NZ615009B2 - Flash defrost system - Google Patents
Flash defrost system Download PDFInfo
- Publication number
- NZ615009B2 NZ615009B2 NZ615009A NZ61500912A NZ615009B2 NZ 615009 B2 NZ615009 B2 NZ 615009B2 NZ 615009 A NZ615009 A NZ 615009A NZ 61500912 A NZ61500912 A NZ 61500912A NZ 615009 B2 NZ615009 B2 NZ 615009B2
- Authority
- NZ
- New Zealand
- Prior art keywords
- defrost
- evaporator
- receiver
- refrigerant
- phase
- Prior art date
Links
- 239000003507 refrigerant Substances 0.000 claims abstract description 78
- 239000007788 liquid Substances 0.000 claims abstract description 57
- 238000005057 refrigeration Methods 0.000 claims abstract description 44
- 230000006835 compression Effects 0.000 claims abstract description 20
- 238000007906 compression Methods 0.000 claims abstract description 20
- 239000012530 fluid Substances 0.000 claims abstract description 17
- 238000010257 thawing Methods 0.000 claims abstract description 9
- 238000005338 heat storage Methods 0.000 claims description 11
- XUKUURHRXDUEBC-KAYWLYCHSA-N Atorvastatin Chemical compound C=1C=CC=CC=1C1=C(C=2C=CC(F)=CC=2)N(CC[C@@H](O)C[C@@H](O)CC(O)=O)C(C(C)C)=C1C(=O)NC1=CC=CC=C1 XUKUURHRXDUEBC-KAYWLYCHSA-N 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 8
- 239000012782 phase change material Substances 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 1
- 230000008859 change Effects 0.000 abstract description 4
- 239000012071 phase Substances 0.000 description 16
- 230000008569 process Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 239000003570 air Substances 0.000 description 2
- 230000003190 augmentative effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004146 energy storage Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/04—Refrigeration circuit bypassing means
- F25B2400/0411—Refrigeration circuit bypassing means for the expansion valve or capillary tube
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/16—Receivers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
- F25B47/022—Defrosting cycles hot gas defrosting
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D21/00—Defrosting; Preventing frosting; Removing condensed or defrost water
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D21/00—Defrosting; Preventing frosting; Removing condensed or defrost water
- F25D21/06—Removing frost
Abstract
Disclosed is a vapour compression refrigeration system with a defrost circuit that includes a compressor (1) arranged to re-circulate refrigerant through a condenser (2), an expansion device (4) and an evaporator (5). To achieve rapid thermodynamically efficient defrosting of the evaporator, hot refrigerant from the condenser is stored in a defrost receiver (6) before passing through the expansion device (4). In a defrost phase, a valve arrangement (7-10) forms a closed defrost circuit connecting the evaporator (5) to the defrost receiver (6) via defrost valve (10) to allow hot fluid to pass from the defrost receiver to the evaporator and liquid refrigerant in the evaporator flows to the defrost receiver (6) via drain valve (9). In a pre-defrost phase, the valve arrangement closes the fluid input to the evaporator (5) and the compressor operates to partially evacuate the evaporator before the evaporator is connected to the defrost receiver, so that flash flooding of the evaporator with hot vapour occurs. A phase change medium (11) may be included to store heat from the condenser output and return it to the evaporator during defrost. Additional heat may be supplied to the defrost liquid to further increase the defrost speed. rigerant from the condenser is stored in a defrost receiver (6) before passing through the expansion device (4). In a defrost phase, a valve arrangement (7-10) forms a closed defrost circuit connecting the evaporator (5) to the defrost receiver (6) via defrost valve (10) to allow hot fluid to pass from the defrost receiver to the evaporator and liquid refrigerant in the evaporator flows to the defrost receiver (6) via drain valve (9). In a pre-defrost phase, the valve arrangement closes the fluid input to the evaporator (5) and the compressor operates to partially evacuate the evaporator before the evaporator is connected to the defrost receiver, so that flash flooding of the evaporator with hot vapour occurs. A phase change medium (11) may be included to store heat from the condenser output and return it to the evaporator during defrost. Additional heat may be supplied to the defrost liquid to further increase the defrost speed.
Description
W0 2012/107773 2012/050293
FLASH DEFROST SYSTEM
TECHNICAL FIELD OF THE INVENTION
This invention relates to a flash defrost system for defrosting
evaporators in vapour compression refrigeration systems. As
will be explained more fully herein, the ion is applicable
to direct expansion, flooded evaporator and liquid overfeed
refrigeration systems.
BACKGROUND
In many applications of vapour compression refrigeration
systems an evaporator is used to cool air, inter alia, in chiller
rooms, arket chilled display cabinets, domestic freezers
and air source heat pumps. In such applications the external
surfaces of the evaporator become covered in ice during.
operation due to condensation and freezing of water vapour in
the atmosphere. Ice formation adversely affects the heat
er performance, and the power consumption of the
compressor rises to compensate for loss of evaporator
efficiency. All such systems are therefore designed to
periodically defrost the ator in order to restore
mance and minimise running costs.
W0 2012/107773
Common methods of defrost include, in order of defrost speed:
discontinuation of the eration s whilst electrical
heaters attached to the evaporator are used to melt and
release the accumulated ice; discontinuation of the refrigeration
effect but, with the compressor still running, diversion of the
hot gas output along an extra line to the evaporator for a time
sufficient to melt and release the ice; discontinuation of the
refrigeration effect and the use of ambient air to melt the ice.
To minimise temperature rises in the refrigerated products the
time of defrost needs to be short, so that ical defrost is
most commonly used in food applications. However, electrical
defrost and hot gas t also incur a cost penalty in terms of
extra energy used.
W0 2009 034 300 A1 discloses an ice maker which es a
vapour compression refrigeration system having multiple
evaporators. Relatively hot refrigerant from a condenser flows
through a defrost receiver before passing through the
evaporators. Individual evaporators can be defrosted by means
of a valve system which connects the evaporator to the t
receiver to allow hot fluid to pass thermosyphonically from the
t receiver to the evaporator and liquid refrigerant in the
evaporator to return by gravity to the defrost receiver.
r, in such a system the length of the defrost period is
relatively unimportant since the remaining evaporators will
continue to operate.
The present invention seeks to provide a new and inventive
form of defrost system which is capable of providing more rapid
and energy-efficient defrosting of the evaporator than has
hitherto been possible.
It is an object of the invention to at least provide the public
with a useful choice.
BRIEF SUMMARY OF THE INVENTION
In one aspect of the invention there is provided a vapour
compression eration system including a compressor
arranged to re-circulate refrigerant through a condenser, an
expansion device and an evaporator, a t receiver with or
without an additional liquid receiver through which hot
refrigerant from the condenser flows before passing through
the expansion device, and a valve arrangement which, in a
defrost phase, connects the evaporator to the defrost receiver
to allow hot refrigerant from the defrost receiver to pass
h the evaporator, wherein
- the valve arrangement is arranged to create, during the
defrost phase, a defrost circuit through which hot refrigerant
vapour flows from the defrost er to the evaporator and
cool liquid erant condensate returns from the evaporator
to the t receiver without passing through the
compressor; and
- the defrost receiver is associated with a heat storage medium
in heat-exchange contact with the refrigerant and from which
stored heat energy is released into the refrigerant g
through the defrost t and transported to the evaporator
during the defrost phase.
Followed by page 3a
- 3a -
In a further aspect of the invention there is provided a method
of defrosting a vapour ssion refrigeration system
including a ssor arranged to re-circulate refrigerant
through a condenser, an expansion device and an evaporator, a
defrost receiver with or t an additional liquid receiver
through which hot erant from the condenser flows before
passing h the expansion device, and a valve
arrangement which, in a defrost phase, connects the
evaporator to the defrost receiver to allow hot refrigerant from
the defrost receiver to pass through the evaporator, wherein
- the valve arrangement is arranged to create, during the
defrost phase, a defrost circuit through which hot erant
vapour flows from the defrost receiver to the evaporator and
cool liquid refrigerant condensate returns from the ator
to the defrost receiver without passing through the
ssor; and
- the defrost receiver is associated with a heat storage medium
in heat-exchange contact with the refrigerant and from which
stored heat energy is released into the refrigerant flowing
through the defrost circuit and transported to the evaporator
during the defrost phase by the s of refrigerant boiling in
the defrost receiver followed by refrigerant condensation in the
evaporator.
In a further aspect of the invention there is provided a vapour
compression refrigeration system including a compressor, a
condenser, a suction manifold, a liquid supply manifold, and a
plurality of evaporators;
Followed by page 3b
- 3b -
each of the evaporators having a respective expansion or
other refrigerant feed device through which refrigerant flows
from the condenser via the liquid supply manifold to the
respective evaporator when the ssor is operated to
re-circulate refrigerant through the condenser and via the
n and liquid supply lds through the respective
ator in a refrigeration cycle; wherein:
a plurality of defrost receivers are provided, each defrost
receiver comprising a respective heat exchanger in association
with a respective heat storage unit, the heat exchanger of each
defrost receiver being ed in association with a respective
one of the evaporators so that refrigerant flows from the
condenser via the liquid supply manifold and through the heat
exchanger of the respective defrost receiver before passing
through the respective expansion or other refrigerant feed
device during the refrigeration cycle;
and each heat storage unit comprises a phase change
material arranged in heat exchange contact with the refrigerant
flowing through the tive heat exchanger so that the
phase change al is melted as it extracts heat from the
refrigerant during the refrigeration cycle;
and each evaporator is provided with a valve
arrangement which is arranged, in a defrost cycle of the
respective ator, to isolate the respective evaporator and
defrost receiver from the suction and liquid supply manifolds
and to t the respective evaporator to the respective
defrost receiver to form a defrost circuit in which refrigerant
from the respective heat exchanger flows through the
Followed by page 3c
- 3c -
evaporator and extracts stored heat energy from the phase
change material in the respective heat storage unit.
Y OF THE INVENTION
The present invention generally proposes a vapour compression
refrigeration system including a ssor arranged to
re-circulate refrigerant through a ser, an expansion
device and an evaporator, in which relatively hot refrigerant
from the condenser flows through a defrost receiver before
passing through the expansion device, and, in a t phase,
a valve arrangement ts the evaporator to the t
receiver to create a defrost circuit which allows hot fluid to pass
from the defrost receiver to the evaporator and liquid
refrigerant in the evaporator to flow to the defrost receiver,
characterised in that the refrigeration system is
constructed and operated such that, in a pre-defrost phase, the
valve arrangement closes the fluid input to the evaporator and
the compressor operates to partially evacuate the evaporator
before the evaporator is connected to the defrost receiver.
By isolating the input to the evaporator prior to commencement
of the t phase and allowing the compressor to remove
refrigerant from the evaporator, the commencement of the
defrost phase causes the hot refrigerant to boil and results in
immediate flash flooding of the evaporator with hot refrigerant
vapour. The invention therefore es a means of
defrosting the evaporator which uses a minimum amount of net
energy
Followed by page 4
W0 2012/107773
from the system and which also enables a significant reduction
in the defrost period. In food applications therefore, the
invention minimises excursions from the ideal storage
temperature of the product.
BRIEF DESCRIPTION OF THE DRAWINGS
The following description and the accompanying drawings
referred to therein are included by way of miting example
in order to rate how the invention may be put into
practice. In the gs:
Figure 1 is a m of a known form of vapour
compression refrigeration circuit upon which the
present invention is based;
Figure 2 is a diagram of a first such refrigeration
circuit incorporating a defrost system in accordance
with the invention;
Figure 3 is a diagram of a second such refrigeration
circuit incorporating a defrost system in accordance
with the invention;
Figure 4 is a modified form of the refrigeration circuit
shown in Fig. 3;
Figure 5 is a modified form of the refrigeration circuit
shown in Fig. 2 which can be used with le evaporators; and
Figure 6 shows a further modification as applied to the refrigeration
circuit of Fig.5.
DETAILED DESCRIPTION OF THE DRAWINGS
Unless the context y requires otherwise, throughout the
description and the claims, the words “comprise”, “comprising”, and the
like are to be construed in an inclusive sense as opposed to an
exclusive or exhaustive sense; that is to say, in the sense of "including,
but not limited to".
Fig. 1, shows a widely used direct expansion ement to which the
present invention may be applied, comprising a closed erant
circuit in which a compressor 1 pressurises vapour phase refrigerant.
The hot superheated gas g the compressor passes to a condenser
2 in which rheating and subcooling occurs. The warm high
pressure liquid refrigerant then passes to a liquid receiver vessel 3
acting as a refrigerant reservoir. Liquid from the reservoir es an
expansion device 4 where a rapid drop in pressure produces a two
phase stream of cold vapour and liquid which then enters the bottom of
ator 5. Evaporation of the liquid phase is completed in the
evaporator so that the required cooling effect is achieved. Cold
sub-cooled vapour from a top exit of the evaporator 5 then returns to
the inlet of the compressor 1 via the suction line of the compressor and
the cycle is repeated.
Various embodiments of the invention will now be described which
achieve rapid energy-efficient defrosting of the evaporator in such a
refrigeration system. In the following description and drawings the
reference numbers used in Fig. 1
are applied to corresponding items within the refrigeration
system.
In the first embodiment which is shown in Fig. 2 a defrost
receiver 6 is ed into the liquid stream between the main
liquid reservoir 3 and the expansion device 4, which may be an
expansion valve. A shut-off valve 7 is ed into the flow
path between the receiver 3 and the defrost receiver 6, and an
isolation valve 8 is inserted between the exit of the evaporator
and the inlet of the compressor 1. A drain valve 9 is
connected in parallel with the expansion valve 4, and a defrost
valve 10 is ted between the top of the defrost receiver 6
and the exit of the evaporator 5. During normal ion the
expansion valve 4 and valves 7 and 8 are open and valves 9
and 10 are closed resulting in a refrigerant flow circuit which is
essentially the same as that shown in Fig. 1. As previously
ned however, normal operation of the t will result in
ice formation on the outside of the evaporator due to
condensation of atmospheric water vapour.
When defrosting of the evaporator is required the expansion
valve 4 is y closed to close off the fluid inlet of the
evaporator while the compressor 1 continues to run. The
suction line to the compressor continues to draw refrigerant
vapour from the evaporator 5, causing partial evacuation of the
evaporator. After a sufficient period of time, valves 7 and 8 are
closed and valve 10 is opened allowing high pressure liquid
refrigerant in the defrost receiver 6 to flash over into the
evaporator 5, which is at a very low pressure. (The compressor
may be turned off during this phase.) Refrigerant vapour
condenses in the evaporator releasing latent heat and
transferring it at high heat transfer ency until the
pressures in the evaporator 5 and the defrost receiver 6
equalise, at which point drain valve 9 is opened to allow liquid
erant in the evaporator to drain back into the er 6
under the action of gravity. When the temperature of the liquid
in the receiver 6 falls to a predetermined level indicating that
defrost is complete, valves 9 and 10 are closed and valves 4, 7
and 8 are opened and the normal operation of the refrigeration
circuit resumes.
In a further improvement of the defrost system in accordance
with the invention the heat energy extracted from the hot liquid
refrigerant and made available for defrost may be augmented
by means of a phase-change unit 11 contained within the
t receiver 6. A suitable phase-change medium is
encapsulated within the phase-change unit 11 so that during
normal operation the hot liquid refrigerant flows in contact with
the phase-change unit melting the phase—change material and
storing enthalpy from the liquid refrigerant stream as latent
heat. During the defrost stage the stored heat energy is
released into the refrigerant stream ating in the closed
loop y accelerating the defrost process. The result of
such extraction of heat from the hot liquid refrigerant stream is
to increase the thermodynamic efficiency of the overall
refrigeration circuit through a more ive expansion
s, which largely compensates for the extra energy
needed to re-cool the evaporator after a defrost. The energy
PCT/G32012/050293
cost of the t process is thereby minimised.
In a second embodiment of the invention which is shown in Fig.
3 the liquid reservoir 3 is ed to act as a defrost receiver.
The evaporator is at a higher level than the receiver, and the
expansion device 4 is of a type which can be fully opened to
remove the ction, for example an expansion valve driven
by a stepper motor. An isolation valve 12 in the compressor
suction line is open when the compressor is running and closed
at other times. A defrost valve 13 connects the exit of the
evaporator to the top of the receiver 3 and is shut in normal
ion. When defrost is initiated the ion valve 4 is
fully closed for a period to allow the evaporator to empty via
the suction line. The compressor 1 is then switched off and
valve 12 is shut. The expansion valve 4 is fully opened
allowing hot liquid to drain back to the liquid receiver, and
valve 13 opens allowing vapour from the top of the receiver 3
to flash over into the partially evacuated evaporator. As the
evaporator is above the receiver and the line from the receiver
3 through the ion valve 4 is full of liquid a flow will be
established from the evaporator through the expansion valve
back to the receiver 3. Vapour will continue to flow from the
receiver 3 h the defrost valve 13 to the evaporator 5
where it will condense, and the condensed liquid will then flow
back to the receiver 3 via the expansion valve 4.
In a variation of this embodiment a heat exchanger 14
containing a phase change medium may be added between the
receiver 3 and the expansion valve 4. This increases the
energy storage capacity while minimising the refrigerant
charge. Alternatively, as shown in Fig. 4, a heat exchanger 15
of the fluid-to-fluid type can be used. The secondary of the
heat exchanger is connected to a pump 16 which circulates an
eeze fluid from a separate tank 17 in a closed circuit, thus
acting to increase the thermal storage capacity of the defrost
system.
In refrigeration installations with multiple evaporators fed from
common liquid supply and suction manifolds, such as those
used in supermarket display ts or cold storage facilities,
the embodiment of the invention shown in Fig. 5 may be used.
The individual evaporators 5 and associated defrost circuitry
ucted and operated as previously described in relation to
Fig. 2 are each connected to the common liquid ld 18
and suction manifold 19. It will be noted that in this case each
evaporator 5 is associated with its own defrost er 6 so
that flash defrosting of the individual evaporators may again
take place as described.
In the embodiments described above the evaporator 5 should
be higher than the heat store module formed by the defrost
receiver 6 and the phase-change unit 11 (if provided) so that
liquid refrigerant can return to the receiver 6 under the action
of gravity. Fig. 6 shows how this requirement can be ed
by adding a pump 20 in series with the valve 9 between the
liquid outlet from the evaporator 5 and the defrost receiver 6.
The pump 20 will return cold liquid refrigerant from the
evaporator 5 to the heat store 6, 11 where it can evaporate and
W0 2012/107773 PCT/G32012/050293
return to the evaporator as vapour. It should also be noted
that with such an arrangement the valve 9 could be replaced
with a non-return valve, ng the requirement for
actuation by the eration control system.
Although the specific embodiments described above are applied
to refrigeration systems of the direct expansion type which
maintain a constant superheat at the evaporator exit, the
invention can also be d to flooded evaporator and liquid
overfeed eration systems. In such systems the
ator is fed with liquid refrigerant and filled with boiling
refrigerant so that a mixture of liquid refrigerant and refrigerant
vapour exits from the evaporator. This requires the addition of
a low pressure accumulator in the suction line so that the liquid
can be separated from the vapour which is returned to the
compressor. Provided the return to the accumulator is above
the fluid level in the evaporator all of the liquid in the
evaporator should evaporate when the liquid feed to the
evaporator is turned off during the frost phase. The
valve arrangement may need to be modified, but the basic
principle of partial evacuation of the evaporator followed by
flash flooding with hot refrigerant from the liquid supply line
would still apply.
In each embodiment of the invention the heat energy extracted
from the hot liquid refrigerant can be augmented by means of
electrical power supplied by a resistance heater located in or
around the defrost receiver with the purpose of accelerating the
t process.
W0 2012/107773
The timing and sequencing of the valve operation, the sizing
and positioning of the t receiver ve to the
evaporator, and the use of thermal ty enhancement by
means of phase change materials, secondary fluid circuit or
electrical power can be optimised for maximum overall system
efficiency.
The type of valves which may be employed in the refrigeration
units described above include, inter alia, check valves, solenoid
valves, ion valves and three—way valves.
The control system employed to manage the operation of the
refrigeration systems described above will initiate and
terminate the defrost process based on information supplied by
temperature and pressure sensors fitted at gic points
around the refrigerant circuits.
Whilst the above description places emphasis on the areas
which are believed to be new and addresses ic problems
which have been identified, it is intended that the features
disclosed herein may be used in any combination which is
capable of providing a new and useful advance in the art.
Claims (14)
1. A vapour compression refrigeration system including a compressor arranged to re-circulate refrigerant through a condenser, an expansion device and an evaporator, a defrost receiver with or without an additional liquid receiver through which hot refrigerant from the condenser flows before passing through the expansion device, and a valve arrangement which, in a t phase, connects the evaporator to the defrost receiver to allow hot refrigerant from the defrost receiver to pass through the ator, wherein - the valve arrangement is arranged to create, during the defrost phase, a t circuit through which hot refrigerant vapour flows from the defrost receiver to the evaporator and cool liquid erant condensate returns from the evaporator to the defrost receiver t passing through the compressor; and - the defrost receiver is associated with a heat storage medium in heat-exchange contact with the refrigerant and from which stored heat energy is ed into the refrigerant flowing through the defrost circuit and orted to the evaporator during the t phase.
2. A vapour compression refrigeration system according to Claim 1 in which the heat storage medium comprises a phase-change medium.
3. A vapour compression refrigeration system according to Claim 2 in which the phase-change medium is contained within the defrost receiver.
4. A vapour compression refrigeration system ing to Claim 2 in which the phase-change medium is included between the defrost receiver and the expansion device.
5. A vapour compression refrigeration system according to Claim 1 in which a fluid-to-fluid heat exchanger is included between the defrost receiver and the expansion device and a fluid heat storage medium is circulated through the secondary of the heat exchanger to a e reservoir.
6. A vapour ssion refrigeration system according to Claim 1 in which heating means is arranged to provide additional heat input to the hot refrigerant flowing from the t receiver.
7. A vapour compression eration system according to Claim 1 which includes a plurality of evaporators and in which each evaporator is associated with a respective defrost receiver.
8. A vapour compression eration system according to Claim 1 in which a pump is arranged to return liquid refrigerant from the evaporator to the defrost receiver during the defrost phase.
9. A vapour compression refrigeration system according to Claim 1, wherein the refrigeration system is arranged such that, in a pre-defrost phase, the valve arrangement closes the fluid input to the evaporator and the compressor operates to partially evacuate the evaporator before the evaporator is connected to the t receiver.
10. A method of defrosting a vapour compression refrigeration system including a compressor arranged to culate refrigerant h a condenser, an expansion device and an evaporator, a defrost receiver with or without an additional liquid receiver through which hot refrigerant from the condenser flows before passing through the expansion device, and a valve arrangement which, in a defrost phase, connects the evaporator to the defrost receiver to allow hot refrigerant from the defrost er to pass through the evaporator, - the valve arrangement is arranged to create, during the defrost phase, a defrost circuit h which hot refrigerant vapour flows from the defrost receiver to the evaporator and cool liquid refrigerant condensate returns from the evaporator to the defrost receiver without passing through the compressor; and - the defrost receiver is associated with a heat storage medium in xchange contact with the erant and from which stored heat energy is released into the refrigerant flowing through the defrost circuit and transported to the evaporator during the defrost phase by the s of refrigerant boiling in the defrost receiver followed by refrigerant condensation in the evaporator.
11. A method according to Claim 10, wherein the valve ement closes the fluid input to the evaporator and the compressor operates to partially evacuate the ator before the evaporator is connected to the defrost receiver.
12. A vapour compression refrigeration system including a compressor, a condenser, a suction manifold, a liquid supply manifold, and a plurality of evaporators; each of the evaporators having a respective expansion or other erant feed device through which refrigerant flows from the condenser via the liquid supply manifold to the respective evaporator when the ssor is operated to re-circulate refrigerant through the condenser and via the suction and liquid supply manifolds h the respective evaporator in a refrigeration cycle; a plurality of defrost receivers are provided, each defrost receiver comprising a respective heat exchanger in association with a respective heat e unit, the heat ger of each defrost receiver being arranged in association with a respective one of the evaporators so that refrigerant flows from the condenser via the liquid supply manifold and through the heat exchanger of the respective defrost receiver before passing through the respective expansion or other refrigerant feed device during the refrigeration cycle; and each heat storage unit comprises a phase change material arranged in heat exchange contact with the refrigerant flowing through the respective heat exchanger so that the phase change material is melted as it extracts heat from the refrigerant during the refrigeration cycle; and each ator is provided with a valve arrangement which is arranged, in a t cycle of the respective evaporator, to isolate the respective evaporator and defrost receiver from the suction and liquid supply manifolds and to connect the respective evaporator to the respective defrost receiver to form a defrost circuit in which refrigerant from the respective heat ger flows through the evaporator and extracts stored heat energy from the phase change material in the respective heat storage unit.
13. A vapour compression refrigeration system according to claim 12, wherein the refrigeration system is arranged such that, in a frost phase of each ator, the valve arrangement closes the fluid input to the evaporator and the compressor operates to partially evacuate the evaporator before the evaporator is connected to the defrost receiver.
14. A vapour compression refrigeration system ntially as herein described with reference to any one of the the embodiments described in
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB1102485.8 | 2011-02-11 | ||
| GB1102485.8A GB2487975A (en) | 2011-02-11 | 2011-02-11 | Flash defrost system |
| PCT/GB2012/050293 WO2012107773A2 (en) | 2011-02-11 | 2012-02-10 | Flash defrost system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| NZ615009A NZ615009A (en) | 2014-09-26 |
| NZ615009B2 true NZ615009B2 (en) | 2015-01-06 |
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ID=
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