BACKGROUND OF THE INVENTION
1. Field of the Invention
[0001] The present invention relates to a refrigerating apparatus which can be advantageously
used in an air conditioning device for an automobile. The present invention is also
related to a modulator used in the refrigerating apparatus.
2. Description of the Related Art
[0002] Known in the prior art is a refrigerating device provided with a condenser and a
receiver arranged downstream of the condenser. The top end of the receiver is provided
with an inlet for introducing therein a condensed coolant from the condenser, and
the coolant is stored in a space inside the receiver. In this case, a liquid phase
is created below in the space at the liquid-gas interface, and the obtained liquid
coolant is fed to a pressure-reducing means for the refrigerating apparatus.
[0003] This prior art suffers from a drawback in that all of the amount of coolant for recirculation
in a refrigerating cycle must be introduced into a receiver, and a result, in this
prior art, an introduction or removal of a large amount of coolant must continuously
occur, and thus the dimensions of the receiver are inevitably greatly increased.
[0004] Another prior art refrigerator is provided with a condenser constituted by an upper
condenser part and a lower super cooling part, and a receiver is arranged between
the condenser part and the super cooling part. The coolant condensed at the condenser
part is temporarily stored in the receiver, for a gas-to-liquid separation therein,
and only the liquid coolant separated in the receiver is returned to the condenser
at the super cooling part thereof.
[0005] This improved prior art also has a construction such that all of the amount of the
coolant recirculated during the refrigerating cycle is introduced from the condenser
part into the receiver, and all of the amount of liquid coolant is removed to the
super cooling portion of the condenser, and this has a drawback in that the dimensions
of the system must be large. Furthermore, connection lines for a communication between
the condenser part and super cooling part of the condenser and the receiver are necessary,
which makes the construction of the system complicated and difficult to arrange in
a limited space in an automobile.
SUMMARY OF THE INVENTION
[0006] An object of the present invention is to provide an apparatus capable of overcoming
the above-mentioned difficulties in the prior arts.
[0007] Another object of the present invention is to overcome these difficulties in the
prior arts by providing, in place of the conventional receiver, a small-size modulator
as the means for storing an excess amount of the coolant recirculated during the closed
refrigerating cycle.
[0008] Still another object of the present invention is to provide a refrigerating system
having a modulator for use in a refrigerating cycle and having a construction such
that it is capable of storing a optimum amount of excess coolant.
[0009] A further object of the present invention is to provide a refrigerating system equipped
with a modulator and capable of obtaining an as high as possible cooling ability of
the system by the provision of a super cooler arranged downstream of the modulator
in the direction of the flow of the coolant.
[0010] Further, another object of the present invention is to provide a refrigerating system
having a super cooling ability due to the provision of a modulator having a simplified
construction.
[0011] According to the present invention, a refrigerating apparatus is provided which comprises:
a coolant recirculation line;
a compressor in the recirculation line for compressing the coolant;
a condenser in the recirculation line for condensing the compressed coolant;
means in the recirculation line for expanding the condensed coolant by reducing
the pressure thereof;
an evaporator in the recirculation line for evaporating the reduced pressure coolant,
which is introduced into the compressor, so that a flow of the coolant as recirculated
in the recirculation line is created to thereby obtain a refrigerating cycle, and;
a modulator defining therein a chamber for receiving, from the condenser, only
a part of the total amount of the coolant recirculated in the refrigerating cycle,
the modulator being capable of defining in said space a boundary between the liquid
and gas states, for separating the gas from the coolant.
[0012] According to the present invention, the modulator does not receive all of the coolant
recirculated in the refrigerating cycle. Namely, any excess amount of coolant is introduced
into the modulator. This excess amount of the coolant in the modulator is changed
in accordance with the cooling ability, as required, and in accordance with variations
in the excess amount of coolant, the coolant in the modulator is supplied to the recirculation
system or an excess amount of coolant is supplied to the modulator.
[0013] Preferably, the modulator has a volume capable of storing the maximum possible excess
amount of the coolant for the refrigerating system, to thereby allow a reduction in
the size of the system.
[0014] Furthermore, because the modulator is arranged between the condenser and the super
cooler, a good super cooling ability is obtained, and because a gas-liquid boundary
is created in the modulator in which the excess amount of the coolant is stored, only
a liquid state coolant is supplied to the super cooler. Namely, merely by arranging
the modulator, which is branched from the heat exchanger, in the system, a more efficient
super cooling operation can be obtained and a difference in the enthalpy can be increased,
resulting in an increase in the cooling ability of the refrigerating system.
[0015] Finally, a combined construction of the condenser and the super cooler allows the
modulator to be merely branched from the heat exchanger at the middle portion thereof,
and thus the modulator can be small in size, and accordingly, the condenser and the
super cooler can be made more compact.
BRIEF EXPLANATION OF THE DRAWINGS
[0016]
Fig. 1 is a schematic representation of a refrigerating system according to the present
invention;
Fig. 2 is a front elevational view of the condenser and a modulator used in Fig. 1;
Fig. 3 shows a condition of the coolant in the modulator wherein a medium (proper)
amount of coolant is located in the modulator;
Fig. 4 shows a condition of the coolant in the modulator wherein the modulator is
occupied substantially only by a gas state coolant;
Fig. 5 shows a condition of the coolant in the modulator wherein the modulator is
completely filled by a liquid state coolant;
Fig. 6 is an enlarged view of the upper part of the modulator, in a modification thereof;
Fig. 7 is a schematic view of refrigerating system of the prior art;
Fig. 8 shows a Mollier diagram illustrating a super cooling, wherein the cooling recirculating
system is shown as imposed;
Fig. 9 is a view for explaining an operation of a system according to the present
invention provided with a modulator between the condenser portion and the sub-cooling
portion;
Fig. 10 is a schematic view of the cooling system in an automobile provided with a
heat exchange device having a modulator branched therefrom at the middle portion thereof;
Fig. 11 is a detailed view of the branched portion of Fig. 11;
Fig. 12 is a schematic view of the heat exchanger having a modulator branched therefrom,
for a definition of a ratio of areas between the condenser portion and sub-cooling
portion;
Fig. 13 is a graph showing a relationship between a sub-cooling portion area ratio
to the engine idling speed and to the compressor drive power;
Figs. 14(a) to (c) show a cooling ability ratio, drive power ratio, and a cooling
ability-drive power ratio, respectively, of the present invention over the prior art
construction, with regard to various cooling load conditions;
Fig. 15 is a diagrammatic view of the heat exchanger for illustrating a super cooling
operation at the sub-cooling portion;
Fig. 16 shows a relationship between the area ratio (A'/A) of the branch pipe to the
modulator and a gas state coolant flow-out ratio;
Fig. 17 illustrates a change in a condition of a separation of gas state coolant in
the modulator, with or without a limiting means;
Fig. 18 schematically shows a modulator provided with an air induction pipe;
Fig. 19 shows the relationship between the branch pipe area ratio and the effective
sub-cooling area ratio r₀;
Fig. 20 illustrate a filling margin portion and variation margin portion provided
in the modulator;
Fig. 21 illustrate a relationship between a rotational speed of the compressor and
the amount of coolant in the modulator, with regard to various vehicle running conditions;
Fig. 22 is a dismantled, perspective view of the modulator in the system shown in
Fig. 10;
Fig. 23 is a cross sectional view of an upper joint in the modulator in Fig. 22;
Fig. 24 is a cross sectional view of a lower joint in the modulator in Fig. 22;
Fig. 25 shows a relationship between the amount of coolant filled in the refrigerating
recirculating system and the output pressure of the compressor;
Fig. 26 is a schematic front view of the heat exchanger in another embodiment of the
present invention;
Fig. 27 is a detailed view of a modulator in Fig. 26;
Fig. 28 is side view of the heat exchanger, and illustrates the modulator with respect
to the tank of the heat exchanger;
Fig. 29 illustrates an arrangement of the heat exchanger provided with a modulator
in Fig. 26, in an engine room of a vehicle;
Fig. 30 shows a relationship between the time lapsed and a temperature in a passenger
room and a temperature of blown out cooling air;
Fig. 31 shows another modification of a modulator provided with an induction pipe
for an introduction of a gas state coolant to the modulator from a tank of the heat
exchanger;
Fig. 31' is cross sectional view taken along the line 31'-31' in Fig. 31;
Fig. 32 is cross sectional view of the induction pipe in Fig. 31;
Fig. 33 is a schematic view of a portion of a pipe for connection to the tank of the
heat exchanger;
Fig. 34 shows another embodiment provided with a joint means between the coolant passageway
and induction pipe;
Fig. 35 diagrammatically illustrates a condition of a coolant in the upper portion
of the modulator when an insufficient amount of coolant is filled in the modulator;
Fig. 36 shows an inside of the modulator as viewed via a sight glass at the upper
end of the modulator in the coolant condition as shown in Fig. 35;
Fig. 37 diagrammatically illustrates a condition of the coolant in the upper portion
of the modulator when a proper amount of coolant is filled in the modulator;
Fig. 38 shows the inside of the modulator as viewed via a sight glass at the upper
end of the modulator in the coolant condition as shown in Fig. 37;
Fig. 39 diagrammatically illustrates a condition of the coolant in the upper portion
of the modulator when an excess amount of coolant is filled in the modulator;
Fig. 40 shows the inside of the modulator as viewed via a sight glass at the upper
end of the modulator in the coolant condition as shown in Fig. 39;
Fig. 41 is a vertical cross sectional view of a modification of the modulator, wherein
a sight glass is provided at the side wall thereof;
Fig. 42 is a vertical cross sectional view of another modification of the modulator,
wherein an upper end of the induction pipe is angled;
Fig. 43 shows another embodiment of the present invention wherein the side tank and
the modulator are combined;
Fig. 44 is a prior art construction of a heat exchanger provided with a super cooler;
and
Fig. 45 shows still another embodiment of the present invention, which is similar
to Fig. 43 but having differences in the construction for a communication of the tank
with the modulator.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0018] Embodiments of the present invention will be described with reference to the attached
drawings.
[0019] Figure 7 shows a prior art system provided with a condenser 400 and a receiver 401
arranged downstream of the condenser. The top end 403 of the receiver 401 is connected
to the condenser 400, and the coolant from the condenser 400 is once stored in the
receiver 401. This prior art suffers from a drawback in that all of the coolant for
recirculation is introduced into the receiver 401 and stored therein, and thus a continuous
introduction or removal of a large amount of coolant must be made, and accordingly,
the dimensions of the receiver 401 are inevitably increased. Another disadvantage
is that two pipes necessary for a connection of the condenser 400 to the receiver
401, which makes the construction of a joint portion complicated.
[0020] Figure 44 shows another prior art refrigerator which is provided with a condenser
400 constructed by an upper condenser part 402 and a lower super cooling part 405,
wherein a receiver 401 is arranged between the condenser part 402 and the super cooling
part 405. The coolant condensed at the condenser part 402 is temporarily stored in
the receiver 401 for a gas-to-liquid separation, and only the liquid coolant, after
separation in the receiver 401, is returned to the condenser at the super cooling
part 405. Also in this prior art construction, however, all of the coolant recirculated
during the refrigerating cycle is introduced from the condenser part 402 into the
receiver 401, and all of the liquid coolant is removed to the super cooling portion
405, and thus the dimension of the system inevitably are large, and further, the joint
construction of the system is complicated.
[0021] Figure 1 shows a system illustrating a refrigerating cycle according to the present
invention. In the drawing, 200 denotes a compressor having a pulley 200-1 connected
to a crankshaft (not shown) of an internal combustion engine via a belt (not shown),
whereby the compressor 200 is driven by the engine. The compressor 200 has an output
connected, via a coolant pipe 350, to an inlet 400-1 of a condenser 400, for an introduction
of a coolant having a high pressure and a high temperature from the compressor 200
into the condenser 400. A heat exchange then takes place in the condenser 400 between
the coolant and the outside air, to thereby liquefy the coolant, which is discharged
under a high pressure from the outlet 400-2 of the condenser and is introduced into
an expansion valve 300, as a pressure reducing means, via a coolant pipe 351. In this
embodiment, the expansion valve 300 as the pressure reducing means is a thermally
operated type responsive to signals from a thermosensitive tube 311, for controlling
a degree of throttling of the pipe 351. A pressure reduction takes place at the expansion
valve 300, causing the coolant to be expanded and formed into a mist, and then supplied
to an evaporator 310. The evaporator 310 is arranged in a air conditioning device
(not shown) for a passenger room of an automobile, so that a heat exchange takes place
between the coolant in the evaporator 310 and the air to be air-conditioned, which
causes the coolant to be vaporized to thus extract heat from the air to cool same,
as is well known.
[0022] The evaporated coolant having a low temperature and a low pressure is recirculated
into the compressor 200 via a coolant pipe 352.
[0023] According to the present invention, a modulator 100 is arranged in the coolant pipe
351 at a position adjacent to the outlet of the condenser 400. As shown in Fig. 2,
the modulator 100 has a closed space S therein which extends vertically in such a
manner that the coolant pipe 351 near the outlet 400-2 of the condenser 400 is directly
and vertically upwardly branched to the space S of the modulator 100 at the bottom
end thereof. As shown in Fig. 2, the condenser 400 is composed of a heat exchange
tube 420 made from a extrusion pipe having a serpentine shape, through which the coolant
passes after the heat exchange. Furthermore, corrugated fins 421 are thermally connected
to the outer surface of the serpentine tube 420, to thus increase a heat exchange
space between the coolant and the air due to the presence of the corrugated fins 421.
As shown in Fig. 2, the condenser 400 is a twin type having two "parallel" serpentine
tube portions 420a and 420b connected with each other at the upstream ends thereof
by a dividing member 422, so that two parallel flows of the coolant are obtained.
The downstream ends of the parallel tube portions are connected with each other by
a combining member 423, to combine same and produce a single flow of the coolant to
the pipe 351 and the expansion valve 300.
[0024] As shown by Fig. 2, basically the total amount of the coolant passed through the
condenser 400 is directed to the expansion valve 300. Nevertheless, any excess coolant
should be held in the system, to avoid a situation such that, when the amount of coolant
in the system is larger than the required amount, a leakage of the coolant occurs
and the total amount of the coolant is reduced, and thus a change occurs in the amount
of the coolant necessary to cope with changes in an air conditioning load. The space
S in modulator 100 is utilized for holding the excess coolant, and is arranged downstream
of the condenser 400 such that the branching portion 360 allows the coolant condensed
in the condenser 400 to be diverted from the pipe 351, and thus the excess coolant
can be accumulated in the modulator 100.
[0025] Figure 3 to 5 show various states of the distribution of the coolant in the space
S in the modulator 100. Under a normal condition, the excess coolant is located in
the modulator 100, whereby a gas-to-liquid boundary is created in the modulator 100.
Namely, in the state shown in Fig. 3, the introduction of vaporized coolant into the
modulator 100 and the removal of the liquefied coolant from the modulator 100 are
balanced, whereby a stabilized level of the liquid coolant is created inside the modulator
100. This level corresponds to the amount of coolant in excess of the usual condition
of the air-conditioning system.
[0026] When a state exists wherein a shortage in the amount of the coolant occurs due to
a leakage of the coolant or an increase in the required air-conditioning load, all
of the coolant in the condenser cannot be liquefied, and thus a large amount of gaseous
coolant is introduced into the modulator 100, causing the liquid state coolant to
be discharged into the coolant pipe 351 and the level of the liquid phase in the modulator
to be lowered, as shown in Fig. 4. Namely, a shortage in the amount of coolant in
the recirculating system is supplemented by feeding the coolant stored in the modulator
100 into the system.
[0027] Conversely, when there is an excess amount of coolant in the refrigerating system
or when there is a reduction of an air conditioning load, a sufficient amount of the
coolant can be condensed in the condenser 400, and accordingly, substantially no gaseous
coolant is fed into the pipe 351 toward the expansion valve 300 and only a liquid
state coolant is introduced into the modulator 100, and thus the space inside the
modulator 100 is completely filled with the liquid state coolant, as shown in Fig.
5. Namely, an amount of coolant in excess of the amount of coolant needed for the
recirculation system can be stored in the modulator 100, and thus the amount of recirculated
coolant can be suitably adjusted in accordance with the air conditioning requirements.
[0028] Figure 6 shows a modification of the modulator 100, wherein the upper end of the
modulator 100 is equipped with a sighting member 190 made of a transparent material
such as glass, which allows an inner condition of the modulator 100 to be observed,
and as a result a shortage in the amount of coolant or an excessively filled condition
of coolant can be detected. In the construction in Fig. 6, a float member 180 is housed
in the modulator 100, to facilitate the observation of the level of the liquid-to
gas boundary. The sighting glass member 190 is fitted to the upper end of the modulator
100 via an O-ring 198, and portions of the outer thin tubular wall constructing the
modulator 100 are radially inwardly deformed along the circumference thereof, so that
the sighting glass 190 is firmly held in the tubular member constructing the modulator
100.
[0029] As described above, with the modulator 100 of the present invention, any change in
the amount of recirculating cooling medium required can be automatically compensated.
Furthermore, the coolant is introduced into or fed from the modulator 100 at a limited
speed, to ensure a stable condition of the coolant in the modulator 100, which is
advantageous because the volume of the modulator 100 can be made as small as possible.
[0030] Similar to the prior art shown in Fig. 44, it is possible to divide the condenser
into two portions, and to arrange the receiver 400 therebetween, for generating the
gas to liquid boundary, whereby the portion downstream of the receiver 400 can be
operated as a super cooler. Figure 8 shows a Mollier diagram wherein the abscissa
shows the enthalpy and the ordinate shows the pressure; the solid line 11 and 12 show
the saturated gas and liquid states, respectively. As is well known, the area inward
of the lines 11 and 12 corresponds to the area wherein the gas and liquid states coexist,
the area on the right hand side of the line 11 corresponds to the area wherein only
the gas state exists, and the area on the left hand side of the line 12 corresponds
to the area wherein only the liquid state exists. Note, the receiver 401 should be
located on the saturated line 12, and therefore, a super cooling will take place in
the area SC of the condenser 400 downstream of the receiver 401. This super cooling
can increase the difference in the value of the enthalpy, and thus increase the cooling
efficiency of the refrigerating apparatus.
[0031] Figure 9 is a schematic view of the refrigerating apparatus wherein the modulator
100 according to the present invention is used in place of the receiver 401 of the
prior art. As shown in Fig. 9, a gas-liquid boundary also can be created in the modulator
100 such that the coolant is in a saturated liquid state at a position where the modulator
100 is located, and as a result, the heat exchanger located downstream of the modulator
100 serves as a sub cooling portion 405, i.e., as a super cooler, and the portion
402 of the heat exchanger located upstream of the modulator 100 serves as a condenser.
[0032] Note, the condensed condition of the medium in the condenser portion 402 depends
on the cooling load. In the condenser portion shown in Fig. 9, the area designated
by dots is in a gas state and the area designated by spaced short bars is in a liquid
state. In the areas shown by oblique lines, the gas and liquid states occur in accordance
with the required cooling load. Such changes in the condensing ability at the condenser
portion 402 can be absorbed by the provision of the modulator 100. Namely when a situation
occurs in which the cooling load is so high that all of the coolant cannot be condensed
in the condenser portion 402, a discharge of an amount of gaseous coolant occurs.
This gaseous coolant however, is absorbed by the modulator 100, and accordingly, a
liquid state coolant in the modulator 100 is discharged to the sub-cooling portion
405, whereby an effective super cooling operation is obtained at the sub-cooling portion
405.
[0033] Figure 10 shows the entire air conditioning system for an automobile, which system
is provided with a condenser having the construction schematically shown in Fig. 9
wherein a modulator 100 is arranged between the condenser part 402 and the super cooler
405 in the condenser 400. Reference numeral 201 denotes an internal combustion engine
having a crankshaft on which a pulley 201-1 is mounted. The pulley 201-1 is connected,
via a belt 201-2, to a pulley portion of an electromagnetic clutch device 202, and
the clutch 202 is selectively engaged for transmitting the rotational movement of
the engine to the compressor 200. In the embodiment shown in Fig. 10, the condenser
portion 402 is a parallel twin type having parallel-connected serpentine pipes 420a
and 420b which are connected to each other at a manifold 423. The modulator 100 is
branched from the manifold 423 such that it is directed upward therefrom. Namely,
the manifold 423 is provided with four branch portions; two being connected to the
serpentine pipes 420a and 420b of the condenser portion 402, one being connected to
the sub cooling portion 405, and one being connected to the modulator 100 as shown
in Fig. 11.
[0034] Figure 12 is a schematic view of a construction of the heat exchanger 400 shown in
Fig. 10. In this type of heat exchanger 400, the provision of the modulator 100 allows
the portion 402 downstream of a position branched to the modulator 100 to act as a
condenser part for condensing the coolant. The portion 405 downstream of the position
branched to the modulator 100 operates as a sub-cooling portion, to thereby obtain
a super cooling effect.
[0035] In the embodiment of the heat exchanger 400 wherein the modulator 100 is branched
from an intermediate portion thereof, the determination of a desired position at which
modulator will be branched therefrom is discussed in relation to the results of experiments.
In Fig. 12, assuming that the total surface area of the heat exchanger is 1, and the
surface area of the sub-cooling portion is r, the optimum position for the branching
the modulator 100 is determined by changing the ratio of the surface area of the sub-cooling
portion r to the total surface area. In Fig. 13, the abscissa is a value of the sub-cooling
area ratio r, and the ordinate shows an engine idling speed or drive power for the
compressor (hose power). The measurement is carried out under a condition in which
the temperature of air introduced into the evaporator 310 is 35 degrees centigrade,
the relative humidity is 60%, the flow amount is 500 cubic meter per hour, the temperature
of air introduced into the heat exchanger 400 is 40 degrees centigrade, and the wind
speed is 2 meters per second. A line ml shows a change made in the drive power for
the compressor 200 with respect to the change in the ratio r, to thereby obtain a
cooling ability equal to that obtained when the sub-cooling ratio is zero. As shown
by a line n1, a change in an engine idling speed is measured when the ratio r is changed,
to thereby obtain a cooling ability equal to the cooling ability under the zero sub-cooling
condition. The drive power ml for the compressor 200 was calculated from the line
n1, in a well known manner.
[0036] When the sub-cooling portion 405 has a large area, the super cooling speed of the
coolant can be made high, and therefore, as it will be easily understood from the
Mollier chart shown in Fig. 8, a large difference in the enthalpy can be obtained,
and thus the cooling ability can be increased. Basically, this means that the larger
the sub-cooling area the greater the cooling ability, enabling a reduction in the
drive power while maintaining the same cooling ability.
[0037] Nevertheless, an increase in the area of the sub-cooling portion 405, while maintaining
a constant value of the area for a heat emission by the heat exchanging device 400,
causes a reduction of the area of the condenser portion 402. This means that it is
necessary to use the small area for heat emission to liquidize the coolant, which
causes the pressure of the coolant at the condenser portion 402 to be increased. Such
an increase in the coolant pressure at the condenser portion 402 brings an adverse
effect, in that the drive power for the compressor 200 must be increased.
[0038] Figure 13 shows this contradictory requirement between the increase in the cooling
ability by an increase in the area of the sub-cooling portion 402 and the prevention
of an increase in the drive power for the compressor due to a reduction of the area
of the compressor portion 402. Generally speaking, a higher value of the sub-cooling
ratio r is more preferable, but as is clear from Fig. 13, the value of the sub-cooling
ratio cannot be higher than 0.1 if a substantial reduction of the drive power of the
compressor 200 is to be obtained.
[0039] Figure 13 also shows a change in the drive power of the compressor needed to obtain
a predetermined cooling ability when the engine is idling. The engine to which the
compressor 310 is connected is subjected to various running conditions by which the
engine speed is determined regardless of the cooling ability requirements. Therefore,
it is necessary to determine the desired value of the sub-cool area while the vehicle
is actually running.
[0040] Figures 14(a), (b) and (c) show the values of the cooling ability (Q), drive power
(L), and the cooling ability-to-drive power ratio (Q/L), respectively, obtained by
the heat exchanger according to the embodiment shown in Fig. 10, provided with a super
cooler, in relation to those obtained by a heat exchanger without a super cooler (Fig.
1). In each of Figs. 14(a), (b) and (c), a solid line A corresponds to a high speed
condition of the vehicle, and a high thermal load applied to the refrigerating apparatus.
In more detail, under the condition A, the temperature of the air introduced into
the evaporator 310 is 35 degrees centigrade, the total air amount is 500 cubic meters
per hour, and the rotational speed of the engine 201 is 3,600 r.p.m. A solid line
B corresponds to a medium speed condition of the vehicle, and a medium thermal load
applied to the refrigerating apparatus. In more detail, under the condition B, the
temperature of the air introduced into the evaporator 310 is 27 degrees centigrade,
the total air amount is 400 cubic meters per hour, and the rotational speed of the
engine 201 is 1,800 r.p.m. Finally, a solid line C corresponds to a low speed condition
of the vehicle, and a low thermal load applied to the refrigerating apparatus. In
more detail, under the condition C, the temperature of the air introduced into the
evaporator 310 is 25 degrees centigrade, the total air amount is 300 cubic meters
per hour, and the rotational speed of the engine 201 is 1,000 r.p.m. As previously
explained, in general an increase in the cooling ability is obtained by an increase
in the area of the sub-cooling portion 405, but this increase in the sub-cooling area
causes an increase in the drive power due to an increase in the pressure of the coolant
at the condenser portion 402. This means that an optimum value of the cooling ability-to-drive
power ratio (Q/L) should be determined from the cooling ability and the drive power.
The results of the experiments show that, when the vehicle is operating under the
low speed and low load area C, a sub-cooling area ratio larger than 0.3 can cause
a worsening of the cooling ability compared to that obtained without a provision thereof,
since the sub-cooling area ratio becomes smaller than a value of 1.0.. Therefore,
preferably the sub-cooling area ratio r is in a range of between 0.1 and 0.3, to thereby
obtain an effective operation of the refrigerating apparatus over the entire range
of operation of the vehicle.
[0041] The inventors also found that, to obtain a proper super cooling operation at the
sub-cooling portion 405, the condensing operation at the modulator 100 is important.
In Fig. 15, a flow of the air for cooling is contact with not only the condenser and
sub-cooling portions 402 and 405 but also the modulator 100, which causes the gaseous
cooling medium to be condensed therein. In this case, the gas-liquid boundary 100a
at the modulator 100 is under a saturated liquid condition, which is obtained as a
result of cooling operation due to a heat emission at the modulator 100. Namely, even
if the coolant introduced into the modulator 100 is in a partly dried state of a gas
and liquid as combined, the cooling effect caused by the heat emission at the modulator
100 itself can maintain the gas-liquid boundary 100a in the modulator 100. In more
detail, the coolant at the connection area 100b is under the combined state wherein
the coolant is basically in a liquid state but includes a small amount of gas. Nevertheless,
an equalized state can be obtained inside the modulator 100, and as a result, the
condition of the coolant at the inlet portion 405a of the sub-cooling portion 405
is the same as the condition of the coolant at the inlet portion 100b of the modulator
100, and thus the coolant in the liquid state including a small amount of gas is introduced
into the sub-cooling portion 405. Therefore, at the sub-cooling portion 405, a condensing
operation of the gas portion in the combined gas and liquid medium is first obtained,
and thereafter, the super cooling operation is obtained. In Fig. 15, the coolant can
obtain the saturated condition along the area D, and thus the super cooling operation
is obtained in the sub-cooling portion 405 at an area downstream of the line D, as
designated by the shaded lines.
[0042] As explained above, the heat emission at the modulator 100 reduces the effective
area for super cooling at the sub-cooling portion 405. A gas flowing-out ratio, in
the total amount of the gas component in the coolant passed through the condenser
portion 402, is defined as a ratio between the amount of gas introduced into the modulator
100 and the amount of gas flowing into the sub-cooling portion 405. Namely, where
there is an emission of heat at the modulator 100, the amount of gas flowing into
the sub-cooling portion 405 is equal to the amount of gas condensed at the modulator
multiplied by the gas flow rate. This means that the amount of gaseous coolant flowing
into the sub-cooling portion 405 corresponds to the degree of condensing at the modulator
100. Namely, the larger the amount of gas phase coolant in the modulator 100, the
smaller the amount of gas phase coolant flowing into the sub-cooling portion 405,
which increases the super cooling efficiency at the sub-cooling portion 405.
[0043] In view of the above, the gaseous coolant must be positively introduced into the
modulator 100. In Fig. 15, A is a value of effective area of the coolant passageway,
and A' is a value of effective area of the branch passageway to the modulator 100.
In this case, the amount of gaseous coolant introduced into the modulator 100 is equal
to the amount of gaseous coolant passing through the coolant multiplied by A'/A. Namely,
the gas flowing out ratio corresponding to A'/(A - A'), so that the larger the effective
area of the branch pipe of the modulator 100, the smaller the amount of gaseous coolant.
[0044] When the effective area A' of the branch pipe to the modulator 100 is too large,
however, the flow speed of the coolant in the modulator 100 becomes too high, and
it becomes difficult is separate the gas state coolant from the flow of the coolant,
and thus the gaseous coolant flow out ratio becomes large. Figure 16 shows a relationship
between the ratio of the effective area of the branch pipe to the modulator 100, to
the effective area of the coolant passageway, A'/A, and the gaseous coolant flow out
ratio. As will be easily understood, a suitable value of the A'/A must be selected
to obtain the desired result.
[0045] Figure 17 is a schematic view of the condition of the coolant at the branch portion
to the modulator 100. The upper part (a) of Fig. 17 show a situation wherein the branch
pipe to the modulator 100 has no means for controlling the flow into the modulator
100, and it is clear that an excessively high speed flow of the coolant in the coolant
passageway at the branch portion to the modulator 100 is generated, which causes a
separation of the gas state coolant by a buoyancy thereof to become difficult. The
lower part (b) of Fig. 17 shows a situation wherein a speed limiting means 100-c (plate
with openings) is provided for a separation of the flow of gas to the branch pipe
to the modulator. This limitation of the speed of the coolant flowing into the modulator
100 by the plate 100c facilitates the separation of gas in the modulator 100 due to
the buoyancy thereof.
[0046] Figure 18 shows an embodiment in which the above explained provision of separate
flows is introduced. The branch pipe 423 is provided therein with a partition 423-1,
which forms an opening for a connection with an introduction pipe 120 having an effective
area of A', the value of which is determined so that a desired introduction of the
gaseous coolant is obtained. The partition wall 423-1 forms openings 424 to ensure
a continual connection with the bottom portion of the modulator 100. Figure 16 shows
that, to obtain an effective super cooling operation, the ratio A'/A should not be
too large and should not be too small. The following is a result of an experiment
made to confirm this finding. In Fig. 19, the abscissa is the ratio A'/A, which is
the ratio of the area of the pipe 120 to the area of the coolant passageway in which
the coolant flows as shown by an arrow Y, and the ordinate is the effective area of
the sub-cooling portion 405, or, which is the ratio r₀ of the area of the sub-cooling
portion producing an effective super cooling operation (the shaded line area in Fig.
15) to the total effective area of the sub-cooling portion 405 of the heat exchanging
apparatus. A solid line E shows a situation wherein the amount of coolant recirculating
in the refrigerating system is 100 kg per hour, and a solid line F is a situation
wherein the amount of coolant recirculating in the refrigerating system is 150 kg
per hour. The effective sub-area ratio A'/A indicates, with regard to the total effective
heat exchange surface area, a rate of a surface area of the part of the sub-cooling
portion where an effective super cooling of the coolant is obtained. This means that
the larger the sub-cooling area ratio A'/A, the more effective is the super cooling
effect. The experimental result in Fig. 19 shows that a large effective sub-cooling
area ratio can be obtained when the branch pipe area ratio A'/A is in a range of between
12 to 36%.
[0047] Note, in the embodiment shown in Fig. 18, the induction pipe 120 is arranged to be
opened to the space inside the modulator at the upper portion thereof, and as a result,
in addition to the advantage of a setting of the desired value of the branch pipe
area ratio, an additional advantage is obtained in that a degree of dryness of the
gas-liquid coolant at the branch position is reduced because the gaseous coolant is
directly introduced into the upper part of the space inside the modulator 100.
[0048] A desired volume of the modulator will now be discussed with reference to Fig. 20,
which shows a schematic construction of the modulator 100. The modulator 100 should
be constructed by a lower filling margin portion 131 below the gas-to-liquid boundary
and an upper variation margin portion 130 above the gas-to-liquid boundary. The lower
portion 131 is used for supplementing an amount of the coolant which may leak from
the refrigerating apparatus after a prolonged use thereof, and the upper portion 130
is used for absorbing a change of the necessary amount of coolant recirculated in
the refrigerating apparatus, which depends on variations of the cooling load of the
system. A value of 100 grams is usually required for the volume of the filling margin
portion 131, but a preferable value of the variation margin portion 120 was not known,
and therefore, experiments were carried out by the inventors of the present invention.
In these experiments, the refrigerating apparatus is operated under various operating
conditions, to obtain an amount of the coolant held in the modulator 100. Figure 21
shows the result of these experiments. In Fig. 21, the abscissa is a rational speed
of the compressor, and the ordinate is an amount of the coolant in the modulator 100.
In Fig. 21, a solid line I is a low load coolant condition where the temperature is
15 degrees centigrade and the humidity is 50%, a solid line H is a medium load condition
where the temperature is 27 degrees centigrade and the humidity is 50%, and a solid
line G is a high load condition where the temperature is 35 degrees centigrade and
the humidity is 60%. As will be clear from Fig. 5, over the entire range of the engine
load, the amount of coolant required is between 90 to 140 grams. As already explained,
to fill the margin portion 131, 100 grams of coolant are required, and therefore,
for the variation margin portion 130 it is considered that a space for about 40 grams
of coolant is required.
[0049] In view of the result of the above experiments, the inventors found a preferable
construction of the modulator 100, which is connected to a refrigerating system for
an operation thereof. The actual construction of the modulator 100 will be explained
as follows. As shown in Figs. 10 and 11, a construction is employed whereby the modulator
100 is branched from the manifold pipe 423, which is shown on an enlarged scale in
Fig. 22, and from the manifold pipe 423, tubes 420-1 and 420-2 to the condenser portions
402 and a tube 421-2 to the sub-cooling portion 405 are branched. Furthermore, a block
joint 426 is integrally connected to the manifold pipe 423 by soldering. The block
joint 426 is provided with a tubular projected portion 428 for a flow of the coolant
from the manifold pipe 423 to the modulator 100, and a screw thread hole 427. As shown
in Fig. 22, the modulator 100 is provided, at the bottom end thereof, with a block
joint 429 integrally connected thereto by soldering. As shown in Fig. 24, the block
joint 429 forms an opening 429a to which the tubular projection 428 of the first block
428 of the manifold pipe 423 is inserted via an O-ring 431, so that the latter, at
the upper surface 432 thereof, is in contact with the bottom surface 430 of the block
joint 429 of the modulator 100. Furthermore, the block joint 429 is formed with a
hole 429b (Fig. 22) to which a bolt 429c is freely introduced, so that the bolt 429c
engages with the screw thread hole 427 of the block joint 426, whereby the block joints
426 and 429 are connected to each other. The O-ring 421 between the block joints 426
and 429 maintains a fluid tight connection therebetween.
[0050] The arrangement of the modulator 100 branched from the heat exchanger 400 at a location
along the coolant passageway therein permits the portion downstream of the branched
portion to be used as the sub-cooling portion 405, which can increase a difference
in an enthalpy for increasing the cooling ability. Nevertheless, the arrangement of
the modulator 100 branched from the heat exchanger at a location along the coolant
passageway of the heat exchanger inevitably reduces an effective area of the condenser
portion 402, which increases the output pressure from the compressor 200. Figure 25
shows a result of experiments by the inventors, for illustrating an increase in the
pressure of the output of the compressor 200 as a result of the provision of the modulator
100 in the heat exchanger 400 as shown in Fig. 10. In Fig. 25, the abscissa is the
total amount of coolant filled in the system, and the ordinate is an output pressure.
A line W shows a result obtained when the modulator 100 is used as arranged in Fig.
10, and a line Z shows a result obtained when a prior art device provided with the
receiver 401 is used. As will be seen from the curve W according to the present invention,
a desired amount of coolant is in a range of between about 600 grams to about 1200
grams. When the amount of the coolant is short by about 600 grams, there is a sharp
drop in the output pressure due to the shortage in the amount of coolant. When the
amount of coolant is larger than about 1200 grams, there is a sharp increase in the
output pressure, which means that an excess amount of the coolant is filled in the
system. As will be seen from the comparison of the result (curve W) of the present
invention, the construction of the present invention including the modulator 100 can
increase the output pressure of the compressor 200, compared with the result (curve
Z) of the prior art, but the increase in the output pressure as obtained in the present
invention is not large.
[0051] In the embodiment as described above (Fig. 10), the heat exchanger 400 is constructed
by a condenser portion 402 and sub-cooling portion 405, which are constructed by serpentine
tubes, but the heat exchanger 400 can be constructed from a plurality of parallel
tubes 482 having a flattened cross sectional shape, as shown in Fig. 26. This type
of the heat exchanger 400 includes, on both sides thereof, horizontally spaced tank
portions 480 and 481 between which a plurality of horizontal parallel pipes 482 having
a flattened shape are arranged to be vertically spaced therein. Corrugated fins 483
are arranged between the adjacent flattened pipes 482 such that the fins are connected
to the surfaces of the pipes 482 by soldering, and partition plates 484 and 485 are
arranged in the side tanks 480 and 481, respectively. The partition plate 484 in the
side tank 480 is located at a higher position than the partition plate 485 in the
side tank 481. An coolant inlet 480-1 is opened to the space inside the tank 480 above
the partition 484, and the coolant outlet 481-1 is opened to the space inside the
tank 481 below the partition 485. As a result, an "S" shaped flow of the coolant is
obtained, from the inlet 480-1 to the outlet 481-1, as shown by arrows f1, f2, f3,
f4, f5 and f6.
[0052] According to this embodiment of the present invention, the modulator 100 is branched
from the side tank 480-1 at a position below the partition 484. Figure 27 shows details
of the means for connecting the modulator 100 to the heat exchanger 400. The modulator
100 is supported by the side tank 480 at the bottom end thereof by a joint 150. The
joint 150 is also used for obtaining a fluid communication between the modulator 100
and the tank 480, and the construction of this joint is similar to that shown in Figs.
23 and 24. The modulator 100 is supported, at the top end thereof, by a supporting
plate 152. As shown in Fig. 28, when viewed from the side of the heat exchanger 400,
the modulator 100 is slightly inclined in the forward direction when arranged in an
engine room 800 of a vehicle as shown in Fig. 29, which makes it easy for an operator
to visually check the level of the coolant in the modulator 100, via the sight glass
190 arranged at the top end of the modulator 100 as shown in Fig. 6. As shown in Fig.
28, a bolt 151 is provided for connecting a pair of joints in the same manner as explained
with reference to Figs. 23 and 24. Furthermore, an inner induction pipe 120, as explained
with reference to Fig. 18, is provided in the modulator 100, and is connected to an
opening 153 in a partition, which opening corresponds to the opening 423-1 in Fig.
18. The partition is further provided with an opening 153 for a direct connection
of the bottom portion of the modulator 100 with the tank 480, which opening 153 corresponds
to the opening 424 in Fig. 18. According to the embodiment as shown, the inner diameter
of the opening 153 to the induction pipe 120 is 3.5 mm, and the inner diameter of
the induction pipe 120 is 5 mm. Furthermore, as will be easily seen from Fig. 28,
the induction pipe 120 is connected to the modulator 100 at the inner wall thereof
by stay members 490, to prevent a movement of the induction pipe 120.
[0053] Figure 29 shows an arrangement of the modulator in the engine room 800 of a vehicle,
with regard to the other components of the engine. In Fig. 29, reference numeral 230
denotes a radiator for cooling a coolant for an internal combustion engine 201. The
radiator 230 is arranged so as to face a fan 231 driven by a crankshaft (not shown)
of the engine body 201. The heat exchanger 400 for the refrigerating system according
to the present invention is arranged in front of the radiator 230. As already explained,
the modulator 100 on one side of the heat exchanger 400 is inclined with respect to
the heat exchanger 400 in the forward direction of the engine chamber of the vehicle,
to allow the operator to check the level of the coolant in the modulator 100 by using
the sight glass 190 at the top end thereof when an engine hood 800' is open.
[0054] Figure 30 shows a difference in the refrigerating ability of the refrigerating system
for a vehicle as shown in Fig. 29, having the modulator 100, and a prior art refrigerating
system as shown in Fig. 7 having the receiver 401. In Fig. 30, the abscissa shows
the time lapsed, and the ordinate shows, at the upper part thereof, the temperature
of the air blown into a passenger room of the vehicle, and at the lower part thereof,
the temperature of the passenger room. Lines designated by K are results obtained
by the prior art system having the receiver 401 in Fig. 7, and lines designated by
J are results obtained by the system according to the present invention provided with
the modulator 100 as shown in Fig. 29. Along the abscissa, a portion L corresponds
to a running condition of the vehicle at a speed of 40 km/h, wherein air from the
passenger room is recirculated into the evaporator 310 and a large amount of air is
introduced into the evaporator 310; a portion M corresponds to a running condition
of the vehicle at a speed of 60 km/h, wherein an outside air having a temperature
of 35 degrees centigrade and a humidity of 60% is introduced into the evaporator 310,
and a medium amount of air is introduced into the evaporator 310; and a portion N
corresponds to a running condition such that the vehicle is stopped by heavy traffic
but the engine is running, wherein air from the passenger room is recirculated into
the evaporator 310, and a large amount of the air is introduced into the evaporator
310. As will be easily seen from Fig. 30, at the area N where the vehicle is stopped,
the engine idling speed was 740 r.p.m. on the line K for the prior art refrigerating
system provided with the receiver 401, but the engine idling speed was 660 r.p.m.
on the line J for the refrigerating system according to the present invention provided
with the modulator 100.
[0055] As explained above, in the refrigerating system provided with a modulator according
to the present invention, an increase in the cooling ability can be obtained over
the entire range of operation of the vehicle. In particular, as will be seen from
Fig. 30, the system according to the present invention provided with the modulator
can reduce the engine idling speed while obtaining an increased cooling ability, resulting
in an increase in the fuel consumption efficiency for the internal combustion engine
201.
[0056] Figure 31 shows another embodiment of the modulator 100 when connected to the side
tank 481, to which a plurality of vertically spaced parallel horizontal pipes 482
are connected and a fluid communication therebetween occurs as shown in Fig. 27. A
connection pipe 126 is provided for the connection to the tank 481, and the pipe 126
is provided, along the entire length thereof, with a partition 160 whereby an induction
passageway portion 120 above the partition 160 and a flow out passageway portion 125
below the partition 160 are created, as shown in Fig. 31'. A sight glass 190 is connected
to the upper end of the modulator 100, and a float member 180 is arranged in the variation
margin portion 130 inside the modulator 100. The function of the variation margin
portion 130 has been described with reference to Fig. 20. An annular projection 100-8
is formed on the inner wall of the modulator 100, to engage the float 180 and prevent
it from moving downward when the level of the liquid coolant in the modulator 100
is lower than a predetermined limit. The sight glass 190 allows the level of the liquid
coolant in the modulator to be visually monitored. A block 191 having a tubular shape
drying agent is arranged around the upper end of the pipe 126 projected into the space
inside the modulator 100, and absorbs moisture in the coolant.
[0057] As shown in Fig. 33, the top wall of the pipe 126 is provided with an opening 128
open to the induction passageway portion 120. The opening 128 is used for a communication
of the space inside the tank 181 above the pipe 126 with the induction passageway
portion 120, as will be seen from Fig. 31, so that an amount of the coolant in the
tank 481 from the condenser portion 402 is introduced into the modulator 100 via the
induction passageway portion 120. The location of the opening 128 is determined such
that a gaseous coolant in the tank 481 is easily introduced into the induction passageway
portion 120 due to the dynamic pressure of the flow of the coolant in the tank 481.
As shown in Fig. 33, the bottom wall of the pipe 126, opposite to the opening 128,
is provided with an opening 129 open to the flow out passageway portion 125. The opening
129 is used for a communication of the space inside tank 181 below the pipe 126 with
the flow-out passageway portion 125, as will be seen from Fig. 31, so that an amount
of the coolant in the modulator 100 flows from the modulator 100 into the tank 481
via the return passageway portion 125, and then into the sub-cooling portion 405.
The pipe 126 passes through the joint 150, which is fitted and fixed to the side wall
of the tank 481, and through a supporting member 150' resting on the joint 150 and
fixed thereto by a bolt 150.
[0058] The pipe 126 as shown in Fig. 31 and 32 is made of an aluminum alloy drawn to obtain
a desired cross-sectional shape. The pipe 126 is connected to the modulator 100 and
the joint 150 by soldering. In Figs. 32 and 33, the partition wall 160 between the
passageway portions 120 and 125 is corrugated, but this wall 160 can have other shapes,
such as a plane shape. As already explained, the partition wall 160 can be formed
integrally by a drawing process, but instead of employing the drawing process, the
partition wall 160 can be formed as a separate member and fixedly arranged inside
the pipe 126.
[0059] Figure 34 shows, another embodiment of the present invention in a construction of
a parallel pipe type heat exchanger, which is provided with a joint 150 in which an
induction passageway 153 and a flow-out passageway 152 are formed. The joint 150 is
connected by a bolt 151 to a base plate 156 fixedly connected to the side tank 481,
and a partition 900 is arranged in the side tank 481, to divide the space inside the
tank 481 into upper and lower portions. The base plate (first joint) 156 forms, in
cooperation with the second joint 150, a coolant passageway 158 therein which is bent
in a substantially V shape, and is connected at one end to the upper portion of the
tank 481 and at the other end to the lower portion of the tank 481. The passageway
158 is connected to the passageway 153 in the joint 150, which is connected to the
induction pipe 120 in the modulator 100, and as a result, a positive introduction
of the gaseous coolant from the upper tank portion can be positively introduced into
the upper portion of the space inside the modulator 100. In this embodiment, the joint
156, to which the second joint 150 is connected by the bolt 151, is connected to the
tank 481 by soldering. Also, an O-ring 157 is arranged between the facing surfaces
of the joints 156 and 150, to obtain an air tight connection therebetween.
[0060] Note, in the construction of Fig. 34, the induction passageway 153 in the joint portion
150 is arranged so that it extends into the coolant passageway 158 in such a manner
that the passageway 153 is substantially opposite to the direction of the flow of
the coolant in the passageway 156. As a result, an effective introduction to the induction
passageway 153 of a gaseous coolant in the passageway 158 is obtained.
[0061] Figure 35 to 40 show various conditions of the coolant as filled in the modulator,
when visually observed. Figure 35 and 36 show a state where there is a shortage in
the amount of coolant filled in the modulator 100, and there is substantially no liquid
coolant therein, so that there are many gas bubbles included in the liquid coolant
introduced into the modulator 100 via the induction pipe 120. This situation can be
determined by observing, via the sight glass 190, white bubbles that appear inside
the modulator.
[0062] Figure 37 and 38 show a situation wherein a suitable amount of the coolant is filled
in the modulator. In this situation, the coolant introduced into the modulator 100
via the induction pipe 120 includes a small amount of gas, and thus the gas-coolant
boundary in the induction pipe 120 is at substantially the same level as that in the
modulator 100, which allows the level of the liquid at the induction pipe 120 to be
observed from outside of the modulator via the sight glass 190.
[0063] Figure 39 and 40 show a situation wherein an excess of coolant is charged within
the modulator. In this case, the liquid state coolant occupies not only the charging
margin portion 131 but also the variation margin portion 130, which makes it impossible
to observe from the outside the level of the liquid in the modulator 100. This shows
the user that an excess charging of the coolant has occurred.
[0064] In place of the previous embodiments, wherein the sight glass 190 is arranged at
the top of the modulator, the embodiment shown in Fig. 41 includes a sight glass 190
arranged at the side wall 100-5 at a position which allows the user to make a direct
observation through the upper end of the induction pipe 120.
[0065] In an arrangement whereby the sight glass 190 is located at the top of the modulator,
the induction pipe 120 is provided with upper end 120 which is bent so as to extend
horizontally for a short length thereof. This construction also allows the user to
observe the condition of coolant at the outlet end of the induction pipe 120.
[0066] Figure 43 show a modification of the condenser 400 provided with a plurality of parallel
pipes connected to side tanks; the modulator 100 being connected to one of the side
tanks. In this embodiment, the modulator 100 is integral with the side tank 481, and
the side tank 900 has an inner vertically extending partition 470 which forms, on
the inner side thereof, a side tank 481 to which a plurality of vertically spaced
heat exchange pipes 482 are opened, and forms on the outer side thereof a modulator
100. The tank 900 also has an upper cap 901 and lower cap 902. A partition 484 is
arranged in the side tank 480, to obtain a flow of coolant introduced into the condenser
portion 402 and to the side tank 481, and then flowing from the modulator 100 to the
sub-cooling portion 405, whereby a U-shaped flow of the coolant is obtained between
the inlet and outlet of the heat exchanger 400, as shown by the arrows h1, h2, h3
and h4. The bottom cap 902 is provided with an outwardly projecting portion 902a which
allows the bottom end of the partition 470 to be spaced from the lower cap 902 so
that a communication passageway 472 is formed therebetween to thereby allow a communication
of the coolant between the side tank 481 and the modulator 100.
[0067] Figure 45 shows a modification wherein, instead of the shaped portion 902a shown
in Fig. 43, the partition 470 is formed by an upper portion without perforations and
a bottom portion 473 which is perforated. Note, the upper end of the perforated portion
473 is located at the position which is substantially the same as the position at
which a boundary between the condenser portion 402 and sub-cooling portion 405 is
situated. In this embodiment, part of the coolant directed from the condenser portion
402 toward the sub-cooling portion 405 is introduced into the modulator 100 via the
perforated part 473 of the partition 470.
[0068] Also note, in the embodiment shown in Fig. 43 or 45, another partition is arranged
not only in the tank 480 but also in the tank 481, in the same way as shown in Fig.
26, to provide an "S" shape flow of the coolant in the heat exchanger 400.
[0069] Although embodiments of the present invention are described with reference to the
attached drawings, many modifications and changes can be made by those skilled in
this art without departing from the scope and spirit of the present invention.
1. A refrigerating apparatus, comprising:
a coolant recirculation line;
a compressor in the recirculation line for compressing the coolant;
a condenser in the recirculation line for condensing the compressed coolant;
means in the recirculation line for expanding the condensed coolant by reducing
the pressure thereof;
an evaporator in the recirculation line for evaporating the reduced pressure coolant,
the coolant passed through the evaporator being introduced into the compressor, so
that a flow of the coolant for recirculation in the recirculation line is created,
to thereby obtain a refrigerating cycle, and;
a modulator defining therein a chamber for receiving from the condenser only a
part of the total amount of the coolant subjected to the refrigerating cycle, the
modulator being capable of defining in said space a boundary between liquid and gas
states, for containing the liquid phase coolant.
2. An apparatus according to claim 1, wherein said space in the modulator has top and
bottom ends which are vertically spaced, the bottom end being open to the recirculation
line.
3. An apparatus according the claim 1, wherein said modulator is connected to said the
recirculation line at a position downstream of the condenser and upstream of the pressure
reducing means.
4. An apparatus according to claim 1, wherein said condenser is provided with an inlet
for a flow of coolant from the compressor, an outlet for a discharge of gas to the
pressure reducing means, at least one pipe arranged in a serpentine form, to provide
spaced portions connected with each other in series, and fins mounted on the pipe
and arranged between adjacent pipe portions.
5. An apparatus according to claim 4, wherein two serpentine passageways are arranged
in parallel between the inlet and the outlet.
6. A refrigerating apparatus, comprising:
a coolant recirculation line;
a compressor in the recirculation line for compressing the coolant;
a condenser in the recirculation line for condensing the compressed coolant;
a super cooler in the recirculation line for receiving the condensed coolant from
the condenser;
means on the recirculation line for expanding the coolant from the super cooler
by reducing the pressure thereof;
an evaporator in the recirculation line for evaporating the reduced pressure coolant
from the expending means, the coolant pass through the evaporator being introduced
into the compressor, so that a flow of the coolant in the recirculation line is created
to thereby obtain a refrigerating cycle, and;
a modulator arranged in the recirculation line between the condenser and the super
cooler, said modulator defining therein with a chamber for receiving from the condenser
only a part of the total amount of the coolant subjected to the refrigerating cycle,
the modulator being capable of defining in said space a boundary between the liquid
and gas states for separating the gas from the coolant and feeding the liquid phase
coolant to the super cooler.
7. A refrigerating apparatus according to claim 6, wherein said condenser and the super
cooler are combined to provide a single heat exchanger unit, and further comprises
connecting means for connecting the heat exchanger unit with the modulator so that
only a part of the flow from the condenser to the super cooler is introduced into
the modulator.
8. A refrigerating apparatus according to claim 6, wherein the super cooler has a heat
emission area having a ratio based on the sum of the heat emission area of the condenser
and the heat emission area of the super cooler, the value of the ratio being in a
range of between 0.1 and 0.3.
9. A refrigerating apparatus according to claim 7, wherein said condenser and the super
cooler are constructed by at least one serpentine pipe located at the coolant recirculation
line, wherein said communication means comprises a manifold pipe having portions for
connection to the condenser, super cooler and modulator, respectively, and a joint
means for connecting said portions to the modulator.
10. An apparatus according to claim 9, wherein said joint means comprises a first joint
member connected to the manifold pipe, a second joint member connected to the modulator,
and a means for obtaining a fluid tight connection between the first and second joint
members.
11. A refrigerating apparatus according to claim 7, wherein said condenser and super cooler
of the heat exchanger unit each comprise a plurality of spaced parallel pipes, and
wherein the heat exchanger unit further comprises a pair of spaced tanks between which
the pipes of the condenser and the super cooler are arranged so that the tanks communicate
with the pipes, at least one of the tanks having a partition for dividing the space
inside thereof into first and second portions, the first portion of the first tank
being connected to the compressor for an introduction of the coolant to be condensed
into the pipes constructing the condenser, so that a flow of the coolant from the
compressor to the super cooler is obtained via the first and second tank, said modulator
being connected to the tank at a position for an introduction of the coolant from
the compressor into the super cooler.
12. A refrigerating apparatus according to claim 11, wherein said second tank is also
provided with a partition located at the level below the partition in the first tank,
for dividing the space therein into upper and lower portions so that the coolant introduced
into the upper portion of the first tank is introduced into the condenser and to the
upper portion of the second tank, and then returned to the pipes of the condenser
and into the lower portion of the first tank, and finally, flows into the pipes of
the super cooler and to the lower portion of the second tank and into the pressure
reducing means, wherein the modulator is connected to the lower portion of the first
tank for an introduction of only a part of the entire coolant used for the recirculation
cycle.
13. An apparatus according to claim 11, wherein said tank and the modulator have an integral
construction composed of a tubular member having vertically spaced open ends, upper
and lower caps connected to those upper and lower ends, and a vertically extending
partition for dividing a space in the tube into the second tank and the modulator,
the partition defining a passageway means for a communication of the second tank with
the modulator.
14. An apparatus according to claim 13, wherein said passageway means comprises a portion
of the bottom cap spaced from the bottom end of the partition, for forming a passageway
for a connection of the second tank with the modulator.
15. An apparatus according to claim 13, wherein said passageway means comprises a perforated
bottom portion of said partition for a communication of the second tank with the modulator.
16. An apparatus according to claim 11, wherein said connecting means comprises passageway
means for diverting a portion of the flow of the coolant in the tank and for re-introducing
the liquid from the modulator to the tank toward the super cooler, and means for a
connection of the passageway means with the tank.
17. An apparatus according to claim 16, wherein said passageway means comprise a partition
having a first opening, and a pipe having one end connected to the first opening and
a second end opened to the inside of the modulator, said partition having a second
opening for an introduction of the liquid in the modulator into the tank toward the
super cooler.
18. An apparatus according to claim 16, wherein said passageway means comprises a pipe
having one end opened to the tank and a second end opened to the inside of the modulator,
the pipe having therein a partition along the length thereof providing a pair of passageways
connected to the condenser and the super cooler, respectively, and means for fixing
the pipe to the tank.
19. An apparatus according to claim 11, wherein said tank is provided with a partition
in the tank across the space therein, and said connection means comprises a first
joint means connected to the tank and cooperating with the partition for generating
a bent flow of the coolant in the tank, a second joint for a connection of the joint
with the modulator, said second joint being provided with a passageway for taking
out a flow of coolant from the passageway into the modulator, and a second passageway
for returning the coolant from the modulator to the first passageway.
20. An apparatus according to claim 19, further comprising a pipe arranged in the modulator
for a connection of the passageway with the space inside the modulator.
21. A modulator for a refrigerating system having a recirculation passageway in which
a compressor, a condenser and a pressure-reducing means are arranged in series to
thereby obtain a refrigerating cycle, said modulator comprising a closed chamber therein
for storing the coolant, said chamber having a bottom end opened to said coolant recirculating
passageway at a position within the condenser or downstream of the condenser and upstream
of the pressure reducing means.
22. A modulator according to claim 21, further comprising a sight glass for observing
the level of the coolant therein.
23. A modulator for a refrigerating system having a recirculation passageway in which
a compressor, a condenser, super cooler and a pressure reducing means are arranged
in series to thereby obtain a refrigerating cycle, said modulator comprising a closed
chamber therein for storing the coolant, said chamber having a bottom end opened to
said coolant recirculating passageway at a position between the condenser and the
super cooler.
24. A modulator according to claim 23, further comprising a sight glass for observing
the level of the coolant therein.
25. An air conditioning system for a vehicle having a engine room in which an internal
combustion engine and a radiator are arranged, said system comprising:
a coolant recirculation line;
a compressor in the recirculation line for compressing the coolant, the compressor
being connected to the engine rotating shaft and being driven thereby;
a heat exchanger having a condenser portion in the recirculation line for condensing
the compressed coolant and a super cooler portion in the recirculation line for receiving
the condensed coolant from the condenser;
said heat exchanger being arranged in the engine room and adjacent to the radiator;
means in the recirculation line for expanding the coolant from the super cooler
by reducing the pressure thereof;
an evaporator in the recirculation line for evaporating the coolant the evaporated
coolant being introduced into the compressor, so that a flow of the coolant in the
recirculation line is created for obtaining a refrigerating cycle, and;
a modulator arranged in the recirculation line between the condenser portion and
the super cooler portion, said modulator defining therein with a chamber for receiving,
from the condenser, only a part of the total amount of the coolant subjected to the
refrigerating cycle, the modulator being capable of defining in said space a boundary
between the liquid and gas states for separating the gas from the coolant so that
liquid phase coolant is introduced to the super cooler.
26. A system according to claim 25, wherein said modulator is arranged inclined, with
respect to the heat exchanger unit, in the forward direction of the vehicle.
27. A system according to claim 26, wherein said modulator has a sight glass at a top
portion of the engine room, to thereby allow the coolant level therein to be observed.