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EP 2 242 965 B1 |
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EUROPEAN PATENT SPECIFICATION |
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Mention of the grant of the patent: |
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30.08.2017 Bulletin 2017/35 |
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Date of filing: 16.02.2009 |
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International Patent Classification (IPC):
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International application number: |
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PCT/EP2009/001062 |
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International publication number: |
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WO 2009/103471 (27.08.2009 Gazette 2009/35) |
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REFRIGERATING CIRCUIT AND METHOD OF SELECTIVELY COOLING OR DEFROSTING AN EVAPORATOR
THEREOF
KÜHLSCHALTUNG UND VERFAHREN ZUR SELEKTIVEN KÜHLUNG ODER ENTFROSTUNG EINES VERDAMPFERS
CIRCUIT DE RÉFRIGÉRATION ET PROCÉDÉ SÉLECTIF DE REFROIDISSEMENT OU DE DÉGIVRAGE D'UN
ÉVAPORATEUR DU CIRCUIT
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Designated Contracting States: |
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AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO
PL PT RO SE SI SK TR |
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Priority: |
21.02.2008 WO PCT/EP2008/001367
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Date of publication of application: |
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27.10.2010 Bulletin 2010/43 |
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Proprietor: Carrier Corporation |
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Farmington, CT 06034-4015 (US) |
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Inventor: |
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- HEINBOKEL, Bernd
50999 Cologne (DE)
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Representative: Schmitt-Nilson Schraud Waibel Wohlfrom
Patentanwälte Partnerschaft mbB |
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Destouchesstraße 68 80796 München 80796 München (DE) |
| (56) |
References cited: :
WO-A-2005/063084 JP-A- 57 021 761 JP-U- 56 063 970 US-B1- 6 460 372
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WO-A-2007/001284 JP-A- 61 272 562 JP-U- 60 096 550
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| Note: Within nine months from the publication of the mention of the grant of the European
patent, any person may give notice to the European Patent Office of opposition to
the European patent
granted. Notice of opposition shall be filed in a written reasoned statement. It shall
not be deemed to
have been filed until the opposition fee has been paid. (Art. 99(1) European Patent
Convention).
|
[0001] The invention relates to a refrigerating circuit and to a method of selectively cooling
or defrosting an evaporator of a refrigerating circuit.
[0002] Refrigerating system evaporators, such as disclosed in
JP61-272562, having a plurality of refrigerant pipes are well-known in the art. Refrigerant is
flown through these pipes for effecting a heat exchange with an ambient air flow.
Refrigerant flow direction and air flow direction often constitute a counter-flow
relationship. It is also known to use the same pipes in a defrosting operation by
flowing a hot gas therethrough. During a defrosting operation, however, the problem
arises that one side of the evaporator (hot gas outlet) is not fully defrosted and
the ice build up at this side remains unmelted. Moreover, at the other side of the
evaporator (hot gas inlet) some of the water generated in the defrosting procedure
normally evaporates, which leads to heavy ice build-up in parts of the refrigerating
system that are still below 0°C. Refrigerating systems often comprise a Cu pipe serpentine,
which is for example located in the floor of the refrigerating system, to which the
evaporator is mounted, and helps in the defrosting operation by carrying hot fluid.
[0003] Accordingly, it would be beneficial to provide a refrigerating circuit having an
evaporator, whose defrosting can be carried out in an energy-efficient manner.
[0004] Exemplary embodiments of the invention include a refrigerating circuit comprising
a compressor, a condenser/gas cooler, an expansion device, an evaporator, and refrigerant
conduits circulating a refrigerant therethrough. The evaporator comprises refrigerant
piping comprising a plurality of substantially horizontal layers, each layer comprising
a plurality of pipes, the pipes being substantially perpendicular to an air flow direction
from an air inlet region to an air outlet region of the evaporator. A pipe selected
from the group of the second pipe to the last but one pipe in the air flow direction
in the bottom layer forms the entry pipe of the evaporator. The entry pipe is connectable
with the expansion device to provide a refrigerating mode, and the entry pipe is connectable
with a hot gas conduit to provide a defrosting mode for the evaporator.
[0005] Exemplary embodiments of the invention further include a method of selectively cooling
or defrosting an evaporator of a refrigerating circuit, the method comprising the
steps of compressing a refrigerant; flowing the refrigerant through a gas cooler/condenser
and an expansion device, when cooling is selected, or flowing the refrigerant through
a hot gas by-pass conduit, when defrosting is selected; flowing the refrigerant through
refrigerant piping of the evaporator, the refrigerant piping comprising a plurality
of substantially horizontal layers, each layer comprising a plurality of pipes; and
flowing air through the evaporator with the air flow direction being substantially
perpendicular to the orientation of the pipes. The refrigerant enters the refrigerant
piping of the evaporator at a pipe of the group from the second pipe to the last but
one pipe in the bottom layer.
[0006] Embodiments of the invention are described in greater detail below with reference
to the Figures wherein:
FIG. 1 shows a schematic of an exemplary evaporator and its integration in a refrigerating
circuit in accordance with the present invention.
[0007] FIG. 1 shows a portion of a refrigerating circuit in accordance with an embodiment
of the present invention in a schematic manner. As the compressor and the condenser/gas
cooler are well-known elements in the art, they have been omitted from FIG. 1 for
easy readability.
[0008] The evaporator 4 is shown in detail. It comprises two layers (8, 10) of refrigerant
pipes (8a-8h, 10a-10h). As such evaporators are often disposed in the floor region
of a refrigerating sales furniture, for example an island freezer, layer 8 is hereinafter
also referred to as the bottom layer, whereas layer 10 is hereinafter also referred
to as the top layer. Each layer comprises eight refrigerant pipes, which are shown
as circles giving their representation a cross-sectional appearance, which indicates
that the pipes run perpendicular to the drawing plane. The pipes are numbered with
regard to the air flow direction 12, which is from left to right in the schematic
of FIG. 1. 8a is the first pipe with regard to the air flow direction, 8b the second
pipe, ..., and 8h is the eighth and last pipe with regard to the air flow direction.
An analogous numbering is adhered to for the top layer 10.
[0009] The refrigerant pipes are interconnected by connection elements, which are schematically
depicted by solid lines and dashed lines. The solid lines represent connection elements
that are disposed towards the user from the drawing plane, whereas the dashed lines
represent connection elements behind the drawing plane. In this manner, the pipes
8a to 8h and 10a to 10h combine with the connection elements to form a refrigerant
serpentine whose long legs run back and forth through the drawing plane. This piping
is used to flow a refrigerant through the evaporator, with the detailed description
of the connection set-up and the resulting refrigerant flow given below.
[0010] The third pipe with regard to the air flow direction 12 in the bottom layer 8, i.e.
pipe 8c, hereinafter also referred to as entry pipe, is in connection to an evaporator
inlet section 14 of the refrigerant conduits. Said evaporator inlet section is selectively
connected to a hot gas conduit 6 or the expansion device 2 of the refrigerating circuit.
According means (not shown) for enabling a flow connection between the evaporator
inlet section 14 and either the expansion device 2 or the hot gas conduit 6 and blocking
the respective other of the expansion device 2 and the hot gas conduit 6 are well-known
in the art and therefore not described in detail. The connection with the expansion
device 2 is selected for a refrigerating mode, whereas the connection with the hot
gas conduit 6 is selected for a defrosting mode.
[0011] In the embodiment shown in FIG. 1 the hot gas conduit 6 originates between the compressor
and the condenser/gas cooler. Thus, it establishes a by-pass conduit, diverting the
refrigerant after its compression and before its cooling in the condenser/gas cooler
from the conventional refrigerating circuit. It is apparent that the junction between
the compressor and the condenser/gas cooler may comprise appropriate means for guiding
the refrigerant either into the hot gas conduit 6 or towards the condenser/gas cooler.
The hot gas conduit 6 may also comprise an expansion device for controlling the temperature/pressure
of the refrigerant upon entering the evaporator 4 in the defrosting mode.
[0012] As mentioned above, the refrigerant enters the evaporator 4 at the entry pipe 8c.
From there it is flown through a first section 18 of the refrigerant piping of the
evaporator 4. The first section comprises the pipes 8c, 8d, ..., 8g, and 8h, which
are the entry pipe 8c and all pipes on the bottom layer that are downstream thereof.
These pipes are interconnected by first connection elements 20. The refrigerant is
flown substantially perpendicular to the air flow direction in the pipes and substantially
in a co-flow relationship with the air flow direction 12 in the first connection elements
20 towards the end of the evaporator 4.
[0013] From pipe 8h the refrigerant is flown through the second section 22 of the refrigerant
piping of evaporator 4. The second section 22 of refrigerant piping comprises the
pipes on the top layer from the end of the evaporator 4 to the pipe that is on the
same level as the entry pipe with regards to the air flow direction 12, in this embodiment
the pipe 10c. The pipes of the second section 22 of the refrigerant piping are interconnected
by second connection elements 24. The refrigerant flow in the pipes 10c to 10h of
the second section 22 of refrigerant piping is substantially perpendicular to the
air flow direction 12. The refrigerant flow in the second connection elements 24 exhibits
a substantially counter-flow relationship with the air flow direction 12.
[0014] From pipe 10c the refrigerant is flown through a third section 26 of the refrigerant
piping of evaporator 4, which is - in refrigerant flow direction - comprised of the
pipes 8b, 10b, 10a, and 8a. Accordingly, pipe 8a is the exit pipe of the evaporator.
It is connected to the evaporator outlet section 16 of the refrigerant conduits, which
leads the refrigerant back to the compressor.
[0015] The above-described structure of the evaporator 4 according to an exemplary embodiment
of the invention has a number of implications for the defrosting and the refrigerating
modes. In the refrigerating mode it is the primary objective to generate a heat transfer
between the refrigerant and the air flow that is as efficient as possible. The counter-flow
relationship between the refrigerant and the air flow direction 12 in the second section
22 of the refrigerant piping provides for very good heat transfer conditions. Moreover,
the third section 26 of the refrigerant piping provides for an extended region, where
the refrigerant is at its warmest in the evaporator and the air flow is also at its
warmest right after entering the evaporator 4. This set-up provides for a maximum
heating of the refrigerant and thus for a maximum heat transfer from the air flow
before the refrigerant leaves the evaporator 4 through the exit pipe 8a. In the case
that the refrigerant has been evaporated in the first or second section (18, 22) of
the refrigerant piping, the third section 26 allows for a maximum amount of superheating
of the gaseous refrigerant.
[0016] In the defrosting mode the above-described structure of the evaporator 4 is particularly
efficient for a number of reasons. In the exemplary embodiment of FIG. 1, the hot
refrigerant, after by-passing the condenser/gas cooler and the expansion device 2,
enters the evaporator 4 at entry pipe 8c. At the point of entry the refrigerant is
the warmest and has the biggest effect in melting the ice build-up in the evaporator
4. Thus, the region around the entry pipe 8c and the downstream portion thereof in
the bottom layer receive the most heat, especially in the beginning stages of the
defrosting operation. An advantageous effect thereof is that the support structure
to which the evaporator 4 is attached, for example the floor portion of an island
freezer, is warmed up starting in the middle region and expanding to the sides. A
warming of the support structure at an early stage of the defrosting operation prevents
a scenario wherein ice is melted somewhere in the evaporator 4 and the water is re-frozen
at the support structure, when supposed to drain out of the evaporator 4. The set-up
provides for the support structure, which may be slightly inclined, to be an ideal
gutter for water generated by melting the ice in all parts of the evaporator 4 at
later stages of the defrosting operation. Another advantage is that water vapour which
may be generated around the entry pipe 8c, where continuous heating is effected by
flowing hot fluid through the refrigerant piping, cannot easily leave the evaporator
4 and re-freeze in other parts of the refrigerating system, where the temperature
is still below 0°C. In other words, instead of generating ice build-up outside of
the evaporator 4, the water vapour helps in defrosting the evaporator 4 from the middle
region towards the sides.
[0017] The foregoing discussion shows that the evaporator 4 of the exemplary embodiment
of the invention in FIG. 1 has a structure that allows for extremely energy-efficient
defrosting of the evaporator 4. This even allows basing the defrosting of the evaporator
solely on the by-pass conduit, when CO
2 is used as a refrigerant. The refrigerant piping of the evaporator 4 of the exemplary
embodiment is not designed in a way to sustain CO
2 in a liquid phase. That means that, when CO
2 is used as refrigerant, the condensation energy is not at the disposal of the defrosting
process, which is compensated for by the energy-efficient layout of the evaporator
4.
[0018] As mentioned before, the hot gas conduit 6 may be a by-pass conduit to the refrigerating
circuit. It may also be part of an independent defrosting circuit. It is apparent
that in addition to the flow switching means between the expansion device 2 and the
hot gas conduit 6, second guiding means would be necessary to direct the fluid coming
out of the evaporator 4 into the defrosting circuit or the refrigerant circuit. The
defrosting circuit would in that case need additional means for generating fluid circulation,
for example a compressor.
[0019] The hot gas conduit 6 may carry a fluid in a liquid or gaseous state to the evaporator,
depending on the specific embodiment of the invention.
[0020] Instead of comprising two layers the evaporator 4 may comprise three or more layers
as well. This would lead to some changes as to how the pipes are connected with connection
elements. Assume an evaporator having the two layers 8 and 10, as depicted, as well
as an additional third layer.Assume that the eight pipes of the third layer are denoted
30a, 30b, ..., 30g, and 30h, in analogy with the first layer 8 and the second layer
10. The first section 18 of the refrigerant piping would have the same structure as
in the exemplary embodiment of FIG. 1. However, the second section 22 of the refrigerant
piping would have a fairly different layout. It would comprise the pipes 10c to 10h
of the intermediate layer and the pipes 30c to 30h of the third layer. A plurality
of options can be thought of as to how to connect these pipes with each other. A first
option would be connecting - in refrigerant flow direction - pipes 10a, 30h, 10b,
30g, 10f, etc., forming a kind of sawtooth wave shape of the connection elements.
[0021] Another option would be connecting - in refrigerant flow direction - pipes 10h, 30h,
30g, 10g, 10f, 30f, etc., forming a kind of square wave shape of the connection elements.
Both options have in common that the refrigerant flows in a generally counter-flow
relationship with respect to the air flow direction 12 in the second section 22 of
the refrigerant piping. Additional options, for example options combining the two
above-described ways of connecting the individual pipes, can be thought of. It is
apparent that the connection options increase with the number of layers of refrigerant
pipes. As far as the third section 26 of the refrigerant piping is concerned, a lot
of options for connections starting at the last pipe of the second section 22, i.e.
either 10c or 30c, to the exit pipe 8a exist. As is clear from simple geometric considerations,
there is no possibility of connecting all pipes without any connection elements exhibiting
co-flow relationship with the air flow direction 12. Therefore, a lot of secondary
considerations are left to be considered by the designer when establishing the connection
element layout.
[0022] Exemplary embodiments of the invention, as described above, allow for energy-efficient
cooling of the air flow through an evaporator in a refrigerating mode as well as for
energy-efficient defrosting of said evaporator in a defrosting mode. Introducing the
hot gas into a pipe in the middle portion of the bottom layer of the evaporator in
the defrosting mode provides for a number of advantages. The region around the point
of entry of the hot gas will be heated most and will be defrosted quickest. Therefore,
the support structure, to which the evaporator is mounted, will be defrosted in the
beginning stages of a defrosting operation and thus will provide for an ice-free surface,
which is ideal for receiving and draining the water that is generated throughout the
defrosting process. Moreover, the water vapour, which is generated in the most heated
portion of the evaporator during the defrosting process, will not be able to leave
the evaporator, as it will not stay a vapour on its way to the end portions of the
evaporator. Thus, energy losses due to the heated vapour leaving the evaporator to
be defrosted are minimized and ice built-up in other parts of the refrigerating system,
caused by said water vapour, is prevented. These aspects allow for a highly efficient
defrosting of the evaporator, eliminating the need for or at least reducing the extent
of additional means for defrosting in the support structure or in the evaporator itself.
This even holds true, when CO
2 is used as the hot gas in the defrosting operation, which is fundamentally less attractive
for use in defrosting, as no condensation takes place at pressures common to these
evaporators. The defrosting operation in a refrigerant circuit in accordance with
an embodiment of the invention is so energy-efficient that shorter defrosting times
can be achieved than with electric defrosting. This time duration advantage is paired
with the overall simplification of not having an additional electric defrosting system
integrated into a refrigerating system.
[0023] In a further embodiment of the invention, the hot gas conduit is a by-pass conduit
originating between the compressor and the expansion device and ending between the
expansion device and the evaporator. This structure allows for using the same fluid
for the refrigerating operation as well as for the defrosting operation, which is
very cost-efficient. It also eliminates the need for having a full second fluid circuit
for the fluid of the defrosting operation and eliminates the need for ensuring a strict
separation of the refrigerating fluid and the defrosting fluid. This layout also allows
for a minimum amount of piping used and thus for a very compact design of the refrigerating
circuit.
[0024] Furthermore, the refrigerant entry pipe may be a pipe in the first half of the evaporator
in the air flow direction. In the invention according to claim 1 a first section of
the refrigerant piping of the evaporator comprises the entry pipe and the pipes on
the bottom layer that are downstream of the entry pipe with regard to the air flow
direction. This allows for an early and thorough heating of the bottom region of the
evaporator in the defrosting process, which is beneficial to the draining of the melted
water during the later stages of the defrosting. This first section leaves the beginning
of the evaporator in the air flow direction out, which leaves the option of flowing
the refrigerant therethrough shortly before leaving the evaporator, which in turn
is beneficial in the refrigerating mode. Therefore, this layout is a good basis for
achieving an excellent trade-off between the refrigerating and the defrosting modes.
[0025] It is furthermore possible that first connection elements connect respective adjacent
pipes of the first section of the refrigerant piping of the evaporator, such that
in operation the refrigerant flows in a co-flow relationship with the air flow direction
in the first connection elements. This allows for an advantageous heating of the bottom
layer, and therefore of the underlying support structure, from a middle region towards
an end region of the evaporator.
[0026] In another embodiment of the invention, a second section of the refrigerant piping
of the evaporator comprises the pipes on the level of and downstream from the entry
pipe with regard to the air flow direction above the bottom layer. It is also possible
that second connection elements connect the pipes of the second section of the refrigerant
piping of the evaporator, such that in operation the refrigerant flows in an overall
counter-flow relationship with the air flow direction in the second connection elements.
This allows for using an advantageous counter-flow relationship between the refrigerant
and the air flow in the refrigerating mode. This layout furthermore allows for implementing
the beneficial counter-flow for one or a plurality of layers above the bottom layer,
i. e. in the second section of the refrigerant piping.
[0027] Moreover, it is possible that the first pipe in the air flow direction in the bottom
layer is an exit pipe. This exit pipe may be connected to an evaporator outlet section
of the refrigerant conduits. Having the refrigerant leave the evaporator in the first
pipe in the air flow direction in the bottom layer ensures that the refrigerant flows
last through the inlet region of the evaporator with regard to the air flow. In the
refrigerating mode, this leads to a region of heat exchange between the air flow and
the refrigerant, when they are both in their warmest state throughout the evaporator.
This allows for the maximum amount of superheating of the refrigerant, when in gaseous
form already, which provides for maximum use of the energetic capacity of the refrigerant
in the refrigerating process.
[0028] In a further embodiment, a third section of the refrigerant piping of the evaporator
comprises the pipes upstream of the refrigerant entry pipe with regard to the air
flow direction. This allows for an extended region of heat transfer between the air
flow and the refrigerant, where they are both at their substantially warmest in the
refrigerating mode. It allows for that region to include all layers, forming a heat
exchange region with above described properties across the hole cross-section of the
air flow.
[0029] The refrigerant piping of the evaporator may comprise two or three layers. An evaporator
having four, five or more layers can also be thought of. Each layer of the refrigerant
piping of the evaporator may comprise five to ten pipes, particularly six to eight
pipes. These numbers of pipes have been found to be beneficial for an efficient heat
exchange both in the refrigerating and the defrosting mode. Depending on the application,
less than five pipes or more than ten pipes may also constitute a good layer size.
[0030] In a further embodiment, the refrigerant entry pipe is the second or third pipe in
the air flow direction in the bottom layer of the refrigerant piping of the evaporator.
This allows for the hot gas entering the evaporator towards the middle in the refrigerating
mode, advantageously heating the middle portion of the bottom region of the evaporator
first in a defrosting mode. It also leaves room for having a heat exchange area of
relatively warm refrigerant and relatively warm air flow in the beginning of the evaporator
with regard to the air flow direction, when the system is operated in the refrigerating
mode.
[0031] The refrigerant may be CO
2. It can also be R22 or R404A or any other refrigerant suitable to the refrigerating
circuit.
[0032] In an exemplary embodiment, the air flow in the evaporator is in the refrigerating
mode cooled down to a temperature below 0°C. In other words, the invention is suitable
for freezers and below 0°C refrigerating systems, where defrosting is a big issue.
[0033] It is also possible that the refrigerating circuit comprises two expansion devices
and two evaporators, a first expansion device and a first evaporator forming a below
0°C refrigerating portion of the refrigerating circuit, the second expansion device
and the second evaporator forming an above 0°C refrigerating portion of the refrigerating
circuit. Accordingly, the invention can be applied to a dual system including a freezer
and a refrigerator. In this case, the defrosting may be carried out on the freezing
portion or on the refrigerating portion or on both portions. It is apparent that according
piping and according compressing means will be necessary.
[0034] With the method of selectively cooling or defrosting an evaporator of a refrigerating
circuit according to exemplary embodiments of the invention, as described above, the
same advantages can be attained as with the refrigerating circuit. This method can
be developed further by method steps corresponding to the features as described with
regard to the refrigerating circuit. In order to avoid redundancy such embodiments
and developments of the method of selectively cooling or defrosting an evaporator
of a refrigerating circuit are not repeated.
[0035] While the invention has been described with reference to exemplary embodiments, it
will be understood by those skilled in the art that various changes may be made and
equivalents may be substituted for elements thereof without departing from the scope
of the invention. In addition, many modifications may be made to adapt a particular
situation or material to the teachings of the invention without departing from the
essential scope thereof. Therefore, it is intended that the invention not be limited
to the particular embodiment disclosed, but that the invention will include all embodiments
falling within the scope of the appended claims.
Reference Numerals
[0036]
- 2
- Expansion device
- 4
- Evaporator
- 6
- Hot gas conduit
- 8
- Bottom layer of refrigerant piping of evaporator
- 10
- Top layer of refrigerant piping of evaporator
- 12
- Air flow direction
- 14
- Evaporator inlet section of refrigerant conduits
- 16
- Evaporator outlet section of refrigerant conduits
- 18
- First section of refrigerant piping of evaporator
- 20
- First connection elements
- 22
- Second section of refrigerant piping of evaporator
- 24
- Second connection elements
- 26
- Third section of refrigerant piping of evaporator
1. Refrigerating circuit comprising a compressor, a condenser/gas cooler, an expansion
device (2), an evaporator (4), and refrigerant conduits circulating a refrigerant
therethrough,
wherein the evaporator (4) comprises refrigerant piping comprising a plurality of
substantially horizontal layers (8, 10) each layer comprising a plurality of pipes
(8a-8h, 10a-10h) the pipes being substantially perpendicular to an air flow direction
(12) from an air inlet region to an air outlet region of the evaporator (4),
wherein a pipe selected from the group of the second pipe (8b) to the last but one
pipe (8g) in the bottom layer (8) forms the entry pipe (8c) of the evaporator (4),
wherein the entry pipe (8c) is connectable with the expansion device (2) to provide
a refrigerating mode,
wherein the entry pipe (8c) is connectable with a hot gas conduit (6) to provide a
defrosting mode for the evaporator (4), characterized by a first section (18) of the refrigerant piping of the evaporator (4) comprises the
entry pipe (8c) and the pipes (8d-8h) on the bottom layer (8) that are downstream
of the entry pipe (8c) with regard to the air flow direction (12).
2. Refrigerating circuit according to claim 1, wherein the hot gas conduit is a by-pass
conduit originating between the compressor and the expansion device (2) and ending
between the expansion device (2) and the evaporator (4).
3. Refrigerating circuit according to claim 1 or 2, wherein the refrigerant entry pipe
(8c) is a pipe in the first half of the evaporator (4) in the air flow direction (12).
4. Refrigerating circuit according to claim 1, wherein first connection elements (20)
connect respective adjacent pipes (8c,8d; 8d,8e; 8e,8f; 8f,8g; 8g,8h) of the first
section (18) of the refrigerant piping of the evaporator (4), such that in operation
the refrigerant flows in a co-flow relationship with the air flow direction (12) in
the first connection elements (20).
5. Refrigerating circuit according to claim 1 or 4, wherein a second section (22) of
the refrigerant piping of the evaporator (4) comprises the pipes (10c-10h) on the
level of and downstream from the entry pipe (8c) with regard to the air flow direction
(12) above the bottom layer (8).
6. Refrigerating circuit according to claim 5, wherein second connection elements (24)
connect the pipes (10c-10h) of the second section (22) of the refrigerant piping of
the evaporator (4), such that in operation the refrigerant flows in an overall counter-flow
relationship with the air flow direction (12) in the second connection elements (24).
7. Refrigerating circuit according to any of the previous claims, wherein the first pipe
(8a) in the air flow direction (12) in the bottom layer (8) is an exit pipe (8a).
8. Refrigerating circuit according to any of the claims 5 to 7, wherein a third section
(26) of the refrigerant piping of the evaporator (4) comprises the pipes (8a, 8b,
10a, 10b) upstream of the refrigerant entry pipe (8c) with regard to the air flow
direction (12).
9. Refrigerating circuit according to any of the previous claims, wherein the refrigerant
piping of the evaporator (4) comprises 2 or 3 layers.
10. Refrigerating circuit according to any of the previous claims, wherein each layer
(8, 10) of the refrigerant piping of the evaporator (4) comprises 5 to 10 pipes, particularly
6 to 8 pipes.
11. Refrigerating circuit according to any of the previous claims, wherein the refrigerant
entry pipe is the second or third pipe in the air flow direction (12) in the bottom
layer (8) of the refrigerant piping of the evaporator (4).
12. Refrigerating circuit according to any of the previous claims, wherein the refrigerant
is CO2.
13. Refrigerating circuit according to any of the previous claims, wherein the air flow
in the evaporator is in the refrigerating mode cooled down to a temperature below
0°C.
14. Refrigerating circuit according to any of previous claims, wherein the refrigerating
circuit comprises two expansion devices and two evaporators, a first expansion device
and a first evaporator forming a below 0°C refrigerating portion of the refrigerating
circuit, the second expansion device and the second evaporator forming an above 0°C
refrigerating portion of the refrigerating circuit.
15. Method of selectively cooling or defrosting an evaporator (4) of a refrigerating circuit,
the method comprising the steps of:
(a) compressing a refrigerant,
(b)
(i) flowing the refrigerant through a gas cooler/condenser and an expansion device
(2), when cooling is selected, or
(ii) flowing the refrigerant through a hot gas by-pass conduit (6), when defrosting
is selected,
(c) flowing the refrigerant through refrigerant piping of the evaporator (4), the
refrigerant piping comprising a plurality of substantially horizontal layers (8, 10)
each layer (8, 10) comprising a plurality of pipes (8a-8h, 10a-10h), and
(d) flowing air through the evaporator (4) with the air flow direction (12) being
substantially perpendicular to the orientation of the pipes (8a-8h, 10a-10h),
wherein the refrigerant enters the refrigerant piping of the evaporator (4) at a pipe
of the group from the second pipe (8b) to the last but one pipe (8g) in the bottom
layer (8),
characterized in that the refrigerant flows through a first section (18) of the refrigerant piping of the
evaporator (4) comprising the entry pipe (8c) and the pipes (8d-8h) on the bottom
layer (8) that are downstream of the entry pipe (8c) with regard to the air flow direction
(12).
1. Kühlkreislauf, umfassend einen Verdichter, einen Kondensator/Gaskühler, eine Expansionseinrichtung
(2), einen Verdampfer (4) und Kältemittelleitungen, welche ein Kältemittel darin zirkulieren,
wobei der Verdampfer (4) Kältemittelrohrleitungen umfasst, welche eine Mehrzahl von
im Wesentlichen horizontalen Lagen (8, 10) umfassen, wobei jede Lage eine Mehrzahl
von Rohren (8a-8h, 10a-10h) umfasst, wobei die Rohre im Wesentlichen senkrecht zu
einer Luftstromrichtung (12) von einem Lufteinlassbereich zu einem Luftauslassbereich
des Verdampfers (4) sind,
wobei ein Rohr, welches aus der Gruppe vom zweiten Rohr (8b) bis zum vorletzten Rohr
(8g) in der unteren Lage (8) ausgewählt wird, das Einlassrohr (8c) des Verdampfers
(4) bildet,
wobei das Einlassrohr (8c) mit der Expansionseinrichtung (2) verbindbar ist, um einen
Kühlmodus bereitzustellen,
wobei das Einlassrohr (8c) mit einer Heißgasleitung (6) verbindbar ist, um einen Entfrostermodus
für den Verdampfer (4) bereitzustellen, dadurch gekennzeichnet, dass ein erster Abschnitt (18) der Kühlrohrleitung des Verdampfers (4) das Einlassrohr
(8c) und die Rohre (8d-8h) auf der unteren Lage (8) umfasst, welche stromabwärts des
Einlassrohrs (8c) in Bezug auf die Luftstromrichtung (12) angeordnet sind.
2. Kühlkreislauf nach Anspruch 1, wobei die Heißgasleitung eine Umgehungsleitung ist,
die zwischen dem Verdichter und der Expansionseinrichtung (2) beginnt und zwischen
der Expansionseinrichtung (2) und dem Verdampfer (4) endet.
3. Kühlkreislauf nach Anspruch 1 oder 2, wobei das Kältemitteleinlassrohr (8c) ein Rohr
in der ersten Hälfte des Verdampfers (4) in Luftstromrichtung (12) ist.
4. Kühlkreislauf nach Anspruch 1, wobei erste Verbindungselemente (20) entsprechend angrenzende
Rohre (8c,8d; 8d,8e; 8e,8f; 8f,8g; 8g,8h) des ersten Abschnitts (18) der Kältemittelrohrleitung
des Verdampfers (4) verbinden, so dass das Kältemittel im Betrieb in einer Gleichstrombeziehung
mit der Luftstromrichtung (12) in den ersten Verbindungselementen (20) strömt.
5. Kühlkreislauf nach Anspruch 1 oder 4, wobei ein zweiter Abschnitt (22) der Kältemittelrohrleitung
des Verdampfers (4) die Rohre (10c-10h) auf der Ebene und stromabwärts des Einlassrohrs
(8c) in Bezug auf die Luftstromrichtung (12) über der unteren Lage (8) umfasst.
6. Kühlkreislauf nach Anspruch 5, wobei zweite Verbindungselemente (24) die Rohre (10c-10h)
des zweiten Abschnitts (22) der Kältemittelrohrleitung des Verdampfers (4) verbinden,
so dass das Kältemittel im Betrieb in einer Gesamtgegenstrombeziehung mit der Luftstromrichtung
(12) in den zweiten Verbindungselementen (24) strömt.
7. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei das erste Rohr (8a) in
Luftstromrichtung (12) in der unteren Lage (8) ein Auslassrohr (8a) ist.
8. Kühlkreislauf nach einem der Ansprüche 5 bis 7, wobei ein dritter Abschnitt (26) der
Kältemittelrohrleitung des Verdampfers (4) die Rohre (8a, 8b, 10a, 10b) stromaufwärts
des Kältemitteleinlassrohrs (8c) in Bezug auf die Luftstromrichtung (12) umfasst.
9. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei die Kältemittelrohrleitung
des Verdampfers (4) 2 oder 3 Lagen umfasst.
10. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei jede Lage (8, 10) der
Kältemittelrohrleitung des Verdampfers (4) 5 bis 10 Rohre, insbesondere 6 bis 8 Rohre,
umfasst.
11. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei das Kältemitteleinlassrohr
das zweite oder dritte Rohr in Luftstromrichtung (12) in der unteren Lage (8) der
Kältemittelrohrleitung des Verdampfers (4) ist.
12. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei das Kältemittel CO2 ist.
13. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei der Luftstrom im Verdampfer
im Kühlmodus auf eine Temperatur unter 0 °C heruntergekühlt wird.
14. Kühlkreislauf nach einem der vorhergehenden Ansprüche, wobei der Kühlkreislauf zwei
Expansionseinrichtungen und zwei Verdampfer umfasst, wobei eine erste Expansionseinrichtung
und ein erster Verdampfer einen unter 0 °C kühlenden Bereich des Kühlkreislaufs bilden
und die zweite Expansionseinrichtung und der zweite Verdampfer einen über 0 °C kühlenden
Bereich des Kühlkreislaufs bilden.
15. Verfahren zur selektiven Kühlung oder Entfrostung eines Verdampfers (4) eines Kühlkreislaufs,
wobei das Verfahren die folgenden Schritte umfasst:
(a) Verdichten eines Kältemittels,
(b)
(i) Strömen des Kältemittels durch einen Gaskühler/Kondensator und eine Expansionseinrichtung
(2), wenn Kühlen ausgewählt ist, oder
(ii) Strömen des Kältemittels durch eine Heißgasumgehungsleitung (6), wenn Entfrosten
ausgewählt ist,
(c) Strömen des Kältemittels durch die Kältemittelrohrleitung des Verdampfers (4),
wobei die Kältemittelrohrleitung eine Vielzahl von im Wesentlichen horizontalen Lagen
(8, 10) umfasst, wobei jede Lage (8, 10) eine Vielzahl von Rohren (8a-8h, 10a-10h)
umfasst, und
(d) Strömen von Luft durch den Verdampfer (4), wobei die Luftstromrichtung (12) im
Wesentlichen senkrecht zur Ausrichtung der Rohre (8a-8h, 10a-10h) ist,
wobei das Kältemittel in die Kältemittelrohrleitung des Verdampfers (4) an einem Rohr
aus der Gruppe von dem zweiten Rohr (8b) bis zum vorletzten Rohr (8g) in der unteren
Lage (8) eintritt,
dadurch gekennzeichnet, dass
das Kältemittel durch einen ersten Abschnitt (18) der Kältemittelrohrleitung des Verdampfers
(4) strömt, welche das Einlassrohr (8c) und die Rohre (8d-8h) auf der unteren Lage
(8) umfasst, welche stromabwärts des Einlassrohrs (8c) in Bezug auf die Luftstromrichtung
(12) angeordnet sind.
1. Circuit de réfrigération comprenant un compresseur, un condensateur/refroidisseur
de gaz, un dispositif de détente (2), un évaporateur (4), et des conduits de frigorigène
dans lequel circule un frigorigène.
dans lequel l'évaporateur (4) comprend une tuyauterie de frigorigène présentant plusieurs
couches sensiblement horizontales (8, 10), comprenant chacune plusieurs tuyaux (8a-8h,
10a-10h), les tuyaux étant sensiblement perpendiculaires à un sens d'écoulement de
l'air (12) d'une zone d'admission d'air à une zone de sortie d'air de l'évaporateur
(4),
dans lequel un tuyau choisi dans le groupe formé du second (8b) à l'avant-dernier
tuyau (8g) installé dans la couche de fond (8) constitue le tuyau d'admission (8c)
de l'évaporateur (4),
dans lequel le tuyau d'admission (8c) peut être raccordé au dispositif de détente
(2) pour assurer un mode de réfrigération,
dans lequel le tuyau d'admission (8c) peut être raccordé à un conduit de gaz chaud
(6) pour assurer un mode de dégivrage pour l'évaporateur (4), caractérisé par
une première section (18) de la tuyauterie de frigorigène de l'évaporateur (4) comprenant
le tuyau d'admission (8c) et les tuyaux (8d-8h) sur la couche de fond (8) qui sont
en aval du tuyau d'admission (8c) par rapport au sens d'écoulement de l'air (12).
2. Circuit de réfrigération selon la revendication 1, dans lequel le conduit de gaz chaud
est un conduit de dérivation ayant son origine entre le compresseur et le dispositif
de détente (2) et se terminant entre le dispositif de détente (2) et l'évaporateur
(4).
3. Circuit de réfrigération selon la revendication 1 ou 2, dans lequel le tuyau d'admission
du frigorigène (8c) est un tuyau dans la première moitié de l'évaporateur (4) dans
le sens d'écoulement de l'air (12).
4. Circuit de réfrigération selon la revendication 1, dans lequel des premiers éléments
de raccordement (20) sont raccordés à des tuyaux adjacents respectifs (8c, 8d ; 8d,
8e ; 8e, 8f ; 8f, 8g ; 8g, 8h) de la première section (18), de la tuyauterie de frigorigène
de l'évaporateur (4), de sorte qu'en fonctionnement le frigorigène s'écoule dans une
relation de co-écoulement avec le sens d'écoulement de l'air (12) dans les premiers
éléments de raccordement (20).
5. Circuit de réfrigération selon la revendication 1 ou 4, dans lequel une deuxième section
(22) de la tuyauterie de frigorigène de l'évaporateur (4) comprend les tuyaux (10c-10h)
au niveau et en aval du tuyau d'admission (8c) par rapport au sens d'écoulement de
l'air (12) au-dessus de la couche de fond (8).
6. Circuit de réfrigération selon la revendication 5, dans lequel les seconds éléments
de raccordement (24) sont raccordés aux tuyaux (10c-10h) de la deuxième section (22)
de la tuyauterie de frigorigène de l'évaporateur (4), de sorte qu'en fonctionnement
le frigorigène s'écoule dans une relation globalement à contre-courant avec le sens
d'écoulement de l'air (12) dans les seconds éléments de raccordement (24).
7. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel le premier tuyau (8a) dans le sens d'écoulement de l'air (12) dans la couche
de fond (8) est un tuyau de sortie (8a).
8. Circuit de réfrigération selon l'une quelconque des revendications 5 à 7, dans lequel
une troisième section (26) de la tuyauterie de frigorigène de l'évaporateur (4) comprend
les tuyaux (8a, 8b, 10a, 10b) en amont du tuyau d'admission de frigorigène (8c) par
rapport au sens d'écoulement de l'air (12).
9. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel la tuyauterie de frigorigène de l'évaporateur (4) comprend 2 ou 3 couches.
10. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel chaque couche (8, 10) de la tuyauterie de frigorigène de l'évaporateur (4)
comprend 5 à 10 tuyaux, en particulier 6 à 8 tuyaux.
11. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel le tuyau d'admission de frigorigène est le deuxième ou le troisième tuyau dans
le sens d'écoulement de l'air (12) dans la couche de fond (8) de la tuyauterie de
frigorigène de l'évaporateur (4).
12. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel le frigorigène est du CO2.
13. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel l'écoulement de l'air dans l'évaporateur est dans le mode de réfrigération
refroidi à une température inférieure à 0 °C.
14. Circuit de réfrigération selon l'une quelconque des revendications précédentes, dans
lequel le circuit de réfrigération comprend deux dispositifs de détente et deux évaporateurs,
un premier dispositif de détente et un premier évaporateur constituant une partie
de réfrigération du circuit de réfrigération inférieure à 0 °C, le second dispositif
de détente et le second évaporateur constituant une partie de réfrigération du circuit
de réfrigération supérieure à 0 °C.
15. Procédé permettant de refroidir ou de dégivrer sélectivement un évaporateur (4) d'un
circuit de réfrigération, le procédé comprenant les étapes consistant à :
(a) compresser le frigorigène,
(b)
(i) faire passer le frigorigène à travers un condensateur/refroidisseur de gaz et
un dispositif de détente (2), quand la réfrigération est choisie, ou
(ii) faire passer le frigorigène à travers un conduit de dérivation de gaz chaud (6),
quand le dégivrage est choisi,
(c) faire passer le frigorigène à travers la tuyauterie de frigorigène de l'évaporateur
(4), la tuyauterie de frigorigène étant constituée de plusieurs couches sensiblement
horizontales (8, 10) chaque couche (8, 10) comprenant plusieurs tuyaux (8a-8h, 10a-10h),
et
(d) faire passer l'air à travers l'évaporateur (4) le sens d'écoulement de l'air (12)
étant sensiblement perpendiculaire à l'orientation des tuyaux (8a-8h, 10a-10h),
dans lequel le frigorigène pénètre dans la tuyauterie de frigorigène de l'évaporateur
(4) au niveau d'un tuyau du groupe formé du second (8b) à l'avant-dernier tuyau (8g)
dans la couche de fond (8),
caractérisé en ce que
le frigorigène s'écoule à travers une première section (18) de la tuyauterie de frigorigène
de l'évaporateur (4) comprenant
le tuyau d'admission (8c) et les tuyaux (8d-8h) sur la couche de fond (8) qui sont
en aval du tuyau d'admission (8c) par rapport au sens d'écoulement de l'air (12).

REFERENCES CITED IN THE DESCRIPTION
This list of references cited by the applicant is for the reader's convenience only.
It does not form part of the European patent document. Even though great care has
been taken in compiling the references, errors or omissions cannot be excluded and
the EPO disclaims all liability in this regard.
Patent documents cited in the description