[0001] This invention relates to a refrigerating apparatus for low-temperature refrigerated
counters, particularly counters for frozen and deep-frozen products.
[0002] A most widely used refrigerating fluid in refrigerating systems for temperatures
suiting the preservation of frozen or deep-frozen food is a mixture of isomers of
chloro-fluorocarbons available commercially under the trade name of Freon R502. The
use of Freon R502 is preferred on account of some thermodynamic features thereof.
Specifically, it can withstand large pressure fluctuations, as are required to reach
the low evaporation temperatures typical of display counters for deep-frozen food,
without involving excessive end-of-compression temperatures. For instance, end-of-compression
temperatures on the order of 180-200°C are met which do not affect the life span of
the compressor equipping the refrigeration circuit.
[0003] However, Freon R502, due to it tending to combine chemically with ozone, is regarded
as highly hazardous for the environment. In order to restrict this hazard, another
mixture, called Freon R22, is preferred.
[0004] On the other hand, Freon R22 is less suited to high compressions from the thermodynamic
standpoint, it producing, for example in traditional systems and for the same performance
level as Freon R502, excessively high end-of-compression temperatures (around 230-240°C)
for an acceptable life span of the compressor.
[0005] To obviate the technical problems brought about by the use of Freon R22, the current
technology offers two alternative approaches, specifically intended for industrial
type systems.
[0006] A first approach provides for the splitting of the target pressure fluctuation over
a number of serially connected compressors using a technique of so-called multi-stage
compression.
[0007] Another approach provides for the distribution of the target temperature fluctuation
between the refrigerated space and the outside in a number of ranges each controlled
by a respective refrigeration circuit. The circuits are operated at increasing temperature
ranges and are cascade coupled thermodynamically by means of common heat exchangers
wherein the refrigerating fluid of one circuit is condensed to a temperature close
to the evaporation temperature of the other cascade-connected circuit.
[0008] This technology has been somewhat wanting in efficiency, especially because of the
refrigerating fluid thermodynamic characteristics deteriorating when it is used for
operation in temperature ranges other than the steady state ones, and especially so
during the system starting transients.
[0009] These and other commonly encountered problems make it necessary to use electrical
compressors of a comparatively sophisticated type, such as open-type or scroll-type
compressors, wherein any heat transfer between the cooling system of the electric
motor driving the compressor and the refrigerating fluid being processed is avoided.
[0010] However, open-type compressors are cumbersome, expensive and complicated, and therefore
unsuited to such widely used articles as refrigerated counters. Accordingly, that
technology is only of interest to industrial systems, where the cost for solving the
problems posed by them can be more readily accommodated.
[0011] The technical problem addressed by this invention is that of fabricating refrigerated
display counters adapted to preserve frozen and deep-frozen products, being cooled
by a refrigerating apparatus which is conceived structurally and functionally to overcome
the drawbacks with which the cited prior art is beset.
[0012] This problem is solved according to the invention by a refrigerating apparatus for
refrigerated counters, characterized in that it comprises at least first and second
refrigeration circuits cascade connected to each other through a common heat exchanger,
each said circuit including at least one electric compressor of the sealed type.
[0013] Consequently, the invention stands, in a first and more general expression thereof,
on the use of sealed compressors in cascade-connected circuits filled with fluids
which have similar physical properties to those of Freon R22.
[0014] This circuit arrangement was regarded heretofore as unsuitable for use in relatively
low-grade installations, as are refrigerated counters, where sealed compressors would
be usually employed. This technical trend, which presently showed to be prejudicial,
is also due to theoretical considerations of vulnerability of the efficiency in the
terms set forth above; in fact, with sealed-type compressors, the refrigerating fluid
is also intended to cool the motor of the electric compressor, which result in added
detriment of the apparatus efficiency, especially during the cycle start transients.
It has been found, however, that such compressors may be conveniently used, the resulting
efficiency penalty being reasonable.
[0015] Vulnerability at the efficiency level of the apparatus, particularly during the start
transient, may be further fought by coupling the first circuit in the cascade (in
thermal contact with the refrigerated counter) both to the next circuit in the cascade
and directly to the environment by means of an additional condenser.
[0016] The invention will be now described in detail with reference to a preferred embodiment
thereof, shown by way of illustration and not of limitation in the accompanying drawings,
where:
Figure 1 is a schematical representation of a refrigerating apparatus embodying this
invention;
Figure 2 shows a partial cross-section through a display counter controlled by the
apparatus of Figure 1.
[0017] In the drawing figures, generally shown at 1 is a refrigerating apparatus according
to the invention, intended for cooling a refrigerated counter schematically shown
at 2 and only partly shown in Figure 2. In that figure, denoted by 23 is a counter
insulating structure which surrounds a vat 24 bordering the refrigerated space devoted
to preserving the products.
[0018] The apparatus 1 comprises first, second, and third refrigeration circuits, respectively
indicated at 3, 4 and 5.
[0019] The first circuit 3 comprises, serially connected together, a compressor 6 of the
sealed type, a condenser 7 of the coil-in-air type, and a de-watering filter 8, from
which there branch off two capillaries 9a and 9b in parallel, each supplying a respective
evaporator 10a,b. The evaporators 10a,b form each a part of a respective heat exchanger,
generally shown at 11a,b, wherethrough the first circuit 3 is cascade connected to
the second and third circuits 4, 5, respectively. In a preferred embodiment of this
invention, the heat exchangers 11a,b are thermally insulated externally using the
same insulating structure 23 as the counter 2 in which they are embedded.
[0020] The second and third circuits 4, 5 form the low-pressure circuit portion of the apparatus
1 relatively to the comparatively high-pressure portion represented by the first circuit
3. They are cascade connected to the first circuit 3 through their respective heat
exchangers 11a,b and are substantially identical with each other. Accordingly, only
one of them will be described in detail, similar parts of the other being denoted
by the same reference numerals with a suffix "a" for the second circuit and a suffix
"b" for the third.
[0021] The second circuit comprises a sealed compressor 18a, a main condenser 12a, and an
auxiliary condenser 13a wherebetween a de-watering filter 14a intervenes along with
a capillary 15a, followed by first and second evaporators, respectively indicated
at 16a and 17a.
[0022] The main condenser 12a is defined by an annular chamber of the heat exchanger 11a
formed between the outer skirt of the evaporator 10a of the first circuit and a tubular
conduit 19a extending coaxially outside it.
[0023] The auxiliary condenser 13a comprises a coil-in-air heat exchanger integral with
the condenser 7 and using the same fin formation and the same cooling fans 22. Relatively
to such fans and the airflow generated thereby, the condensers 13a,b locate downstream
from the condenser 7 of the first circuit.
[0024] The first evaporator 16a comprises a tubular coil partway embedded in the insulating
structure 23 of the counter 2 and being in heat transfer contact with the vat 24.
Accordingly, it provides heat transfer mainly by conduction with the preserved products.
[0025] The second evaporator 17a is suspended in the space to be refrigerated and mainly
intended for convective heat transfer. It is for this reason that it comprises a finned
heat exchanger.
[0026] The steady state operation of the refrigerating apparatus according to the invention
is as follows. The three refrigeration circuits 3, 4 and 5 are passed through by a
refrigerating fluid such as Freon R 22 flowing in the direction of the arrows. That
fluid is compressed, in the first circuit 3, by the compressor 6 from a pressure P1,
whose value is related to the evaporation temperature, to a pressure P2 related to
the condensation temperature.
[0027] The end-of-compression temperature reached by the refrigerating fluid is related
to the pressure fluctuation P1-P2, and as such, it can be held within acceptable values
for an adequate service life of the compressor 6.
[0028] The compressed and condensed refrigerating fluid is directed to its respective heat
exchangers 11a,b through the capillaries 9a,b. Where, as in the example shown, two
discrete circuit are used for the low-pressure circuit portion, the use of two separate
capillaries connected in parallel is preferred because it has been found that this
solution provide better balance of the thermal load on the low-pressure circuits.
[0029] The heat exchangers 11a,b are shared by the low-pressure circuit portion and the
high-pressure portion of the apparatus 1, wherefor they perform the condenser and
evaporator functions, respectively. Thus, the refrigerating fluid compressed by the
compressors 18a,b will be condensed at a lower temperature than room temperature having
a value close to the evaporation temperature in the evaporator of the first circuit
3.
[0030] As a result, as the condensed fluid is caused to evaporate in the evaporators 16a,b
and 17a,b due to lamination through the respective capillaries 15a,b, it will cause
the evaporators to cool to the target end temperature for preservation of the products
introduced into the vat 24 of the counter 2.
[0031] The auxiliary condensers 13a,b bear little influence at this stage of the apparatus
steady state operation, since the end-of-compression temperature reached by the refrigerating
fluid at the outlet of the compressors 18a,b is comparatively close to the average
temperature of air at the outlet of the condenser 7.
[0032] Such auxiliary condensers operate instead at full capacity during the starting transient
of the apparatus, when the three circuits all operate at a starting temperature which
is close to room temperature.
[0033] Under these conditions, the output from the refrigerating fluid, which is inherently
related to the operating temperature, will deteriorate. This deterioration only appears
in the low-pressure circuit portion, making the heat transfer rate achieved in the
heat exchangers 11a,b insufficient, under the same pressure fluctuation and size of
the remaining elements of each circuit, for the apparatus to gradually attain balanced
operation of the high- and low-pressure circuit portions.
[0034] The auxiliary condensers serve to provide, during this starting transient of the
apparatus, a further means of dissipating heat as necessary to accommodate this temporary
loss of efficiency.
[0035] Among the principal advantages afforded by this apparatus is that it can ensure good
refrigerating efficiency accompanied by adequate life of its components and improved
environmental safeguard. Furthermore, the apparatus is suited to such widely used
articles as refrigerated display counters. Advantageously, the proposed configuration
affords appreciable savings in space, thereby the apparatus can find room beneath
the insulating structure which borders the vat of a refrigerated counter. Contributive
to such space savings is the embedding of the heat exchangers which interconnect thermally
the low- and high-pressure circuit portions in said insulating structure. This has
the added advantage of providing optimum insulation for said heat exchangers at no
cost.
1. A refrigerating apparatus for refrigerated counters, characterized in that it comprises
at least first (3) and second (4,5) refrigeration circuits cascade connected to each
other through a common heat exchanger (11a,b), each said circuit including at least
one electric compressor (6;18a,b) of the sealed type.
2. A refrigerating apparatus according to Claim 1, wherein said common heat exchanger
comprises two coaxial pipes respectively forming the evaporator (10a,b) for said first
refrigeration circuit and the condenser (12a,b) for said second circuit.
3. A refrigerating apparatus according to Claim 2, wherein the innermost pipe of said
common heat exchanger is the evaporator for said first circuit and the outermost pipe
is the condenser for said second circuit.
4. An apparatus according to Claim 1, wherein cascade connected to said first circuit
(3) through respective heat exchangers (11a,b) are plural refrigeration circuits in
parallel with one another (4,5), said first circuit comprising, for each heat exchanger
in said cascaded refrigeration circuits, a respective discrete lamination means (9a,b).
5. An apparatus according to Claim 1, wherein said at least one second circuit comprises
a main condenser (12a,b) and an auxiliary condenser (13a,b) in series with each other.
6. An apparatus according to Claim 5, wherein said auxiliary condenser (13a,b) in said
second circuit is set close against a condenser (7) in the first circuit.
7. An apparatus according to Claim 6, wherein said condenser and auxiliary condenser
are in-air condensers integral with a single finned sink.
8. A refrigerated display counter (2) cooled with a refrigerating apparatus according
to one or more of the preceding claims.
9. A refrigerated display counter according to Claim 8, comprising an insulating structure
(23) wherein said common heat exchanger (11a,b) is embedded at least partway.