AU2019213457A1 - Laundry Dryer including a Heat Pump System - Google Patents

Abstract

P-62199/EP Abstract The invention relates to a dryer (1) including o A treating chamber (3) where items are introduced and treated with a process air flow; o a heat pump system (30) having a refrigerant circuit in which a refrigerant can flow, said refrigerant circuit including a first heat exchanger (32) where the refrigerant is heated up, a second heat exchanger (31) where the refrigerant is cooled off, a compressor (33) to pressurize and circulate the refrigerant through the refrigerant circuit, and a pressure lowering device; said first and/or second heat exchanger (32, 31) being apt to perform heat exchange between said refrigerant flowing in said refrigerant circuit and said process air; the refrigerant being a flammable refrigerant; o wherein each of said first and second heat exchanger (32, 31): • is a finned tube heat exchanger comprising a tube (40) having multiple sections (41) one above the other and a plurality of fins (50); • is divided in three portions: a central portion (60) wherein said multiple sections (41) of the tube are in contact with said plurality of fins (50), and a first and second end portions (61, 62) where said tube (40) is not in contact with the plurality of fins (50); o and wherein a ratio between a total external volume (TEV2) of all sections of the tube included in the central portion (60) in contact with the plurality of fins of the second heat exchanger (31) and a total external volume (TEV1) of all sections of the tube included in the central portion (60) in contact with the plurality of fins of the first heat exchanger (32) has a value lower than 0.95. jii )L

Description

LAUNDRY DRYER INCLUDING A HEAT PUMP SYSTEM

Technical field

The present invention relates to a laundry dryer including a heat pump system, wherein the refrigerant of the heat pump circuit includes a flammable refrigerant.

Background of the invention

The heat pump technology in a laundry dryer is at present the most efficient way to dry clothes in terms of energy consumption. In a heat pump system of the laundry dryer, a process air stream flows in a closed process air stream circuit. Further, the heat pump system includes a closed refrigerant circuit. The process air stream is moved by a main fan, passes through a laundry chamber, which is preferably formed as a rotatable laundry drum, and removes there water from wet clothes. Then, the process air stream is cooled down and dehumidified in an evaporator, heated up in a condenser and re-inserted into the laundry drum again.

The refrigerant is compressed by a compressor, condensed in the condenser, expanded in an expansion device and then vaporized in the evaporator.

Thus, the condenser and the evaporator are components of the process air stream circuit as well as of the refrigerant circuit. The condenser and the evaporator are heat exchangers between the process air stream circuit and the refrigerant circuit.

Usually, the components of the heat pump system are placed in a basement of the laundry dryer. The basement of a laundry dryer is part of a casing, which includes in addition to the basement also walls, substantially vertically supported from the basement, such as for instance a front wall and a rear wall, and lateral walls. In the casing, a drum, where the laundry is introduced in order to dry the same, is rotatably supported. In particular, the compressor, the evaporator and the condenser are arranged in said basement below the laundry drum.

Typical refrigerants used in heat pumps are Hydroflorocarbons (HFCs), such as, for example, R134a and R407C. However, the use of these refrigerants can adversely impact on global warming, as they have a high Global Warming Potential (GWP), which is a relative measure of the amount of heat trapped in the atmosphere by such

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2019213457 12 Aug 2019 refrigerants (in gas form), compared to the amount of heat trapped in the atmosphere by a similar mass of carbon dioxide.

Especially in the last years, the global warming problem has become increasingly severe, and alternative refrigerants have thus been extensively studied and employed.

As also disclosed by document EP 3 066 406 B1, hydrocarbon refrigerants, such as for example propane (R-290) and propylene (R-1270), proved to be a good alternative for replacing the above high-GWP refrigerants in heat pump dryers and washer-dryers appliances. These natural fluids have ideal thermal and physical properties, besides having a negligible GWP. However, since these alternative refrigerants are flammable and explosive, the existing regulations currently limit the maximum charge of refrigerant in laundry, so as to prevent possible issues due to leakages in the refrigerant circuit.

Summary of the invention

The Applicant has thus realized that, in addition to the choice of refrigerant, also the design of the heat exchangers, i.e. namely of the evaporator and the condenser, can severely affect energy consumption, drying efficiency and time performances. A proper configuration of the heat exchanger(s) allows achieving several benefits, such as maximizing the heat exchange between the refrigerant and the process air, reducing the pressure drop both in the refrigerant and in the process air circuit, and reducing the amount of refrigerant needed for a proper functioning of the heat pump. All these benefits allow saving energy, improve the drying efficiency and, in general, together with the choice of a refrigerant having a low GWP, allow the realization of a more “ecofriendly” dryer.

Therefore, it is an object of the present invention to provide a laundry dryer with a heat pump system having an improved design, aimed at maximizing the fraction of refrigerant charge effectively involved in the heat exchange.

Another object of the present invention is to provide a laundry dryer with a heat pump system, which allows good performance in terms of efficiency having at the same time a negligible impact on global warming.

According to an aspect, the invention relates to a dryer including:

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2019213457 12 Aug 2019 o A treating chamber where items are introduced and treated with a process air flow;

o a heat pump system having a refrigerant circuit in which a refrigerant can flow, said refrigerant circuit including a first heat exchanger where the refrigerant is heated up, a second heat exchanger where the refrigerant is cooled off, a compressor to pressurize and circulate the refrigerant through the refrigerant circuit, and a pressure-lowering device; said first and/or second heat exchanger being apt to perform heat exchange between said refrigerant flowing in said refrigerant circuit and said process air; the refrigerant being a flammable refrigerant;

o wherein each of said first and second heat exchanger:

is a finned tube heat exchanger comprising a tube having multiple sections one above the other and a plurality of fins;

is divided in three portions: a central portion wherein said multiple sections of the tube are in contact with said fins, and a first and second end portions where said tube is not in contact with the fins;

o and wherein a ratio between a total external volume of all sections of the tube included in the central portion in contact with the plurality of fins of the second heat exchanger and a total external volume of all sections of the tube included in the central portion in contact with the plurality of fins of the first heat exchanger has a value lower than 0.95.

In the following, with the term “dryer” both drying machines which dry only as well as combined washer-dryers are meant. In particular, also washer-dryers that wash the laundry, spin/centrifuge it and finally tumble dry it.

The dryer includes a “treating chamber”, such as a washing and/or drying chamber (commonly called drum) where the laundry can be located in order to be washed and/or dried; the chamber can be rotated around a chamber axis during the washing and/or drying operations. Further, the dryer may be a front-loading dryer, which means

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2019213457 12 Aug 2019 that the axis of rotation of the treating chamber is positioned in a horizontal manner or slightly tilted with respect to a horizontal plane, or a top laundry dryer, where the axis of the treating chamber is substantially vertical.

In a preferred embodiment, the dryer is a front loading laundry dryer.

The dryer preferably comprises a casing preferably including a front wall, a rear wall, side walls, top wall and a base section or basement. The front or top wall may comprise a user panel to command the functioning of the dryer by the user. The casing defines the limit between the internal volume of the dryer and the outside to the dryer. Further, preferably, the casing includes a door hinged to the casing itself, e.g. to the front wall in case of a front loading dryer, which is openable in order to introduce the laundry in the laundry chamber, or to the top wall in case of a top loading dryer.

The basement has, among others, the function of housing several component of the dryer, such as a portion of a drying air conduit, heat exchangers, a motor for rotating the chamber, a fan, etc. Further, it has also the function of supporting some of the walls of the casing.

The basement can be realized in any material; preferably it is realized in plastic material. Further, the walls of the casing can also be realized in any material.

The basement is generally positioned on a floor and where it rests when the machine is in a standard operating condition.

The basement for example may be divided in an upper and a lower shell. The upper and lower shells define the outer boundaries of the basement, dividing a volume “inside” of the basement and an “outside” to the basement.

In a heat pump dryer, the treating chamber is part of a process air circuit, in particular for example a closed-loop air circuit in case of a condensed dryer or an open air circuit in case of a vented dryer, which in both cases includes an air duct for channelling a stream of air to dry the load. The process air circuit is connected with its two opposite ends to the treating chamber. Hot dehumidified air is fed into the treating 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 the 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 appliance in the

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2019213457 12 Aug 2019 ambient where the latter is located or it continues in the closed-loop circuit. In this second case, 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. Alternatively, 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. Different circuits are known in the art in case of a washer-dryer.

The heat pump of the dryer includes a refrigerant circuit in which a refrigerant can flow and which connects via piping a first heat exchanger or evaporator, a second heat exchanger or condenser, a compressor and a pressure-lowering device. The refrigerant is pressurized and circulated through the system by the compressor. On the discharge side of the compressor, the hot and highly pressurized vapor is cooled in 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 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.

In order to compress the refrigerant, the compressor includes an electric motor which is commonly powered by a current, for example a current coming from the mains.

In order to exchange heat with the process air, the first and second heat exchangers are positioned inside the process air circuit. The process air circuit defines a bottom portion or a bottom part. The second heat exchanger is in abutment to the bottom part or portion of the process air circuit. In the following, a “horizontal plane”, which is used as a reference plane, is defined as follows. The second heat exchanger touches at least in three points the bottom part of the process air conduit. These three points defines a plane and this plane is a horizontal plane for the reference system of the present description. If there are more than three points of abutment between the second heat exchanger and the bottom part/portion of the process air conduit, then the horizontal plane is the plane that includes the majority of the points of connection.

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This plane is generally really “horizontal” in the general meaning, that is, it is parallel to the floor where the dryer is put, which is commonly accepted to be “horizontal”. However, there are situations in which the above-defined plane is not horizontal in the common meaning of the term, for example it is tilted (i.e. it forms an angle) with the floor where the dryer is positioned. This can happen for example because the floor is not flat and the dryer had to be adjusted, for example using standard provided “heightadjustable legs”, to be stable on an uneven floor. Alternatively, the heat exchanger can be indeed positioned tilted with respect to the floor.

Preferably, the first and/or second heat exchanger is located in the basement of the dryer.

In the present invention, the refrigerant used in the heat pump circuit is a flammable refrigerant and preferably a hydrocarbon refrigerant. Although for flammable refrigerant a maximum charge limit is set by current regulations, these refrigerants have ideal thermal and physical properties for use in heat exchangers and, most importantly, they have low GWPs, which means a negligible impact on global warming.

The first and second heat exchanger of the invention are finned tube heat exchangers comprising a tube having multiple sections one above the other and a plurality of fins. A total length of said first and second heat exchanger is defined along a length direction. The total length of the first heat exchanger can be equal to that of the second heat exchanger or different.

Finned tube heat exchangers are the most commonly used type of heat exchangers to transfer heat between a fluid (the refrigerant that flows inside the tube) and the air (the drying process air that flows through the fins and outside the tubes).

Such heat exchangers typically comprise a continuous bent tube having straight portions connected by U-bend sections, along which straight portions fins are transversally mounted. The fins are provided with holes, or apertures, having proper shape and size to allow to be assembled transversally along the continuous bent tube. Moreover, the fins are suitably designed so that a contact with proper interference is ensured between the tube and the holes of the fins. The contact between tube’s portions and fins can be random and/or sporadic, due to mounting process that may alter mechanical tolerances and relative positioning of the tube and fins mounted thereon.

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Alternatively, such heat exchangers may comprise individual straight tubes inserted in circular holes or apertures of transversal fins, such tubes being then expanded to provide a proper contact with interference between the tubes and the circular holes of the fins. Ends of the straight tubes are then connected in pairs by means of short Elbend sections, in order to ensure the continuity of the refrigerant circuit. The U-bend sections are typically welded or soldered to the straight tubes.

In any case, there is a plurality of tube sections, all part either of the same tube or of different separated tubes. For simplicity, the singular “tube” is used in the following to indicate both a continuous bent tube and an assembly of tubes, the latter comprising multiple straight tubes stacked one above substantially parallel to one another, and connected at their ends by suitable connecting sections, such as the aforementioned U-bend sections welded or soldered to the ends of the straight tubes.

Preferably, these tube sections are all parallel to each other. These tube’s sections may correspond to the portions of the tube which are “straight”, that is extending substantially along a single direction without bends or curves. Preferably, these tube’s sections are horizontal, that is, they are parallel to the horizontal plane.

In both the above constructions, such finned tube heat exchangers generally comprise a central portion, for example corresponding substantially to the length of the straight tubes’ sections. This central part is that part across which process air flows and where therefore heat exchange takes place between the refrigerant flowing in the tubes’ sections and the process air. Further, the finned tube exchangers include lateral portions, on the two opposite sides of the central portion, comprising U-bend tube sections connecting the straight tube portions and not involved in the heat exchange (or minimally involved in it), as process air is not made to flow therethrough or only minimally.

Although such lateral portions are not useful in terms of heat exchange, they are necessary for construction reasons, as the straight tube’s sections of the central portion have to be connected to ensure continuity of the refrigerant circuit.

The minimum length of the lateral portions depends on the minimum bending radius of the tubes, which in turns depends on size and flexibility of the material of the tube(s), and on the space needed for welding or soldering the U-bend sections when multiple individual straight tubes are used. According to the standard technology, for heat

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2019213457 12 Aug 2019 exchangers the length of the lateral portions (sum of the two lengths) is between 40 and 60 mm. This length is taken along a length direction, which is better defined below. In use, the whole heat exchanger is filled with refrigerant. Therefore, a fraction of refrigerant not involved in the heat exchange, namely the fraction of refrigerant flowing in the lateral portions, must be taken into account when finned tube heat exchangers are involved. This is of particular concern when flammable and explosive refrigerants such as the aforementioned hydrocarbons are used, due to their limited maximum charge. This maximum charge might for example be fixed in regulations.

This maximum charge limit can in turn affect the drying performances of the laundry dryer, as the best performances of a conventional laundry dryer are typically observed for higher values of refrigerant charge.

The reference above defined horizontal plane allows defining two orthogonal directions: a length direction and a thickness direction. These two directions are both horizontal directions, that is, they are parallel to the horizontal plane, and forms an angle of substantially 90° among each other.

In the following, by “length direction”, a horizontal direction substantially parallel to a plane containing at least two of the multiple tube sections stacked one above the other is meant to be indicated. This plane is preferably a vertical plane, that is, a plane perpendicular to the horizontal plane. In the following, thus, “length” means a measure taken along the length direction.

The first and the second heat exchanger of the invention are divided in three portions: a central portion wherein said multiple sections of the tube are in contact with said fins, and a first and second end portions where said tube is not in contact with the fins.

Further, an external volume of all sections of the tube included in the central portion (in short, total external volume or TEV) in contact with the fins of the first or of the second heat exchanger can be defined as well.

TEV = TT*(De/2)^A2*Nt*Le where Nt= number of sections,

Le= length of the tubes’ sections in the central area,

De= external diameter of the tubes’ sections.

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In case the diameters is not the same for all tubes or sections, then there is a sum of the various volumes given by tube’s sections having different diameters. The same applies in case the length is not the same for all tube’s sections.

Preferably, the external diameter De is comprised between 4 mm and 10 mm.

The length of the tube’s section is calculated as the length along their extension direction. Generally, the tube’s sections are straight thus their length is equal to the extension of the tube from one end to the other. This can correspond to the length of the central portion along the length direction if the tube’s sections are substantially horizontal (if the tube’s sections extend horizontally).

The volume above is calculated in that way in case the tube’s sections have a circular cross section. If the tube’s sections are not circular, then the volume is

TEV = (cross section of the tube section)*Nt*Le

Preferably, the number of sections is comprised between 20 and 70.

Preferably, the length of the sections Le is comprised between 200 mm and 450 mm, more preferably between 200 mm and 300 mm. Preferably the length of the tube’s sections (length of the tube in the central portion) is equal to: Le > 280 mm, preferably Le > 300 mm, more preferably Le > 320 mm, even more preferably Le > 350 mm.

Preferably the thickness of the tube (that is, the thickness external wall of the tube) is comprised between 0.2 mm and 0.8 mm.

This TEV can be defined in the same manner for both the evaporator (called TEV1) and the condenser (TEV2). According to the present invention, the ratio TEV2/TEV1 is < 0.95. Preferably TEV2/TEV1 < 0.9, more preferably TEV2/TEV1 < 0.85, even more preferably TEV2/TEV1 < 0.7. However, preferably TEV2/TEV1 > 0.5.

Inside the heat pump circuit, when the compressor is switched ON, the majority of refrigerant charge is located within the condenser because in this heat exchanger refrigerant is at high pressure and, for a portion of it in its liquid state, with a high density level compared to the vapour phase present in the evaporator.

The evaporator instead works at low pressure and therein the refrigerant is in a liquid vapour mixture, superheated vapour being in a relevant portion of the heat exchanger, therefore its density level is low.

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Considering the charge limit for flammable refrigerant, it is important to limit the volume occupied by the refrigerant within the heat exchangers, especially within the condenser.

Possible solutions for reducing the volume occupied by the refrigerant within the heat exchangers are, for example, the following. A first solution is to reduce the number of tube’s sections present in the heat exchanger. Alternatively, the length of the tube’s sections can be reduced. As a third possibility, the inner diameter of the tube’s sections can be reduced.

Such solutions are effective in reducing the volume that can be used by the refrigerant, however they may penalize the performance of the heat pump because there is insufficient heat exchange.

For instance, the reduction of tube diameter, either external or internal, reduces the internal volume of the tubes, which is desired, but it also reduces the surface of the pipe’s sections which comes into contact with the process air and thus provides for the heat exchange. This can be compensated by adding more fins, but the efficiency of heat exchange between the refrigerant and the fins is lower than the efficiency of heat exchange with the tube’s portion. Inner and external diameter of the tubes are connected to each other: tubes in standard heat exchangers normally have “standard” thicknesses, constant and dependent on the material in which the tube is formed.

In standard dryers, in addition, process air exiting the drum is filtered before entering into the evaporator. The process air may include fluff and/or otherwise undesired material which has been unintentionally removed from the laundry during the drying. In order to filter this air to remove the undesired material, a filter is generally positioned before the evaporator. More than one filter can be used as well. These filters however cannot remove all the undesired material from the process air and it is not uncommon that some fluff may remain in the process air flow. For this reason, too many fins may increase air pressure drops, and the space between fins especially at the evaporator cannot be reduced too much because of risks of clogging due to the fluff not trapped by the air filter.

A trade-off between design constraints due to charge limitation and good heat exchange is therefore desirable.

io

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Due to the ratio defined in the invention, therefore, the condenser has a total volume smaller than the evaporator, thus the “more refrigerant consuming” heat exchanger is smaller and this takes care of the refrigerant small charge. At the same time, such ratio allows still a proper heat exchange between the air and the refrigerant.

Preferably, the total external volume of all sections of the tube included in the central portion of the second heat exchanger is comprised from 200 cc and 600 cc.

Preferably, the total external volume of all sections of the tube included in the central portion of the first heat exchanger is comprised from 250 cc and 600 cc.

Tests have shown that for a dryer these are the preferred dimensions of the heat exchangers for an optimal heat exchange efficiency when an inflammable refrigerant is used.

Preferably, said first and/or second heat exchanger is a coil heat exchanger and wherein the tube in said end portions includes bends. In this embodiment, the end portions are particularly shaped as U-bend tube sections.

Preferably, said tube of said first and/or second heat exchanger has an external diameter comprised between 4 mm and 10 mm. More preferably, it is comprised between 5 mm and 8 mm. The upper value of such size interval is advantageously selected to limit the inner volume of the tubes of the second heat exchanger so that, for a same amount of refrigerant, a higher density of refrigerant circulating within the tubes is obtained, which in turns increases the cooling capacity of the second heat exchanger and reduces the occurrence of pressure losses when low charges of refrigerator are involved. The lower limit, on the other end, is provided to ensure a minimum acceptable cooling capacity of the heat exchanger. The inner volume of the tube refers to the following. The volume in issue is only the volume included in the central portion of the second heat exchanger (i.e. the sum of the inner volumes of all portions of tube included in the central portion of the second heat exchanger). The inner volume can be measured as:

Inner volume = TEV - volume occupied by the external wall of the tube

Preferably, the thickness of the tube (that is, the thickness external wall of the tube) is comprised between 0.2 mm and 0.8 mm.

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Preferably, the dryer comprises a process air circuit including said treating chamber, and a basement where said heat pump is located, the process air circuit including a basement portion comprising a process air conduit where the first and second heat exchangers are positioned, wherein said central portion of said first and/or second heat exchanger is completely contained in said basement process air conduit. The whole central portion of the condenser is thus used for heat exchange, using the maximum available heat exchange surface.

Preferably, said flammable refrigerant includes propane or propylene. Propane and propylene are highly efficient natural refrigerants with the lowest levels of harmful emissions.

Preferably, said first and/or second heat exchanger defines a total length along a length direction, said end portions being at the opposite side of the central portion along said length direction, said length direction being substantially perpendicular to a main direction of flow of said process air when passing through said first and/or second heat exchanger. In this embodiment, the first and/or second heat exchanger has therefore a so-called “cross-flow configuration”, particularly suitable for low-pressure applications such as laundry dryers, and in general when a large volume flow of vapor is involved and a low-pressure drop is required. Moreover, this configuration allows a reduced size of the heat exchanger.

Preferably, the first and/or second heat exchanger defines a thickness along a thickness direction, and wherein the thickness is comprised between 40 mm and 150 mm. After a certain thickness, there are no significant improvement in the overall efficiency of the heat pump, because pressure drops become significative. Therefore, the selected range is a compromise between a “small” heat exchanger so that little refrigerant is used, and a good heat exchange.

Preferably, said first and/or second heat exchanger defines a total length along a length direction, said end portions being at the opposite side of the central portion along said length direction, the total length being smaller than 550 mm. The total length Lt is the sum of the central length Le plus the two lateral lengths Lc. Dryers have commonly standard accepted dimensions to be respected and this maximum length is optimal to use all the available space. For example, standard maximum dimensions

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2019213457 12 Aug 2019 of a dryer are in Europe 60 cm x 60 cm (length x thickness), while commonly the basement of the dryer is few cm smaller.

Preferably, said basement comprises an upper and a lower shell, said basement process air conduit being formed by said upper and lower shells. An easy assembly of the machine is obtained.

Preferably, the high pressure of the refrigerant in the stable phase of the heat pump cycle is comprised between 19 bar and 38 bar.

Preferably, the low pressure of the refrigerant in the stable phase of the heat pump cycle is comprised between 7 bar and 17 bar.

In addiction the bigger the exchange area of the condenser, the lower the condensation pressure of the refrigerant. Therefore increasing the dimensions of the condenser it is possible to obtain the same airflow at the same temperature at the outlet of the condenser with a lower condensation pressure of the refrigerant. This is useful for improving performances.

The pressure mentioned is measured in this way:

Low pressure of the refrigerant is measured at the inlet of the compressor, between the evaporator and the compressor, when the cycle of the heat pump is in the stable state.

High pressure of the refrigerant is measured at the outlet of the compressor, between the compressor and the condenser, when the cycle of the heat pump is in the stable state.

In case of propane as refrigerant fluid:

the high pressure in the stable phase of the cycle is preferably comprised between 19 and 32 bar, preferable from 21 to 29 bar.

The low pressure in the stable phase of the cycle is preferably comprised between 7 and 14 bar, preferable from 9 to 12 bar.

In case of propylene as refrigerant fluid:

The high pressure in the stable phase of the cycle is preferably comprised between 23 and 38 bar, preferable from 25 to 35 bar.

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The low pressure in the stable phase of the cycle is preferably comprised between 8 and 17 bar, preferable from 11 to 15 bar.

The stable phase is defined as follows. The whole heat pump cycle can be divided in a first transient phase and in a stable phase. The first transient phase starts at the beginning of the heat pump cycle and can last up to 60% of the total duration of the cycle, preferably up to 45%, more preferably up to 30% of the total duration of the cycle. In the transient phase, the pressure increases gradually (single pressure measurements can still fluctuate, but the general trend of the pressure is that of an increase). In the stable phase, the pressure is substantially constant (also in this case single measurements fluctuate, but the general trend is a substantially constant value of pressure). The stable phase starts at the end of the transient phase and may continue up to the end of the heat pump cycle. The stable phase satisfies the following conditions during its duration.

First condition is that the stable phase contains the highest pressure of the whole phase.

Second condition relates to its being “constant”. The pressure is measured at a given frequency, therefore, the curve of the pressure during the heat pump cycle includes a plurality of points, one at each sampling time. These pressure values are noted with Xi with i= 1 ....N, where N depends on the length of the cycle.

Within the stable phase of the heat pump cycle, taken an average of all the Xi in the

stable phase, called averaged value Xaver, at least 90% of all points Xi in the stable phase are such that:
	leaver bar
Preferably,	leaver bar
More preferably,	leaver < 2 bar

Defined the stable phase as above, then it is verified whether:

- when it comes to the high pressure (measured at the outlet of the compressor, between the compressor and the condenser)

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2019213457 12 Aug 2019 bar < X_aver < 38 bar,

- when it comes to the low pressure (measured at the inlet of the compressor, between the evaporator and the compressor) bar < Xaver < 17 bar.

Preferably, the amount of inflammable refrigerant contained in said heat pump refrigerant circuit is comprised between 80 g and 300 g. More preferably, the amount of inflammable refrigerant is comprised between 100 g and 250 g. More preferably, the amount is comprised between 120 g and 200 g.

The amount of inflammable refrigerant might be set by regulations, which can also be country-dependent. The amount is relatively “low” to minimize the risk of combustion.

Preferably, said tube is realized in copper, aluminum or a combination of the two. These materials have excellent thermal conductivity, besides having good properties of thermal expansion, resistance to internal pressure, corrosion resistance and fatigue strength. Preferably, the tube is realized in aluminum or one of its alloys. Because of mechanical characteristics of Cu and Al to ensure similar mechanical resistance, the wall thickness of the Al tube is higher than Cu tube. This means that if the external diameter of Cu and Al tube is the same, the internal diameter of Al tube is lower than Cu one. Considering the cost of raw material, there is an economical advantage of using Al tube instead of Cu tube heat exchangers, despite the higher amount of material. A low internal diameter means a low inner volume of heat exchangers and this is particularly helpful in case of flammable refrigerant where the charge quantity is limited.

The inner diameter reduction, keeping same number of pipes’ sections and length of the heat exchangers can be achieved also by reducing the external diameter of the tube, not only with increasing the thickness of the wall. A high external diameter tube however increases the turbulence of the air flowing through the exchanger. This high turbulence increases the heat exchange coefficient of the air improving the heat amount exchanged by the exchanger.

Therefore, given an external diameter, it is better to reduce the overall inner volume using Al pipes.

Preferably, said compressor is a rotary compressor.

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Brief description of the drawings

Further advantages of the present inventien will be better understeed with nen-limiting reference to the appended drawings, where:

- Fig. 1 is a perspective view of a laundry dryer realized according to the present inventien;

- Fig. 2 is a perspective view of the laundry dryer of Fig. 1 with an element of the casing removed for showing some internal components;

- Fig. 3 is a perspective view, in a disassembled configuration, of the basement of the dryer of Fig. 1 or Fig. 2;

- Fig. 4 is a perspective view of the basement of Fig. 3 with all elements contained therein removed;

- Figs. 5 is a top view ef the basement ef Fig. 3;

- Fig. 6 is a perspective view of a heat exchanger, detail of the dryer of figure 3;

- Fig. 7 is a front view of the heat exchanger of figure 6;

- Fig. 8 is a top view ef the heat exchanger of figures 6 and 7;

- Fig. 9 is a side view of the heat exchanger of figures 6 - 8;

- Fig. 10 is a simplified view ef figure 9; and

- Fig. 11 is a graph shewing the high pressure (curve above) and low pressure (curve below) measurements of the pressure ef the refrigerant vs. time in a cycle of the heat pump.

Detailed descriptien ef ene er mere embediments ef the inventien

With initial reference to Figs. 1 and 2, a laundry dryer realized according to the present inventien is globally indicated with 1.

Laundry dryer 1 comprises an euter bex er casing 2, preferably but net necessarily parallelepiped-shaped, and a drying chamber, such as a drum 3, for example having the shape ef a hellew cylinder, for housing the laundry and in general the clothes and garments to be dried. The drum 3 is preferably rotatably fixed te the casing 2, so that

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2019213457 12 Aug 2019 it can rotate around a preferably horizontal axis R (in alternative embodiments, rotation axis may be tilted). Access to the drum 3 is achieved for example via a door 4, preferably hinged to casing 2, which can open and close an opening 4a realized on the cabinet itself.

More in detail, casing 2 generally includes a front wall 20, a rear wall 21 and two lateral walls 25, all mounted on a basement 24. Preferably, the basement 24 is realized in plastic material. Preferably, basement 24 is molded via an injection molding process. Preferably, on the front wall 20, the door 4 is hinged so as to access the drum. The casing, with its walls 20, 21, 25, defines the volume of the laundry dryer 1. Advantageously, basement 24 includes an upper and a lower shell portion 24a, 24b (visible in Figures 3 - 5 detailed below).

The dryer 1, and in particular basement 24 is situated generally on a floor.

Laundry dryer 1 also preferably comprises an electrical motor assembly 50 for rotating, on command, revolving drum 3 along its axis inside cabinet 2. Motor 50 includes a shaft 51 which defines a motor axis of rotation M.

Further, laundry dryer 1 may include an electronic central control unit (not shown) which controls both the electrical motor assembly 50 and other components of the dryer 1 to perform, on command, one of the user-selectable drying cycles preferably stored in the same central control unit. The programs as well other parameters of the laundry dryer 1, or alarm and warning functions can be set and/or visualized in a control panel 11, preferably realized in a top portion of the dryer 1, such as above door

4.

With reference to Figure 2, the rotatable drum 3 includes a mantle, having preferably a substantially cylindrical, tubular body 3c, which is preferably made of metal material and is arranged inside the casing 2 and apt to rotate around the general rotational axis R. The mantle 3c defines a first end 3a and a second end 3b and the drum 3 is so arranged that the first end 3a of the mantle 3c is faced to the laundry loading/unloading opening realized on the front wall 20 of the casing 2 and the door 4, while the second end 3b faces the rear wall 21.

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Drum 3 may be an open drum, i.e. both ends 3a and 3b are opened, or it may include a back wall (not shown in the appended drawings) fixedly connected to the mantle and rotating with the latter.

In order to rotate, support elements for the rotation of the drum are provided as well in the laundry of the invention. Such support elements might include rollers at the front and/or at the back of the drum, as well as or alternatively a drum shaft connected to the rear end of the drum (shaft is not depicted in the appended drawings). In Fig. 2, for example, a roller 10 connected to the basement via a bracket 101a as well as a roller 10 connected to the rear wall 21 via a boss 101 is depicted. Any support element for the rotation of the drum around axis R is encompassed by the present invention.

Dryer 1 additionally includes a process air circuit which comprises the drum 3 and a process air conduit 18, depicted as a plurality of arrows showing the path flow of a process air stream through the dryer 1 (see Figures 3 and 4). In the basement 24, a portion of the process air conduit 18 is formed by the connection of the upper shell 24a and the lower shell 24b. Process air conduit 18 is preferably connected with its opposite ends to the two opposite sides of drum 3, i.e. first and second rear end 3a,3b of mantle 3c. Process air circuit also includes a fan or blower 12 (shown partially in Fig. 5).

The dryer 1 of the invention additionally comprises a heat pump system 30 including a second heat exchanger (called also condenser) 31 and a first heat exchanger (called also evaporator) 32 (see figure 3). Heat pump 30 also includes a refrigerant closed circuit (partly depicted) 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, in correspondence of the evaporator 32, absorbing heat. A compressor 33 receives refrigerant in a gaseous state from the evaporator 32 and supplies the condenser 31, thereby closing the refrigerant cycle. In the following the heat exchangers are named either condenser and evaporator or first and second heat exchanger, respectively. More in detail, the heat pump circuit connects via piping 35 (see Fig. 3) the evaporator 32 via the compressor 33 to the condenser 31. The outlet of condenser 31 is connected to the inlet of the evaporator 32 via an expansion device (not visible), such as a choke, a valve or a capillary tube.

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The refrigerant present in the refrigerant closed circuit of heat pump 30 is in this preferred embodiment propane.

Preferably, in correspondence of evaporator 32, the laundry dryer 1 of the invention may include a condensed-water canister (also not visible) which collects the condensed water produced, when the dryer 1 is in operation, inside evaporator 32 by condensation of the surplus moisture in the process air stream arriving from the drying chamber (i.e. drum) 3. The canister is located at the bottom of the evaporator 32. Preferably, through a connecting pipe and a pump (not shown in the drawings), the collected water is sent in a reservoir located in correspondence of the highest portion of the dryer 1 so as to facilitate a comfortable manual discharge of the water by the user of the dryer 1.

The condenser 31 and the evaporator 32 of the heat pump 30 are located in correspondence of the process air conduit 18 formed in the basement 24 (see Figure 3)In case of a condense-type dryer - as depicted in the appended figures - where the air process circuit is a closed loop circuit, the condenser 31 is located downstream of the evaporator 32. The air exiting the drum 3 enters the conduit 18 and reaches the evaporator 32, which cools down and dehumidifies the process air. The dry cool process air continues to flow through the conduit 18 till it enters the condenser 31, where it is warmed up by the heat pump 30 before re-entering the drum 3.

It is to be understood that in the dryer 1 of the invention, an air heater, such as an electrical heater, can also be present, in addition to the heat pump 30. In this case, heat pump 30 and heater can also work together to speed up the heating process (and thus reducing the drying cycle time). In the latter case, preferably condenser 31 of heat pump 30 is located upstream the heater. Appropriate measures should be provided to avoid the electric heater to fuse plastic components of the dryer 1.

Further, with now reference to Figures 4 and 5, in the basement, the process air conduit 18 includes a duct formed by the upper and the lower shells 24a, 24b, having an inlet 19in from which process air is received from the drum 3 and an outlet 19 to channel process air out of the basement 24. Between inlet 19in and outlet 19, the duct is formed, preferably as two single pieces joined together and belonging to the upper and lower shell 24a, 24b, and including a first and a second portion 28 and 29. In the

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2019213457 12 Aug 2019 first portion 29 of this duct, seats are formed for locating the first and the second heat exchangers 31,32. Preferably, heat exchanger 31,32 are placed one after the other, the second heat exchanger 31 being downstream in the direction of flow of the process air the first heat exchanger 32. Further, the second portion 28 channels the process air exiting from the second heat exchanger 31 towards the basement outlet 19.

In the first portion 29 of the basement 24 thus the heat exchangers, and in particular the condenser 31, are located. The condenser 31 is in contact with the lower shell 24b of the basement 24, which forms a flat portion 29a for the abutment of the condenser. The points of contact between the basement conduit 18 and the condenser define a plane indicated with P in figure 5. Plane P is considered the horizontal plane of reference. In this case, considering the dryer 1 positioned on a flat floor and a flat portion 29a of the basement, the horizontal plane P is parallel to the floor and it is defined by the standard (X,Y) coordinates. However plane P can be tilted with respect to the floor.

Given the P plane, a vertical Z direction can be defined, so that also vertical planes, like plane V of figure 4, can be defined as well, as planes perpendicular to plane P.

In figures 6 - 8 a detailed representation of the heat exchanger 31 or 32 is given. The heat exchanger 31,32 comprises a tube or pipe 40 having an inlet 40a and an outlet 40b and including straight parallel sections, all indicated with 41, and bends, all indicated with 42, connecting the straight parallel sections 41 among each other. The sections 41 are one above the other, that is, some of the sections 41 lie on the same vertical plane. The heat exchanger 31, 32 therefore defines several vertical planes one parallel to the other(s) connecting different groups of sections 41. In the same manner, several sections may lie on the same horizontal plane, i.e. a group of sections lie on a plane parallel to the P plane. The heat exchanger 31, 32 therefore defines several horizontal planes one parallel to the other connecting different groups of sections 41. The distance between two nearest-neighbour sections 41 belonging to the same horizontal plane is called the pitch of the row of sections in the same horizontal plane. The distance between two nearest-neighbour sections belonging to the same vertical plane is called the pitch of the sections in the same vertical plane. This is schematically depicted in figure 10.

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Preferably, pipe or tube 40 is realized in Aluminium. Preferably, its external diameter is comprised between 4 mm and 10 mm.

A system of coordinates can be defined using plane P, wherein the straight sections 41 are extending along the X direction. This direction is also called the “length” direction. The Y direction defines a “thickness” direction.

The bends 42 may be soldered connecting different sections 41 in different planes.

The sections 41 are surrounded by fins 50. The fins 50 are positioned perpendicularly to the straight sections 41, that is, they extend along the Y direction. They also define a pitch, that is, a distance between two nearest-neighbour fins is called the fins’ pitch.

Preferably, a pitch of the fins of the evaporator is comprised between 1.8 mm and 3.3 mm. Preferably, a pitch of the fins of the condenser is comprised between 1.4 mm and

3.3 mm.

Preferably, a pitch of the tubes of the first and/or the second heat exchanger is comprised between 15 mm and 30 mm. Preferably, a pitch of rows of the tubes of the first and/or the second heat exchanger is comprised between 10 mm and 30 mm.

Fins have apertures 51 in order to accommodate the sections 41 of the pipe 40. A view of the apertures is given in the side view of figure 9. The fins 50 then are in contact with the sections 41. There is no need to have a connection between each fin 50 and each section 41.

As shown in detail in figures 6-8, each heat exchanger is therefore divided in three parts: a central part 60 where the fins 50 are present and the tube 40 has the straight portions 41, and two lateral portions 61,62 at the two lateral ends of the central portion 60 free from the fins and including the bends 42.

The central portion 60 has generally the form of a parallelepiped, with a front surface 70 which is generally a vertical surface where the process air impinges and an exit surface 71, also vertical, from where the air exits. These surfaces 70, 71 are preferably perpendicular to the main flow of process air (see for example figure 10). The surfaces 70, 71 are preferably rectangular.

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As visible in figure 3, only the central portion 60 is located inside the process air conduit formed in the basement 24, and more precisely in its portion 29. The lateral portions

61,62 are external to the conduit and are only marginally invested by the process air.

In the frame of reference defined, the total length of the condenser 31, which is the total length of the condenser 31 along the length or X direction, is called Lt. This length is equal to the length of the central portion (which is generally equal to the length of each section 41) Le plus the lengths of the two lateral portions Lc. Assuming that the lengths of the two lateral portions are identical, then

Lt =Le + 2 x Lc

For the condenser 31 and the evaporator, preferably Lt < 550 mm.

Further, in the Y direction, the heat exchangers 31,32 defines a thickness t, which is substantially the extension of the fins 50 (assuming that all fins have the same extension) along the Y direction.

For the condenser and the evaporator, preferably 40 mm < t < 150 mm.

For both condenser and evaporator, the external volume of the central portion 60 can be calculated. This external volume is called TEV1 for the evaporator and TEV2 for the condenser. In the present embodiment, the tube 40 is substantially a cylinder and therefore its volume is calculated by the area of a circumference multiplied by the length of the cylinder.

TEV1,2 = rr*(De/2)^A2*Nt*Le where Nt= number of tubes,

Le= length of the tubes’ sections in the central area,

De= external diameter of the tubes’ sections.

According to the invention TEV2/TEV1 < 0.95, which means that the evaporator in general has a bigger external volume than the condenser. In the figures this difference, due to a tube having a bigger diameter in the evaporator than in the condenser, is not visible (the tube 40 is covered by the fins in figure 3).

In normal operation, when the dryer 1 is switched on, the compressor starts and the heat pump 30 starts its cycle. The pressure, both low and high (at the inlet and outlet

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2019213457 12 Aug 2019 of the compressor 33, respectively), of the refrigerant starts to increase. The increase of the pressure takes place in the so called “transient phase” of the heat pump cycle. This behaviour is depicted in figure 11 (the upper graph is relative to pressure measurements at the outlet of the compressor, while the lower graph is relative to measurements of the pressure at the inlet of the compressor). At the end of the transient phase, the stable phase begins. In the stable phase, the pressure is substantially constant, or increases/decreases only slightly. The measurements substantially fluctuate around a substantially constant average value. In Figure 11, in particular, the stable phase terminates at the end of the heat pump cycle.

Considering an average Xaver of the pressures’ values at the inlet/outlet of the compressor 33, these values are preferably comprised within the following ranges:

bar < Xaver (low) < 17 bar, bar < Xaver (high) < 38 bar.

Claims (14)

1. Claims

   1. A dryer (1) including o A treating chamber (3) where items are introduced and treated with a process air flow;

   o a heat pump system (30) having a refrigerant circuit in which a refrigerant can flow, said refrigerant circuit including a first heat exchanger (32) where the refrigerant is heated up, a second heat exchanger (31) where the refrigerant is cooled off, a compressor (33) to pressurize and circulate the refrigerant through the refrigerant circuit, and a pressurelowering device; said first and/or second heat exchanger (32, 31) being apt to perform heat exchange between said refrigerant flowing in said refrigerant circuit and said process air; the refrigerant being a flammable refrigerant;

   o wherein each of said first and second heat exchanger (32, 31):

   is a finned tube heat exchanger comprising a tube (40) having multiple sections (41) one above the other and a plurality of fins (50);

   is divided in three portions: a central portion (60) wherein said multiple sections (41) of the tube are in contact with said plurality of fins (50), and a first and second end portions (61, 62) where said tube (40) is not in contact with the plurality of fins (50);

   o and wherein a ratio between a total external volume (TEV2) of all sections of the tube included in the central portion (60) in contact with the plurality of fins of the second heat exchanger (31) and a total external volume (TEV1) of all sections of the tube included in the central portion (60) in contact with the plurality of fins of the first heat exchanger (32) has a value lower than 0.95.

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2. 2. The dryer (1) according to any of the preceding claims, wherein the total external volume (TEV2) of all sections of the tube included in the central portion of the second heat exchanger (31) is comprised from 200 cc and 600 cc.
3. 3. The dryer (1) according to any of the preceding claims, wherein the total external volume (TEV1) of all sections of the tube included in the central portion of the first heat exchanger (32) is comprised from 250 cc and 600 cc.
4. 4. The dryer (1) according to any of the preceding claims, wherein said first and/or second heat exchanger (32, 31) is a coil heat exchanger and wherein the tube (40) in said end portions (61,62) includes bends.
5. 5. The dryer (1) according to any of the preceding claims, wherein said tube of said first and/or second heat exchanger (32, 31) has an external diameter (De) comprised between 4 mm and 10 mm.
6. 6. The dryer (1) according to any of the preceding claims, comprising a process air circuit including said treating chamber (3), and a basement (24) where said heat pump (30) is located, the process air circuit including a basement portion comprising a process air conduit where the first and second heat exchangers (32, 31) are positioned, wherein said central portion (60) of said first and/or second heat exchanger is completely contained in said basement process air conduit.
7. 7. The dryer (1) according to any of the preceding claims, wherein said flammable refrigerant includes propane or propylene.
8. 8. The dryer (1) according to any of the preceding claims, wherein said first and/or second heat exchanger (32, 31) defines a total length (Lt) along a length direction (X), said end portions (61,62) being at the opposite side of the central portion (60) along said length direction, said length direction being substantially perpendicular to a main direction of flow of said process air when passing through said first and/or second heat exchanger.
9. 9. The dryer (1) according to any of the preceding claims, wherein the first and/or second heat exchanger (32, 31) defines a thickness along a thickness direction (Y), and wherein the thickness is comprised between 40 mm and 150 mm.

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10. 10. The dryer (1) according to any of the preceding claims, wherein said first and/or second heat exchanger (32, 31) defines a total length (Lt) along a length direction (X), said end portions being at the opposite side of the central portion along said length direction, the total length being smaller than 550 mm.
11. 11. The dryer (1) according to any of the preceding claims when dependent on claim 6, wherein said basement (24) comprises an upper and a lower shell (24a, 24b), said basement process air conduit being formed by said upper and lower shells.
12. 12. The dryer (1) according to any of the preceding claims, wherein the high pressure of the refrigerant in the stable phase of the heat pump cycle is comprised between 19 bar and 38 bar.
13. 13. The dryer (1) according to any of the preceding claims, wherein the low pressure of the refrigerant in the stable phase of the heat pump cycle is comprised between 7 bar and 17 bar.
14. 14. The dryer (1) according to any of the preceding claims wherein the amount of inflammable refrigerant contained in said heat pump refrigerant circuit is comprised between 80 g and 300 g.