and in that the inlet header and/or the outlet header of said module is located at least partially outside said air duct.
  • the headers, or at least some (or one) of the headers outside the air duct frees some space within the air duct itself. Therefore, the lateral width, e.g., the dimension substantially perpendicular to the air flow, of the duct itself can be reduced, for example by the amount which was occupied by the header now located outside the duct, without reducing the heat exchange capacity of the first and/or second heat exchanger. In this way, the other components present within the dryer can be more easily arranged in the casing of the layer and/or additional component(s) can find space in the casing as well.
  • the lateral width of the air duct can be kept constant and the heat exchange layers can be lengthened of the amount which was occupied by the header now located outside the duct, thus increasing the heat transfer capacity of the dryer, and at the same time without hindering the correct placement of other components in the air duct.
  • the air duct in which the modules are present can be in any location of the laundry dryer, depending on the layout of the same, and it can have any configuration, e.g., it can be straight, curved, realized integral to another portion of the casing of the laundry dryer or separated from the same; it may include further elements in addition to the modules of the heat exchangers or it may be empty otherwise, etc.
  • the air duct has the function of a housing for the first and/or second heat exchanger and to direct the flow through the same.
  • the air duct is air tight.
  • the dryer of the invention may include, alternatively or in combination, any of the following characteristics.
  • each of said heat exchange layers includes a first and a second opposite ends, said first end being connected to said inlet header and said second end being connected to said outlet header.
  • inlet and outlet headers are located at the two opposite ends of each heat exchange layer.
  • the channels thus are transporting the refrigerant from the inlet to the outlet header directly.
  • each of said heat exchange layers includes a first and a second opposite ends, said first end being connected to said inlet or said outlet header and said second end being connected to an additional header.
  • the layout of the modules can change and different inlets and outlets can be present as well from the headers, e.g., a plurality of inlet and outlet headers can also be present for the same module.
  • the inlet and outlet headers are stacked one on top of the other.
  • said casing includes a basement.
  • Said air duct, wherein said heat exchange layers are at least partially arranged, is realized in said basement.
  • the process air exits the chamber through an aperture realized in the boundary of a door of the casing and it bends downwards passing through a filter to collect lint. Furthermore, the process air bends again to flow within the basement of the casing, wherein there is generally available space to locate the heat exchanger(s) of the heat pump. In the basement, the air duct for the flow of the process air is preferably realized, to allow the process air to exchange heat with the heat exchangers, so that from humid it can turn hot and dehumidified in order to be redelivered within the chamber.
  • the air duct and the heat exchangers can be located on top of the dryer, e.g., on top of the drying chamber; or it can be located on the basement like in the above described embodiment, however, differently from above, the process air exits the chamber through apertures realized in the uppermost region of the drying chamber and returns in the drying chamber via additional apertures realized in a lowermost region of the same.
  • both said first and second heat exchangers include heat exchanger module, respectively called first and second heat exchanger module, the heat exchange layers of said first and second heat exchanger modules being located at least partially inside said air duct.
  • both heat exchangers include modules having the headers and the plurality of stacked heat exchange layers. In this way, the heat transfer between the refrigerant and the process air is most efficient. In addition, also the space occupied by the heat exchangers is minimized, due to the modules' construction.
  • the heat exchangers both exchange heat with the process air and thus they are both, at least partially, located within the air duct. More preferably, they are both located within the air duct realized in the basement of the dryer.
  • said air duct includes a longitudinally straight portion wherein the heat exchange layers of said first and/or second heat exchanger modules are at least partially located.
  • the air duct realized in the dryer includes a straight portion to minimize the space occupied by it and to maximize the heat exchange between the process air and the modules.
  • the air duct might include other portions as well, such as curved or bended portions.
  • the air duct is straight for all its extension.
  • the direction defined by the longitudinal extension of the heat exchange layers and the direction defined by the longitudinal extension of the straight portion of the air duct are substantially perpendicular one to the other, so that the air flow flowing parallel to the lateral walls of the air duct impinges on the heat exchange layers in a "frontal" manner.
  • both said first and second heat exchangers include the heat exchanger module, respectively called first and second heat exchanger module, and a first longitudinal direction of the heat exchange layers of said first module and a second longitudinal direction of the heat exchange layers of said second module are substantially parallel to each other.
  • the first and/or second longitudinal direction is substantially perpendicular to the direction of flow of said process air inside said air duct. It is preferable, in order to maximize heat exchange, that the process air stream flowing through the air duct "hits" the modules substantially in a perpendicular manner, i.e., in such a way that a vertical plane - defined by the module vertical and longitudinal extensions - and the direction of the process air stream within the air duct are substantially perpendicular. In this way, air turbulence is minimized and heat transfer maximized.
  • the preferred configuration is thus having two substantially parallel modules within the straight portion of the air duct. More preferably, these two modules are also perpendicular to the longitudinal extension of the air duct.
  • both said first and second heat exchangers include the heat exchanger module, respectively called first and second heat exchanger module, and a first longitudinal direction of the heat exchange layers of said first module and a second longitudinal direction of the heat exchange layers of said second module form an angle between each other different from 0° and 180°.
  • the air flow within the air duct regardless of the shape of the duct itself, is not always parallel to the air duct, for example it can enter the same forming an angle with the longitudinal extension of the latter.
  • placing the modules at different angles can maximize the length of the heat exchange layers and thus maximize the heat exchange capacity, because the width of the duct is not any more the maximum extension available, the modules being positioned diagonally to it.
  • both said first and second heat exchangers include the heat exchanger module, respectively called first and second heat exchanger module.
  • the said first module and said second module are both at least partially arranged inside said air duct, said air duct including first and second opposite lateral walls, and the inlet header or outlet header of said first module in proximity to said first or second lateral wall, and the inlet header or outlet header of said second module in proximity to the same of said first or second lateral wall, are located at least partially outside said air duct.
  • both said inlet and said outlet header of said module of said first and/or said second heat exchanger positioned "on the same side" of the air duct, e.g., attached to the same either left or right wall, are located at least partially outside said air duct.
  • all inlet and outlet headers of said first and said second heat exchanger are located outside said air duct.
  • said air duct includes an upper portion and a lower portion connectable or connected to each other, and at least a lateral slot in said upper and/or lower portion in which said portion of said inlet or outlet header is inserted and from which said portion is apt to exit the air duct.
  • the air duct has to be at least divided in two pieces which are then connected to each other in order to allow the insertion of the first and/or second heat exchanger.
  • a slot in one of the walls e.g., in one or both upper and lower portions of the air duct, is preferably present.
  • said air duct includes a sealing element apt to seal a gap formed between the slot and the inserted inlet or outlet header.
  • the header protruding from the air duct leaves a gap between the wall(s) of the air duct and the header itself.
  • a sealing element is used to prevent this leakage.
  • the outlet header of the module of the first heat exchanger is located at least partially outside said air duct and the laundry dryer further includes an additional fluid circuit where an additional fluid is apt to flow, located in such a way that the refrigerant flowing within the outlet header can exchange heat with said additional fluid.
  • the header Due to the fact that the header is placed outside of the air duct, it can be easily cooled down, using an additional fluid.
  • a fluid can be for example air moved by a fan, condensed water or other fluids.
  • the circuit can include a fan only, without any piping, with the name "circuit” simply indicating the movement of the fluid in a given direction.
  • the circuit might be "designed" by the basement or casing itself which includes walls which confine the additional fluid motion.
  • This additional fluid is not the process air.
  • the dryer includes a fan moving said additional fluid, said fan being located in such a way to cool down the refrigerant in or exiting the outlet header of the first heat exchanger.
  • the fan is used to cool down only the outlet header.
  • An air barrier or an insulating layer, suitably located, is preferably used to avoid that also the inlet header of the first heat exchanger is cooled by the fan.
  • the additional fluid in this preferred embodiment is air moved by a fan.
  • the fan can be for example the same cooling fan already present in the dryer in order to cool down the compressor.
  • a dedicated fan can be included in the dryer that cools down the refrigerant in or exiting the header without cooling down the compressor.
  • the dryer also includes a temperature sensor apt to detect the temperature of the refrigerant flowing in said outlet header, said fan is apt to be commanded depending on the temperature sensed by said sensor.
  • the fan could for example operate in an on/off manner.
  • a maximum temperature threshold can be selected, and the temperature of the refrigerant flowing inside the outlet header of the first heat exchanger, or of the refrigerant which has just exited the outlet header, is checked. In case such a temperature rises above the selected maximum temperature threshold, the fan is activated to cool the refrigerant.
  • the fan has a variable rotating speed which also depends on the detected temperature by the sensor, i.e., the higher the temperature of the refrigerant, the higher the rotational speed of the fan.
  • the outlet header of the module of the second heat exchanger is located at least partially outside said air duct and the dryer further includes a second additional fluid circuit where an additional fluid is apt to flow, located in such a way that the refrigerant flowing within the outlet header can exchange heat with it.
  • the dryer includes a further fan moving said second additional fluid, said further fan being located in such a way to move said additional fluid so that it exchanges heat with the refrigerant in or exiting the outlet header of the second heat exchanger.
  • This even further fan is used to cool down the refrigerant exiting the second heat exchanger and directed towards the compressor.
  • the additional fluid which is preferably air moved by the fan, is warming up the refrigerant flowing towards the compressor and speed up the warm up process of the heat pump system.
  • the risk of unwanted refrigerant droplets flowing into the compressor is minimized.
  • this further fan can be used to avoid overheating of the refrigerant and thus to cool down the same when it exits the module of the second heat exchanger.
  • This fan can also operate in an analogous manner than the fan described above with reference to the outlet of the first heat exchanger.
  • the cross-section of said inlet and/or said outlet header and/or said intermediate header is oblong, wherein its smallest diameter is smaller than a width of said layer.
  • the headers of the heat exchangers' modules are oblong, e.g., they have an oval or rectangular cross section, in order to further reduce the internal volume of the exchangers, reducing space, and also in order to save some refrigerant.
  • the refrigerant is indeed relatively expensive and it is preferred to minimize the same for a given heat exchange capacity.
  • the exchange surface e.g., the total external surface of channels layers and fins which can enter into contact with the process air and exchange heat
  • the exchange surface can be increased since the portion of the process air duct used to locate the header is reduced, so the extension of the channels can be increased.
  • the minimum dimension of the cross section of the inlet/outlet/intermediate header is fixed: it has to be wide enough to be connected to one end of the heat exchange layer and thus it has to be at least as wide as the heat exchange layer.
  • the maximum width, or diameter can be reduced below the layers' width.
  • said cross section of said inlet and/or said outlet header and/or said intermediate header is oval or rectangular.
  • said channels have a hydraulic diameter smaller or equal than 5 mm.
  • the hydraulic diameter of each of the channel is smaller or equal than 5 mm, i.e. D H ⁇ 5 mm, more preferably D H ⁇ 3 mm, even more preferably D H ⁇ 1 mm.
  • the module of the invention may include many channels, therefore the refrigerant flow is divided in a plurality of smaller refrigerant streams, one per channel. In this way the pressure drop of the refrigerant within the channels is reduced compared to the refrigerant pressure drop in bigger channels. Additionally, it is known that the maximum pressure that a pipe can withstand is inversely proportional to its hydraulic diameter. A small hydraulic diameter therefore means that the channels can withstand higher pressures than bigger pipes. For this reasons, high pressures refrigerants, such as carbon dioxide, can be used in the heat pump circuit of the dryer of the invention.
  • the shape of the cross section of the channels is not relevant for the present invention, and it can be squared, rectangular, circular (in this case the hydraulic diameter coincide with the diameter of the circle), elliptic, and so on.
  • the cross section of the plurality of channels does not have to be the same for all channels in the plurality, but it can be different and the various channels can have a combination of the possible above listed cross sections.
  • the cross section may vary both in hydraulic diameter and/or in shape along the extension of the channel.
  • said heat exchange layer includes a plurality of channels one parallel to the others.
  • the channels extend along a direction which is substantially parallel to the horizontal plane and also perpendicular to the flow of the process air stream when the dryer is functioning.
  • the channels which preferably have a diameter much smaller than their length, extend from one header to another header in such a way that their longitudinal extension results substantially parallel to the horizontal plane and perpendicular to the flow of process air with which the heat exchange takes place.
  • the channels are rectilinear, their longitudinal extension (and longitudinal direction) corresponds to their longitudinal axis.
  • their longitudinal extension (and longitudinal direction) corresponds to the line joining the point from which they depart from the inlet/outlet header and the first point having the maximum distance from the inlet/outlet header longitudinal axis.
  • the channels may include rectilinear portions and/or bumps or other turbulence-inducing elements that may enhance the heat transfer between the refrigerant and the air process stream. Additionally, channels may include smooth or corrugated inner and/or outer surfaces and may comprise bends or curves.
  • the channels are rectilinear.
  • the channels include a plurality of rectilinear portions connected to each other via U-bends.
  • the rectilinear portions are preferably stacked one on top of the other in a vertical direction.
  • the rectilinear portions are coplanar, more preferably in a plane parallel to the horizontal plane.
  • the channels are bended forming an arch, their longitudinal extension being preferably still perpendicular to the process air flow.
  • This latter embodiment is used in particular to place the module of the dryer of the invention in the most suitable location within the process air conduit. Indeed, it is known that there are portions of the process air conduit in which the process air flow is more uniform and less turbulent. Heat exchange between the process air flow and the refrigerant is therefore optimal in these locations.
  • An arched channel allows the positioning of the module also in locations in which other objects are present or narrow thus in general to better exploit the available space and/or to reduce the limitations given by a not even distribution of the air flow.
  • said first heat exchanger includes more heat exchanger modules that said second heat exchanger.
  • Fig. 1 is a schematic view, where some elements have been removed for clarity, of a laundry dryer according to the invention
  • Fig. 2 is a perspective view of a portion of an embodiment of the dryer of the invention of fig. 1 with the casing removed;
  • Fig. 3 is a perspective view in section of an element of the dryer of fig. 1;
  • Figs. 4a and 4b are a schematic front view and top view, respectively, of an embodiment of the heat exchanger module of the dryer of the invention of fig. 1;
  • Figs. 5a and 5b are a schematic front view and top view, respectively, of a further additional embodiment of the heat exchanger module of the dryer of the invention of fig. 1;
  • Figs. 6a and 6b are a schematic front view and top view, respectively, of an embodiment of connection between two heat exchanger modules of any of the examples of figs. 4a-4b to figs. 5a-5b;
  • Figs. 7a and 7b are a schematic top view of a comparison laundry dryer and a laundry dryer of the present invention, respectively, according to a preferred embodiment of the invention.
  • Figs. 8a and 8b are a schematic top view of a comparison laundry dryer and a laundry dryer of the present invention of fig. 1, respectively, according to an additional preferred embodiment of the invention
  • Figs. 9a, 9b and 9c are two schematic top views (9a & 9c) of a laundry dryer of the present invention of fig. 1, and of an enlarged detail thereof, 9b, according to two further additional preferred embodiments of the invention;
  • Figs. 10a, 10b and 10c are schematic front view of three different embodiments of a heat exchanger module used in the laundry dryer of the invention of fig. 1;
  • Fig. 11 is a schematic top view of a laundry dryer of the present invention of fig. 1, according to a further additional preferred embodiment of the invention.
  • Fig. 12 is a schematic top view of a laundry dryer of the present invention of fig. 1, according to a further additional preferred embodiment of the invention.
  • Fig. 13 is a schematic lateral cross section of a heat exchanger module used in the laundry dryer of the invention of fig. 1;
  • Fig. 14 is a schematic lateral view of an element of the laundry dryer of fig. 1. Detailed description of the preferred embodiments of the invention
  • a laundry dryer realized according to the present invention is globally indicated with 1.
  • Laundry dryer 1 comprises an outer box casing 2, preferably but not necessarily parallelepiped-shaped, and a drying chamber, such as a drum 3, for example having the shape of a hollow cylinder, for housing the laundry and in general the clothes and garments to be dried.
  • the drum 3 is preferably rotatably fixed to the casing, so that it can rotates around a preferably horizontal axis (in alternative embodiments, rotation axis may be vertical or tilted). Access to the drum 3 is achieved for example via a door, preferably hinged to casing, which can open and close an opening realized on the casing itself.
  • casing 2 generally includes a front panel 20, a rear wall panel 21 and two sidewall panel all mounted on a basement 24.
  • Panels 20, 21 and basement 24 can be of any suitable material.
  • the basement 24 is realized in plastic material.
  • basement 24 is molded.
  • basement 24 includes an upper and a lower shell (in fig. 2 only the lower shell 24a is visible).
  • the dryer defines an horizontal plane ( ⁇ ', ⁇ ') which is substantially the plane of the ground on which the dryer is situated, and a vertical direction Z' perpendicular to the plane ( ⁇ ', ⁇ ') ⁇
  • Laundry dryer 1 also comprises an electrical motor assembly la (visible in figs. 7b and 8b) for rotating, on command, revolving drum 3 along its axis inside casing.
  • Casing 2, revolving drum 3, door and motor la are common parts in the technical field and are considered to be known; therefore they will not be described in details.
  • Dryer 1 additionally includes a process air circuit 4 which comprises the drum 3 and an air process conduit 11, schematically depicted in fig. 1 as a plurality of arrows showing the path flow of a process air stream through the dryer 1.
  • air process conduit 11 includes an air duct 11a which is formed by the connection of the two upper and lower shells 24a. Air process conduit 11 is preferably connected with its opposite ends to two opposite sides of drum 3.
  • Process air circuit 4 may also include a fan or blower 12 (see fig. 1) and an electrical heater (not shown in the figures).
  • the air duct 11a can be integral with the basement 24 as depicted in fig. 2, or it can be a different element attached to the same, as depicted in fig. 14. Moreover, the air duct 11a can be located not only in the basement 24, but also in correspondence of a top or lateral part within the casing 2 of the laundry dryer 1.
  • the dryer 1 of the invention additionally comprises a heat pump 30 including a first heat exchanger called also condenser 31 and a second heat exchanger called also evaporator 32.
  • Heat pump 30 also includes a refrigerant closed circuit (schematically depicted in the picture with lines connecting the first to the second heat exchanger and vice versa, see in detail fig. 1) in which a refrigerant fluid flows, when the dryer 1 is in operation, cools off and may condense in correspondence of the condenser 31, releasing heat, and warms up, potentially even evaporating, in correspondence of the second heat exchanger (evaporator) 32, absorbing heat.
  • a refrigerant closed circuit (schematically depicted in the picture with lines connecting the first to the second heat exchanger and vice versa, see in detail fig. 1) in which a refrigerant fluid flows, when the dryer 1 is in operation, cools off and may condense in correspondence of the condenser 31, releasing heat, and warms up, potentially even evapor
  • the condenser and/or evaporator which indicates in this case respectively a gas heater and gas cooler, the refrigerant cools off or it warms up, respectively, without condensation or evaporation.
  • the heat exchangers are named either condenser and evaporator or first and second heat exchanger, respectively.
  • the heat pump circuit connects via piping 35 (visible in figs. 7b or 8b) the second heat exchanger 32 where the refrigerant warms up and may undergo a phase transition from the liquid to the vapor via a compressor 33 to the first heat exchanger 31, in which the refrigerant cools off and may condense again.
  • the cooled or condensed refrigerant arrives via an expansion device 34, such as a choke, a valve or a capillary tube, back at the evaporator 32.
  • the condenser 31 and the evaporator 32 of the heat pump 30 are located in correspondence of the process air conduit 11. More preferably, they are located in correspondence of the air duct 11a, for example of basement 24, at least partially.
  • the condenser 31 is located downstream of the evaporator 32.
  • the air exiting the drum 3 enters the conduit 11 and reaches the evaporator 32 which cools down and dehumidifies the process air.
  • the dehumidified cool process air continues to flow through the conduit 11 till it enters the condenser 31, where it is warmed up by the heat pump 30 before re-entering the drum 3.
  • a lint filter 103 to block the lint is preferably present in the dryer 1.
  • the lint filter 103 is preferably located before the process air reaches the evaporator 32, e. g., when it exits the drum 3.
  • First and/or second heat exchanger 31, 32 further include - according to a characteristic of the invention - one or more heat exchanger modules 10 located along the process air conduit 11.
  • the first and the second heat exchangers 31 and 32 are located in the air duct 11a.
  • the preferred location of the air duct 11a within the casing 2 is a volume of the same where enough space is available to host the modules 10.
  • the evaporator can include a different number of modules from the condenser (as per the appended figure 2 where the evaporator 32 includes two modules 10 and the condenser four modules 10).
  • the condenser 31 includes more modules than the evaporator 32.
  • the modules can be identical or different.
  • a heat exchanger module 10 includes an inlet header 5 and an outlet header 6.
  • Inlet and outlet headers 5,6 have preferably the structure of a pipe.
  • the headers have a longitudinal extension along an axis, which corresponds to the main direction of flow of the refrigerant within the headers.
  • the refrigerant is flowing into the module 10 via the inlet header 5 and exiting the same via the outlet header 6.
  • a plurality of channels, each indicated with 7, is fluidly connecting the inlet to the outlet header and vice versa, so that the refrigerant can enter and exit the module.
  • the plurality of channels is subject to the flow of process air, i.e., channels 7 are located within the air duct 11a of the dryer 1.
  • Channel 7 due to their configuration, allow a better heat exchange between the refrigerant and the process air than known dryers.
  • Channel 7 defines a longitudinal direction X along which it extends, which correspond to the longitudinal extension of the heat exchange layer 8.
  • the channels 7 are mounted in the module 10 so that their longitudinal extension X is substantially perpendicular to a process air flow direction and substantially parallel to the horizontal plane.
  • the longitudinal direction X lies on a plane parallel to the ( ⁇ ', ⁇ ') plane defined by the dryer 1.
  • the refrigerant flow within channels 7 is substantially perpendicular to the process air flow.
  • the direction of the process air stream and the direction of the refrigerant flow can form an angle therebetween.
  • each heat exchange layer includes a plurality of channels 7 which are preferably adjacent and parallel to each other. More preferably, each module 10 includes a plurality of heat exchange layers 8, more preferably all heat exchange layers 8 are stacked one on top of the other in a stackwise direction Z and even more preferably parallel to each other, substantially forming a plurality of parallel rows.
  • the stackwise direction is the vertical direction, i.e., Z and Z' are parallel to each other.
  • heat exchange layer 8 includes a single tube, having for example an elongated cross section, including two substantially parallel flat surfaces 9a,9b. Within the tube, separators 8a are realized in order to longitudinally divide the interior of the tube in the plurality of channels 7. Such a structure is schematically depicted in the cross section of a heat exchange layer 8 of fig. 13. The cross section of the single channel 7 can be arbitrary. Each heat exchange layer 8 has a width W which depends on the number of channels which are located one adjacent to the other (see figures 4b and 5b).
  • each couple of adjacent stacked heat exchange layers 8 is connected via fins 50.
  • the upper surface 9a of a heat exchange layer 8 is connected via the plurality of fins 50 to the lower surface 9b of the adjacent heat exchange layer 8.
  • the width W of the layer 8 defines a direction Y which, together with the longitudinal direction X of channels 7 defines a heat exchange layer plane (X,Y).
  • the heat exchange layer plane (X,Y) might be, when the module is mounted on the dryer, either parallel to the horizontal plane ( ⁇ ', ⁇ ') defined by the dryer 1 or tilted with respect to the same.
  • the heat exchange layer plane (X,Y) can be perpendicular to the stackwise direction Z or form an angle with the same.
  • each heat exchange layer 8 can also be not planar, but for example curved, e.g., having a concavity pointing either up or down along the stackwise direction.
  • a section of a header 5,6 is represented.
  • the header 5,6 includes a cylindrical envelope 107 in which a plurality of holes 7a are realized, the channels 7 forming a heat exchange layer 8 being inserted therein.
  • different configurations are possible, as better detailed below.
  • the cross section of the headers 5,6 is circular, or preferably oblong.
  • the cross section of the header refers to the cross section of the header along a plane perpendicular to the stackwise direction Z.
  • the oblong cross section is such that its smallest diameter, i.e., the smallest cord passing through the geometrical center of the cross section, is smaller than the width W of the heat exchange layer 8.
  • the cross section includes a "long side" 105 on which the heat exchange layer's 8 end can attach, and which has to have at least a width equal to (or wider than) W, and a "shorter side" 106 realized in order to minimize space.
  • the cross section of the header 5,6 is an oval, in figure 10c a rectangle.
  • a single module 10 may also include a header 5,6 having a given cross section and the other header 5,6 having a different cross section.
  • the refrigerant entering the module 10 via the inlet header 5 can come from the outlet header 6 of another module 10, from the compressor 33 or from the expansion device 34. Additionally, the refrigerant exiting the outlet header may be directed towards the inlet header 6 of another module 10, towards the expansion device 34 or towards the compressor 33.
  • the connection between the compressor 33, modules 10 and expansion device 34 and between modules is made via piping 35, as it can be seen in figures 7b and 8b. In the following figures, the flow of the refrigerant will be indicated with a dotted line having a pointing arrow in the direction of the flow.
  • the heat exchange layers 8 includes two opposite ends 8b,8c. In some embodiments, one end 8b is connected to the inlet header 5 and the opposite end 8c is connected to the outlet header 6. Alternatively, an additional intermediate header can be present, as detailed below.
  • the two headers 5,6 are mounted vertically (i.e. their axis Z is the vertical axis Z' of the dryer 1) on the basement 24 of the dryer 1, parallel one to the other, and the channels 7 connecting the two headers 5,6 are substantially straight along the longitudinal direction X.
  • Channels 7 are divided in heat exchange layers 8, each of which includes a different tube defining upper and lower surfaces 9a,9b (see fig. 14) within which the channels 7 are realized.
  • a plurality of heat exchange layers 8 connects the inlet 5 to the outlet header 6, all layers having a first end 8b and a second end 8c longitudinally opposite to each other, the first end being connected to the inlet header and the second end being connected to the outlet header.
  • Heat exchange layers are stacked one on the other along the vertical direction forming a plane (Z,X) defined by the longitudinal extension X of the channels 7 and the direction of stacking Z. This plane is perpendicular to the horizontal plane ( ⁇ ', ⁇ ') and to direction of flow of process air as clear from figs. 4a, 4b.
  • each heat exchange layer has a width direction Y perpendicular to the longitudinal extension X of the channels 7.
  • this width direction Y is parallel to the horizontal plane ( ⁇ ', ⁇ ') and the air flow direction; i.e., the layer planes (X,Y) are horizontal (parallel to the horizontal plane ( ⁇ ', ⁇ ')).
  • the module 10 is mounted so that the heat exchange layers 8 form parallel planes between which the process air flows.
  • a plurality of apertures 7a is realized, in each aperture 7a a channel 7 being inserted.
  • the so- formed rows of apertures 7a are parallel one to the other and perpendicular to the longitudinal extension Z of the header 5,6.
  • the refrigerant enters the inlet header 5 of module 10 via an inlet aperture 5in along a flow direction parallel to the longitudinal extension Z of header 5 and branches off into the various channels 7 via apertures 7a.
  • the heat exchange layers 8 are "parallel" to each other according to the refrigerant flow direction.
  • the flow of the refrigerant is substantially parallel to the flow direction of the refrigerant in the other channels and has the same direction.
  • the refrigerant then exits the module via an outlet aperture 6out of outlet header 6.
  • the direction of flow of refrigerant in the headers 5,6 is perpendicular to the process air flow.
  • the flow of the refrigerant in the inlet header is parallel to the flow of the refrigerant in the outlet header, but with opposite direction.
  • the refrigerant flow in the inlet and in the outlet header can also be parallel and have the same direction.
  • one of the two headers includes a transversal separator 17 which divides the header in two separated portions.
  • the first portion represents the inlet header 5, while the second portion is the outlet header 6.
  • the second header 5a is an intermediate header for the refrigerant flow. The flow of refrigerant entering the header 5 is therefore prevented by separator 17 to go from the first to the second portion 5,6 of the header.
  • the heat exchange layers 8 are thus divided in two groups: the first group Gl connects the first portion 5 (the inlet header 5) to the intermediate header 5a and the second group G2 connects the intermediate header 5a to the second portion, outlet header 6.
  • the refrigerant flow which enters the first portion 5 (the inlet header 5) in a vertical Z direction is distributed via apertures 7a into the first group Gl of heat exchange layers 8 and the refrigerant flows within the parallel channels in the first group Gl towards the intermediate header 5a. Therefore, the heat exchange layers within the first group Gl are parallel with respect to the refrigerant flow.
  • the refrigerant streams exit the first group Gl of heat exchange layers 8 and enter the intermediate header 5a, where they merge. From the intermediate header 5a, the refrigerant flow then enters the second group G2 of heat exchange layers 8 reaching the outlet header 6.
  • the heat exchange layers within the second group G2 are parallel to each other with respect to the refrigerant flow.
  • the layers of the two groups Gl, G2 are in series with respect to the refrigerant flow. Indeed, the refrigerant flows in parallel in all layers belonging to the same group, while it has to flow through the layers of first and the second group in a given order - the layers of the two groups being thus in series.
  • a first and a second module 10, 10' are connected to each other.
  • These two modules can for example both belong to the condenser 31, as depicted in the schematic drawings of figs. 7b and 8b.
  • the two modules are realized parallel one to the other and one in front of the other in the direction of flow of the process air, both substantially perpendicular to the horizontal plane.
  • Both modules have heat exchange layers 8,8' which are parallel to the horizontal plane.
  • the refrigerant flow enters the inlet header 5 of the first module 10, it divides within the plurality of channels 7 and the various streams merges in the outlet header 6.
  • the refrigerant exits the first module 10 via the outlet header 6, thus entering the inlet header 5' of the second module 10'.
  • the refrigerant flow travels through the plurality of channels 7' and exits the second module via the outlet header 6' of the second module.
  • the modules 10,10' are in series with respect to the process air flow and in series with respect to the refrigerant flow.
  • At least one of the module 10 of the first and/or of the second heat exchanger and more preferably both a modules 10 of the first and a module 10' of the second heat exchanger are located at least partially within the air duct 11a, as said above. Due to the fact that the heat exchange between the process air and the refrigerant take place in correspondence to the surface of the heat exchange layers 8,8' and of the fins 50, the heat exchange layers 8,8' and fins 50 are preferably completely located within the air duct 11a, so that the heat exchange is maximized. According to the invention, at least one header 5,6,5a of one module 10,10' is located - at least partially - outside the air duct 11a.
  • air duct 11a is preferably "openable", e.g., it includes an upper and a lower portion 111, 112 which can be assembled after the modules 10,10' have been inserted.
  • Upper and lower portion 111,112 can be integral with the basement or anyhow with a portion of casing 2, or can be separated elements as depicted in fig. 14.
  • Modules 10,10' are inserted within air duct 11a preferably in such a way that the process air (depicted as an arrow in fig. 14) flow passes through the heat exchange layers 8, 8' and it is substantially parallel to the layers itself.
  • the modules are mounted perpendicular to the air flow, i.e., the stackwise direction is substantially perpendicular to the process air flow direction.
  • the air duct 11a includes a straight portion 118 (see fig. 14), i.e., in the horizontal plane the air duct extends rectilinearly at least for a given length. As shown, the air duct 11a is straight for all its extension. Other configurations are possible, e.g., the air duct 11a may include curvilinear portions as well, such as an arc or bend (not shown in the appended drawings), to better follow the natural path of the process air stream entering the duct.
  • the process air flow entering the same is flowing substantially parallel to the straight portion itself, e.g., the air duct 11a includes an inlet 113 for the process air, an outlet 114 for the same and opposite lateral walls 117 (only one visible in fig. 14) parallel to which the process air can flow.
  • the modules 10, 10' are thus preferably located substantially perpendicularly to the lateral walls 117.
  • the air duct 11a is parallel to the sidewall of casing 2. It is to be understood that the air duct 11a can also be diagonally placed within the basement 24.
  • all modules 10,10' of both evaporator 32 and condenser 31 adjacent or in proximity to the same side of the air duct 11a are located at least partially outside the air duct 11a.
  • only the headers 5,6 of the modules 10,10' of the condenser located in correspondence to the same side (e.g., of the same lateral wall 117) of the air duct 11a are positioned at least partially outside the air duct 11a.
  • only the headers of the modules of the evaporator located in correspondence to the same side of the air duct 11a are located at least partially outside the air duct 11.
  • all headers 5,5a,6 of all modules 10,10' of all heat exchangers 31,32 are located outside the air duct 11a, at least partially.
  • a slot 115 is preferably realized in the air duct itself in order to allow for the header to protrude.
  • the slot is realized in correspondence of the lateral wall 117. More preferably, in the air duct 11a, a number of slots 115 equal to the number of headers 5,6 located outside the duct is formed. Slot 115 can be cut in the upper or in the lower portion 111,112 of air duct, or in correspondence to both, depending on the design of these two portions.
  • a sealing element such as gasket or sponge material, is located in correspondence of each gap present between the protruding header 5,6,5a and the wall 117 to close the same (not visible in the figures).
  • Locating one or more of the headers 5,6 of modules 10,10' outside the air duct 11a means that, in the direction of the longitudinal extension of the layers X, inside the air duct, a length equal to the diameter of the header (or a length smaller than the diameter if only a fraction of the header is located outside) in that direction is "free", compared to a dryer in which a header having the same diameter is completely located inside the air duct 11a.
  • a volume of air duct 11a having a width equal to the diameter of the header along the X direction, a length equal to the length of the whole air duct and a height equal to the height of the air duct becomes usable in a different way.
  • the width of the air duct 11a can be made narrower with respect to the air duct of the comparison dryer.
  • This is the solution chosen comparing figs. 8a and 8b.
  • the heat exchange capacity remains the same, due to the fact that the same extension of heat exchanging surface is present in the comparison and the invention dryer: the same channels and fins having the same length are present inside the air duct 11a of dryer l CO mparison and invention dryer 1.
  • the air duct 11a narrower in the dryer of the invention 1 than in the comparison dryer l CO mparison, more volume is available for the other elements and devices which have to be located inside the dryer.
  • the process air stream is exchanging heat with the refrigerant flowing into the modules 10.
  • the surface in which heat exchange takes place is substantially the same with the headers 5(6) located outside or inside the air duct 11.
  • the dryer 1 of the invention keeps an air duct 11 having the same width as the comparison duct of dryer l CO mparison- In this way, the heat exchange capacity of the dryer of the invention is increased: the length of the channels and thus of the heat exchange layers is longer than in the comparison dryer, so there is a broader heat exchanging surface, being a "segment" of air duct 11a equal to the diameter of the header header-free and thus it can be occupied by longer heat exchange layers.
  • the cross section of the header 5,6 located inside or outside the air duct 11a is not relevant for this aspect of the invention, any header having any type of cross section can be located outside the air duct 11.
  • any header having any type of cross section can be located outside the air duct 11.
  • placing the header outside the air duct allows to recover less space than in case of a circular header, for example, however the reasoning above still apply.
  • the space outside the air duct 11a occupied by the header is minimized, due to the small volume occupied by an oblong header.
  • the type of module 10,10' used in the heat exchangers 32,31 of figs. 7b and 8b is the one depicted with reference to the embodiment of fig. 5a,5b, thus the inlet and the outlet headers 5,6 are vertically stacked one on top of the other in the same stacking direction as the heat exchange layers 8.
  • the inlet header 5 is located outside the air duct 11a, automatically in this embodiment also the outlet header 6 is located outside as well, and vice versa.
  • intermediate header 5a can be located outside air duct 11a.
  • the modules 10,10' of the first and of the second heat exchanger 32,31 are shown substantially parallel to each other, in other words the longitudinal extension X of a heat exchange layer of a module is substantially parallel to the longitudinal extension X of a heat exchange layer of another module.
  • the heat exchange layers 8 of all modules 10 are all extending all along the same X direction which is substantially perpendicular to the longitudinal extension Y of the air duct 11a. This configuration is preferred when the process air stream flowing within the air duct is substantially perpendicular to the X direction. However, this is not always the case, for example, due to the path that the process air has to follow from the drying chamber to the air duct, it may enter the latter at a given angle. In this case, having substantially parallel modules may not be the optimal configuration.
  • the process air enters the duct 11 at a given angle.
  • the modules 10,10' belonging to the first and the second heat exchanger 32, 31, or to the same first or second heat exchanger when the latter includes more than one module, are arranged in such a way that they are inclined towards each other, in other words, the longitudinal extensions of the heat exchange layers 8 of the modules 10,10' are not parallel to each other, but form an angle which is different from 0° (and ⁇ multiples thereof).
  • the modules 10,10' "follow" the path of the process air stream inside the air duct 11a, so that the process air always "hits" the module perpendicularly to the stackwise direction.
  • the modules are inclined with respect to each other and also in respect of the longitudinal extension of the air duct, allowing the use of longer module 10, 10' than in the embodiment in which the modules 10,10' are arranged perpendicular to the longitudinal extension of the air duct 11a.
  • an additional heat exchange takes place between the refrigerant flowing within one of the header 5,6 located outside the air duct 11 and an additional fluid, different from the process air.
  • the additional fluid may flow in an additional circuit, which does not need to be confined, e.g., a circuit simply indicates a direction of forced flow of the fluid.
  • the casing and/or basement of the dryer defines a conduit for the flow of such an additional fluid by walls or elements positioned in the same.
  • the header wherein the additional heat exchange takes place is the outlet header 6 of the condenser 31, before the refrigerant enters the expansion device 34. Cooling the refrigerant present within, or at the exit of, the header further decreases the temperature of the refrigerant, increasing the performances of the heat pump.
  • the additional fluid can be air, moved by a first fan 51.
  • the additional fluid is air coming from the outside of the casing 2.
  • the additional fluid is air already present within casing 2.
  • the first solution is preferred, being the external, ambient, air generally cooler than the air already present in the casing.
  • the first fan 51 is a dedicated fan mounted in the basement 24 and directed towards the header 6.
  • the dimensions of the fan 51 are such that the whole outlet header 6 is subjected to a flow of additional air blown by the fan.
  • a fan of the compressor (not shown) can be used to both cool down the compressor itself and the header 6.
  • inlet and outlet header 5,6, of the first heat exchanger are separated one from the other, but rather close in spatial distance. Therefore, care should be taken not to blow the additional fluid towards the inlet header 5 so that the refrigerant entering the condenser 31 is cooled, decreasing the performances of the heat pump.
  • the inlet header 5 can be either insulated or a fluid deflector (not shown) can be placed in front of the same, so that the additional fluid is diverted away before it hits the inlet header of the condenser 31.
  • the outer header 6 of the condenser's module is located on top of the inlet header 5 (alternatively, in another non-depicted embodiment, the inlet header can be located on top of the outer header).
  • the inlet header can be either insulated, for example by applying caulking, or a fluid deflector (not shown) can be placed in front of the same, so that the additional fluid is diverted away before it hits the inlet header.
  • an even further heat exchange takes place between the refrigerant flowing within or exiting the outer header 6 of module 10 of evaporator 32.
  • the heat exchange takes place between a further additional fluid and the refrigerant.
  • the further additional fluid can for example be air, moved by a second fan 51a. More preferably, the further additional fluid is air coming from the outside of the casing 2. Alternatively, the further additional fluid is air already present within casing 2.
  • the fan 51a is a dedicated fan mounted in the basement 24 and directed towards the header 6.
  • the dimensions of the fan 51a are such that the whole outlet header 6 is subjected to a flow of additional air blown by the fan.
  • the characteristics of this second fan 51a are preferably those already outlined with respect to the first fan 51.
  • the second fan 51a is preferably put into operation, i.e., it forces air towards the outlet header 6 of evaporator's 32 module 10, when the heat pump system is in the warming-up phase. Indeed, when the heat pump 30 is switched on, there is an initial phase in which the refrigerant has to be heated in the evaporator 32 in order to evaporate before entering into the compressor. A complete evaporation of the refrigerant avoids or at least minimizes the risk of droplets of refrigerant entering in the compressor and also speeds up the warming-up phase.
  • the second fan 51a blows air, which is at least at room temperature if not at higher temperature due to the heat releasing elements located in the casing (e.g., engine, heat pump, etc.), onto the header 6 at the outlet of refrigerant from the evaporator 32, before the refrigerant enters in the compressor, so that the blown air warms up the refrigerant.
  • the heat releasing elements located in the casing e.g., engine, heat pump, etc.
  • the second fan 51a is switched off.
  • the second fan 51a is also used to prevent over-heating of the evaporator 32.
  • the evaporator's module 10 can have the same configuration shown in fig. 9b, where the outer header 6 of the evaporator's module 10 is located on top of the inlet header 5 (alternatively, in another non-depicted embodiment, the inlet header can be located on top of the outer header). It is preferable to avoid directing the flow of the further additional fluid also towards the inlet header 5 of the evaporator's module.
  • the inlet header can be either insulated, for example by applying caulking, or a fluid deflector (not shown) can be placed in front of the same, so that the further additional fluid is diverted away before it hits the inlet header.
  • first and/or second fan 51, 51a are regulated depending on measurements obtained via respective temperature sensors (not depicted in the drawings).
  • a first temperature sensor is associated to the first fan 51, the temperature sensor being apt to measure the temperature of the refrigerant at or in proximity of the outlet header 6 of condenser 31, before the refrigerant enters the expansion device 34.
  • a first temperature threshold is set, so that, if the temperature sensor detects a temperature higher than such first threshold, the first fan 51 is put into rotation and air is blown towards the outlet header 6 of the condenser's module. In case the temperature decreases below the same or below a second temperature threshold, then the fan is stopped.
  • the first fan 51 can include a variable speed motor, so that, if the temperature sensor detects a temperature higher than the first threshold, the first fan 51 is put into high speed rotation, while a low speed rotation is kept otherwise.
  • the second fan 51a can be controlled in cooperation with a second temperature sensor checking the temperature of the refrigerant within or exiting the outlet header of the evaporator 32 upstream of the compressor 33.
  • the second fan 51a can be controlled in an on/off manner, for example - in order to avoid overheating - the second fan can be put into operation when the temperature of the refrigerant is above a third threshold, and stopped otherwise.
  • the second fan 51a is operated when the temperature of the refrigerant is below a fourth threshold, and it is stopped when the temperature of the refrigerant, measured by the second temperature sensor, is high enough.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Detail Structures Of Washing Machines And Dryers (AREA)

Abstract

La présente invention concerne un sèche-linge (1) comprenant un carter (2) soutenant une chambre de séchage (3) pour recevoir une charge à sécher ; un conduit d'air de processus (11) en communication avec la chambre de séchage (3) où un courant d'air de processus est disposé à circuler et incluant un conduit d'air ; et une pompe à chaleur (30) ayant un circuit de pompe à chaleur dans lequel un fluide frigorigène (R) peut circuler, ledit circuit de pompe à chaleur incluant un premier échangeur de chaleur (31) où le fluide frigorigène est refroidi et le flux d'air de processus est chauffé, et un second échangeur de chaleur (32) où le fluide frigorigène est chauffé et l'air de processus est refroidi. Le premier et/ou le second échangeur de chaleur le deuxième sont thermiquement couplés à la conduite d'air de processus (11) pour procéder à un échange de chaleur entre ledit fluide frigorigène dans ledit circuit de pompe à chaleur et ledit courant d'air de processus et le premier et/ou le deuxième échangeur thermique (31; 32) comprennent en outre un module échangeur de chaleur (10; 10'). Le module inclut un en-tête d'entrée (5;5') pour diriger un flux dudit fluide frigorigène dans ledit module ; un en-tête externe (6;6') pour rejeter ledit fluide frigorigène dudit module ; et une pluralité de couches d'échangeur de chaleur (8,8') reliant avec fluidité ladite entrée (5;5') audit en-tête de sortie (6;6') pour permettre au fluide frigorigène (R) de circuler par ladite entrée vers ledit en-tête de sortie et/ou inversement ; lesdites couches (8,8') étant empilées les unes sur les autres et chaque couche comprenant une pluralité de canaux. En outre, ladite pluralité de couches d'échangeur de chaleur (8;8') est organisée au moins partiellement disposées à l'intérieur dudit conduit d'air et que l'en-tête d'entrée et/ou de l'en-tête de sortie dudit module se trouve au moins partiellement à l'extérieur dudit conduit d'air.
PCT/EP2013/063160 2013-06-24 2013-06-24 Sèche-linge à pompe à chaleur Ceased WO2014206441A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
CN201380077712.7A CN105324529B (zh) 2013-06-24 2013-06-24 热泵式衣物干燥机
AU2013396776A AU2013396776B2 (en) 2013-06-24 2013-06-24 Heat pump laundry dryer
EP13734686.2A EP3014011B1 (fr) 2013-06-24 2013-06-24 Sèche-linge à pompe à chaleur
PCT/EP2013/063160 WO2014206441A1 (fr) 2013-06-24 2013-06-24 Sèche-linge à pompe à chaleur

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP2013/063160 WO2014206441A1 (fr) 2013-06-24 2013-06-24 Sèche-linge à pompe à chaleur

Publications (1)

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WO2014206441A1 true WO2014206441A1 (fr) 2014-12-31

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PCT/EP2013/063160 Ceased WO2014206441A1 (fr) 2013-06-24 2013-06-24 Sèche-linge à pompe à chaleur

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EP (1) EP3014011B1 (fr)
CN (1) CN105324529B (fr)
AU (1) AU2013396776B2 (fr)
WO (1) WO2014206441A1 (fr)

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KR20160116465A (ko) * 2015-03-30 2016-10-10 엘지전자 주식회사 세탁물처리장치
JP2016209446A (ja) * 2015-05-13 2016-12-15 東芝ライフスタイル株式会社 衣類乾燥機
CN110331566A (zh) * 2015-01-30 2019-10-15 杭州三花研究院有限公司 烘干系统及其使用方法
JP2020039964A (ja) * 2019-12-19 2020-03-19 東芝ライフスタイル株式会社 洗濯乾燥機
US12092402B2 (en) 2019-03-20 2024-09-17 Fujitsu General Limited Heat exchanger

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JP7164287B2 (ja) * 2017-04-13 2022-11-01 東芝ライフスタイル株式会社 衣類乾燥機
WO2020079849A1 (fr) * 2018-10-19 2020-04-23 三菱電機株式会社 Séchoir de salle de bains
AU2018453171B2 (en) * 2018-12-21 2024-12-19 Electrolux Appliances Aktiebolag Laundry dryer
CN115398162B (zh) * 2020-02-27 2024-09-10 江森自控泰科知识产权控股有限责任合伙公司 水箱混合歧管
CN114517397A (zh) * 2022-01-04 2022-05-20 青岛海尔洗衣机有限公司 用于烘干衣物的设备

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EP2468944A1 (fr) * 2010-12-27 2012-06-27 Electrolux Home Products Corporation N.V. Séchoir à linge avec pompe de chaleur pour usage domestique
EP2549008A1 (fr) * 2011-07-22 2013-01-23 Electrolux Home Products Corporation N.V. Agencement de cave dans un appareil de traitement du linge à pompe thermique

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US5048602A (en) * 1989-05-22 1991-09-17 Showa Aluminum Kabushiki Kaisha Heat exchangers
EP1209277A2 (fr) 2000-11-20 2002-05-29 Electrolux Zanussi S.p.A. Sèche-linge avec pompe à chaleur
EP1231448A2 (fr) * 2001-02-07 2002-08-14 Modine Manufacturing Company Echangeur de chaleur
JP2008237390A (ja) * 2007-03-26 2008-10-09 Sanyo Electric Co Ltd 洗濯乾燥機
US20110280736A1 (en) 2010-04-28 2011-11-17 Lee Yongju Control method of dryer
EP2468944A1 (fr) * 2010-12-27 2012-06-27 Electrolux Home Products Corporation N.V. Séchoir à linge avec pompe de chaleur pour usage domestique
EP2549008A1 (fr) * 2011-07-22 2013-01-23 Electrolux Home Products Corporation N.V. Agencement de cave dans un appareil de traitement du linge à pompe thermique

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110331566A (zh) * 2015-01-30 2019-10-15 杭州三花研究院有限公司 烘干系统及其使用方法
KR20160116465A (ko) * 2015-03-30 2016-10-10 엘지전자 주식회사 세탁물처리장치
KR102483087B1 (ko) * 2015-03-30 2022-12-29 엘지전자 주식회사 세탁물처리장치
JP2016209446A (ja) * 2015-05-13 2016-12-15 東芝ライフスタイル株式会社 衣類乾燥機
US12092402B2 (en) 2019-03-20 2024-09-17 Fujitsu General Limited Heat exchanger
JP2020039964A (ja) * 2019-12-19 2020-03-19 東芝ライフスタイル株式会社 洗濯乾燥機

Also Published As

Publication number Publication date
CN105324529A (zh) 2016-02-10
AU2013396776B2 (en) 2018-12-06
EP3014011A1 (fr) 2016-05-04
CN105324529B (zh) 2017-12-26
AU2013396776A1 (en) 2015-12-24
EP3014011B1 (fr) 2018-08-08

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