[0001] This invention relates to a refrigeration apparatus and refrigeration method, and
in particular to refrigeration apparatus capable of operating in either a vapour compression
mode or a thermosyphon mode.
[0002] UK Patent GB 2 233 080 B describes a refrigeration apparatus which may be operated
in a mechanical mode, or alternatively in a thermosyphon mode. In the mechanical mode
the apparatus operates in a conventional manner utilising a vapour compression cycle,
with refrigerant vapour being compressed before being passed through a heat exchanger
(condenser) where sensible heat is rejected to the atmosphere from the compressed
refrigerant, then passing the resulting condensate through a restriction, typically
an expansion valve, and finally passing the expanded and cooled refrigerant to a heat
exchanger (evaporator) to absorb heat from a fluid to be chilled. When ambient temperatures
are sufficiently low the refrigerant path may be reconfigured to bypass the compressor
and the expansion valve such that the only cooling effect experienced by the refrigerant
is when the refrigerant is passed through the condenser, the evaporator being located
below the condenser such that the refrigerant may circulate without the mechanical
assistance normally provided by the compressor. Clearly, operation in the thermosyphon
mode is more economical than the mechanical or vapour compression mode.
[0003] In a typical refrigerating unit incorporating this feature, several refrigerating
systems are arranged so that the fluid to be chilled is passed through the evaporators
in series. A number of the systems may cool the fluid by vapour compression operation
while other systems operating with warmer inlet fluid may contribute a share of the
required cooling by thermosyphon operation. However, such units are expensive and
involve high capital costs and in practice are restricted to very large units where
stand-by equipment is specified. It has not yet been possible to use an individual
two-mode system, as when the system changes from vapour compression refrigeration
to thermosyphon refrigeration there is a period of delay while the heat rejection
equipment, previously in contact with the compressed (and thus heated) refrigerant,
cools to a temperature below that of the fluid being chilled.
[0004] It is among the objects of the present invention to provide an apparatus and method
which obviate or mitigate this disadvantage.
[0005] According to the present invention there is provided refrigeration apparatus capable
of operating in i) vapour compression mode or ii) thermosyphon mode, the apparatus
defining a refrigerant path comprising:
compression means for compressing a refrigerant;
heat rejection means for cooling the compressed refrigerant;
restriction means for expanding the refrigerant;
chilling means for permitting the absorption of heat by the refrigerant from a
fluid to be chilled;
valve means configurable for selectively directing refrigerant i) to pass through
the compression means and restriction means or ii) to bypass the compression means
and restriction means; and
thermal storage means for i) being cooled while the apparatus operates in the vapour
compression mode and ii) providing a chilling effect during changeover to thermosyphon
mode.
[0006] According to a further aspect of the present invention there is provided a refrigeration
method including i) a vapour compression mode or ii) a thermosyphon mode, the method
including the steps of:
rejecting heat from a refrigerant;
chilling a fluid with the refrigerant; and
i) when operating in vapour compression mode the method further including the steps
of:
a) compressing the refrigerant;
b) expanding the refrigerant; and
c) cooling a thermal storage means; and
ii) when operating in thermosyphon mode the method further including the step of:
a) providing a chilling effect using the thermal storage means, at least during
initial changeover from vapour compression mode to thermosyphon mode.
[0007] The chilled fluid may be the fluid contained within a space to be cooled, for example
a refrigerated compartment, but will usually be a liquid, such as water, to be utilised
as a cooling medium for a region to be cooled, such as an air conditioned space, which
may be remote from the refrigeration apparatus.
[0008] Preferably, the thermal storage means i) is cooled by the chilled fluid while the
apparatus operates in the vapour compression mode and ii) chills the fluid on changeover
to thermosyphon mode.
[0009] Preferably also, operation in thermosyphon mode is achieved without any mechanical
circulation of the refrigerant, which, in the vapour compression mode, is typically
provided by the compression means. In this case the chilling means will be positioned
below the heat rejection means. Alternatively, if some other arrangement is desired,
refrigerant circulation means may be provided for use in the thermosyphon mode.
[0010] Thus, the present invention allows changeover from compression mode to thermosyphon
mode without the period of delay that occurs in conventional two-mode systems as the
heat rejection means cools to a temperature below that of the fluid being chilled;
during this changeover period the present invention provides for chilling of the fluid
by the thermal storage means.
[0011] In a preferred embodiment, with selection of appropriate thermal storage means, the
invention may operate at full capacity in the vapour compression mode irrespective
of cooling load, any excess capacity being utilised to cool the thermal storage means.
On the thermal storage means reaching a condition where it cannot be cooled further,
the fluid temperature will drop sharply, allowing a thermostatic switch to reconfigure
the valve means to provide the thermosyphon mode. The thermal storage means then begins
to chill the fluid, preventing an immediate rise in temperature of the fluid and allowing
time for the apparatus to adjust to thermosyphon mode.
[0012] Preferably also, the thermal storage means contains a phase change material which
will absorb or reject heat at a substantially constant temperature. Substances suitable
for use in such means include acetic acid and lactic acid.
[0013] These and other aspects of the present invention will now be described, by way of
example, with reference to the accompanying drawing, which illustrates, in schematic
form, refrigeration apparatus in accordance with a preferred embodiment of the present
invention.
[0014] The apparatus includes ducting 10 which partially defines a refrigerant path around
which refrigerant is cycled in either i) a mechanical or vapour compression mode or
ii) a thermosyphon mode. In vapour compression mode the refrigerant is first subject
to compression by a positive displacement compressor 12, from which the high pressure
refrigerant passes to heat rejection means in the form of a condenser 14, which is
exposed to ambient air. Following condensing and cooling in the condenser 14, the
refrigerant passes to restriction means in the form of an expansion valve 16, which
causes a sufficient portion of the refrigerant to vaporise to reduce the temperature
of the remaining liquid to that consistent with the lower pressure. The expanded and
cooled refrigerant is then passed to a heat exchanger in the form of a chiller 18
where the refrigerant absorbs heat from fluid to be cooled. On exit from the chiller
18, the refrigerant, now in the form of low pressure vapour, returns to the compressor
12.
[0015] The chiller 18 forms part of a secondary cooling circuit around which a fluid, such
as water, is circulated. Following chilling, the water passes through a thermal store
20 which contains a phase change material. The water then passes through a region
to be cooled 22, before returning to the chiller 18, circulation of the fluid around
the cooling circuit being achieved by means of a fluid pump 24.
[0016] The refrigeration circuit includes a three-way valve 26 and a two-way ball valve
28, and for operation in the vapour compression mode the valves 26, 28 are configured
such that refrigerant is passed through the compressor 12 and the expansion valve
16. However, when the ambient temperature is particularly low (that is lower than
the temperature of the water to be chilled), the valves 26, 28 may be configured to
bypass the compressor 12 and valve 16, such that the refrigerant is cooled solely
by ambient air as it passes through the condenser 14. Also, the chiller 18 is positioned
below the condenser 14 and the ducting 10 is arranged such that the refrigerant will
circulate in this thermosyphon mode without mechanical assistance, thus minimising
the energy consumption of the apparatus.
[0017] While operating in vapour compression mode, the compressor 12 may operate at full
capacity, irrespective of the cooling load, any excess cooling of the water being
absorbed by the thermal store 20, in which the excess cooling capacity is utilised
to solidify a liquid, at constant temperature. When the phase change material has
completely solidified there will be a sharp decrease in the temperature of the water,
which may be detected by a thermostat 30 which operates to switch the apparatus from
vapour compression mode to thermosyphon mode, that is by shutting down the compressor
12 and reconfiguring the valves 26, 28 to bypass the compressor 12 and the expansion
valve 16. Initially, on switching from vapour compression mode to thermosyphon mode,
the refrigerant in the ducting 10 downstream of the compressor 12 and upstream of
the expansion valve 16 will be at a higher temperature than the water and it takes
some time for the refrigerant and the condenser hardware and ducting to be cooled
to a level where its temperature is lower than that of the water. Also, in order for
circulation of refrigerant to take place without mechanical assistance, the temperature
of the refrigerant in the condenser 14 must fall below the temperature at the outlet
from the chiller 18, the reverse of the situation in the vapour compression mode.
During this transition period the water is chilled by the thermal store 20, as the
phase change material in the store is melted by the circulating water.
[0018] From the above description it will be seem that this embodiment of the invention
provides an arrangement in which refrigeration apparatus capable of operating in a
thermosyphon mode may be utilised on an individual basis, and not necessarily as part
of a larger system. Further, the provision of the thermal store 20 allows the system
to be operated at full capacity in vapour compression mode, which is of course more
efficient than operating at part capacity.
[0019] The present invention may be utilised in a wide variety of applications, but is particularly
useful where the cooling load is to be maintained at a relatively high temperature,
such as in air conditioning systems for building which chill the ceilings of rooms
and corridors. Such air conditioning is particularly suitable for thermosyphon cooling
techniques as the chilled ceilings must be kept at a temperature higher than the dew
point of the room air. These relatively high temperatures allows the associated refrigeration
apparatus to operate in thermosyphon mode for a significant number of hours per year.
[0020] It will be clear to those of skill in the art that the above described embodiment
is merely exemplary of the present invention and that various modifications and improvements
may be made thereto without departing from the scope of the invention.
1. Refrigeration apparatus capable of operating in i) vapour compression mode or ii)
thermosyphon mode, the apparatus defining a refrigerant path comprising:
compression means (12) for compressing a refrigerant;
heat rejection means (14) for cooling the compressed refrigerant;
restriction means (16) for expanding the refrigerant;
chilling means (18) for permitting the absorption of heat by the refrigerant from
a fluid to be chilled;
valve means (26, 28) configurable for selectively directing refrigerant i) to pass
through the compression means (12) and restriction means (16) or ii) to bypass the
compression means (12) and restriction means (16); and
thermal storage means (20) for i) being cooled while the apparatus operates in
the vapour compression mode and ii) providing a chilling effect during changeover
to thermosyphon mode.
2. The apparatus of claim 1 in which the chilled fluid is a cooling medium for a region
(22) to be cooled.
3. The apparatus of claim 1 or claim 2 in which the thermal storage means (20) is i)
arranged to be cooled by the chilled fluid while the apparatus operates in the vapour
compression mode and ii) arranged to chill the fluid during changeover to thermosyphon
mode.
4. The apparatus of claims 1, 2 or 3 in which the chilling means (20) is positioned below
the heat rejection means (14 ) to allow operation in thermosyphon mode without any
mechanical circulation.
5. The apparatus of claims 1, 2 or 3 wherein refrigerant circulation means is provided
for use in the thermosyphon mode.
6. The apparatus of any one of the preceding claims wherein the thermal storage means
(20) is arranged such that the apparatus is operable at full capacity in the vapour
compression mode irrespective of cooling load, any excess capacity being utilised
to cool the thermal storage means (20).
7. The apparatus of claim 6 further comprising a thermostatic switch (30) to reconfigure
the valve means (26, 28) from the vapour compression mode to the thermosyphon mode
on the thermal storage means (20) reaching a condition where it cannot be cooled further.
8. The apparatus of any one of the preceding claims wherein the thermal storage means
(20) contains a phase change material which will absorb or reject heat at a substantially
constant temperature.
9. The apparatus of claim 8 wherein the phase change material is one of acetic acid or
lactic acid.
10. A refrigeration method including i) a vapour compression mode or ii) a thermosyphon
mode, the method including the steps of:
rejecting heat from a refrigerant;
chilling a fluid with the refrigerant; and
i) when operating in vapour compression mode the method further including the steps
of:
a) compressing the refrigerant;
b) expanding the refrigerant; and
c) cooling a thermal storage means; and
ii) when operating in thermosyphon mode the method further including the step of:
a) providing a chilling effect using the thermal storage means, at least during
initial changeover from vapour compression mode to thermosyphon mode.
11. The method of claim 10 wherein the chilled fluid provides a cooling medium for a region
to be cooled.
12. The method of claim 10 or claim 11 wherein the thermal storage means is i) cooled
by the chilled fluid in vapour compression mode and ii) chills the fluid during changeover
to thermosyphon mode.
13. The method of claim 10, 11 or 12 in which, in the thermosyphon mode, the refrigerant
circulates without any mechanical circulation.
14. The method of any one of claims 10 to 13 wherein operation in vapour compression mode
is at full capacity irrespective of cooling load, any excess capacity being utilised
to cool the thermal storage means.
15. The method of claim 14 wherein the mode of operation changes from i) vapour compression
mode to ii) thermosyphon mode on the thermal storage means reaching a condition where
it cannot be cooled further.
16. The method of any one of claims 10 to 15 wherein the thermal storage means absorbs
or rejects heat at substantially constant temperature.