Information
-
Patent Grant
-
6311506
-
Patent Number
6,311,506
-
Date Filed
Wednesday, July 7, 199927 years ago
-
Date Issued
Tuesday, November 6, 200124 years ago
-
Inventors
-
Original Assignees
-
Examiners
Agents
- Vardnell & Vardnell, PLLC
-
CPC
-
US Classifications
Field of Search
US
- 062 1964
- 062 1961
- 062 201
- 062 197
- 062 203
- 062 204
- 062 205
- 062 208
-
International Classifications
-
Abstract
A control unit is disclosed for controlling a refrigerating machine in such a way that a refrigerating power exceeding the required performance is secured while the control unit has a function of bypassing hot gas by means of a hot gas bypass line. A temperature-responsive valve is mounted in the hot gas bypass line in addition to a pressure regulating valve. If a preset temperature Tr of a brine becomes equal to or higher than a given temperature (0° C.), the temperature-responsive valve opens the bypass line. If the preset temperature Tr becomes lower than the given temperature, the temperature-responsive valve closes the bypass line.
Description
FIELD OF THE INVENTION
The present invention relates to a control unit for a refrigerating machine and, more particularly, to a control unit capable of securing refrigerating capability more than required.
DESCRIPTION OF THE PRIOR ART
FIG. 8
shows the whole construction of a temperature control system that acts as a refrigerating machine and incorporates a chiller
10
. This temperature control system chiefly consists of the chiller
10
, a controlled object
1
whose temperature is to be controlled, and a circulatory fluid line
3
between the chiller
10
and the controlled object
1
. For example, the controlled object
1
is a vacuum chamber that surface-processes or otherwise processes semiconductor wafers under a desired temperature.
In the chiller
10
described above, a compressor
12
, a condenser
13
, an expansion valve
14
, and an evaporator
11
are connected in series via a conduit
15
. A refrigerant
16
is passed through this conduit
15
to carry out refrigeration cycles. A brine (anti-freezing fluid)
17
circulating through the circulatory fluid line
3
exchanges heat with the refrigerant
16
, thus cooling the brine
17
. Thus, it is maintained at a preset temperature. As a result, the controlled object
1
is controlled to a target temperature.
FIG. 11
particularly shows the line arrangement in the chiller
10
.
This chiller
10
has a hot gas bypass line
18
that provides a bypass line for gas delivered from the compressor
12
and sends it to the evaporator
11
.
A pressure regulating valve
19
is mounted in the hot gas bypass line
18
to open this line
18
when the vapor pressure of the refrigerant
16
in the evaporator
11
becomes equal to or less than a given pressure, thus permitting passage of the hot gas. When the vapor pressure of the refrigerant
16
in the evaporator
11
becomes higher than the given pressure, the regulating valve
19
closes the hot gas bypass line
18
, thus cutting off the hot gas.
The pressure regulating valve
19
is installed to maintain the vapor pressure higher than the preset pressure, for the following reason. If the vapor pressure becomes equal to or lower than the preset pressure (atmospheric pressure), the refrigerant
16
does not sufficiently vaporize within the evaporator
11
and returns to the compressor
12
while maintained in a liquid state. This is so-called the phenomenon of the fluid back and may damage the compressor
12
.
The pressure regulating valve
19
operates according to the difference between the vapor pressure of the entering refrigerant
16
and the force of a spring.
Because of the mechanical structure of the prior art pressure regulating valve
19
, the valve operates according to the difference between the vapor pressure of the entering refrigerant
16
and a spring force, even if the vapor pressure becomes higher than the given pressure, the valve
19
is slightly open, and the hot gas is bypassed to the evaporator
11
via the hot gas bypass line
18
.
If the hot gas is unnecessarily bypassed to the evaporator
11
, the refrigerating capability becomes deteriorated. As the preset temperature of the brine
17
(i.e., the target temperature of the controlled object
1
) becomes lower, the refrigerating capability becomes lower. Therefore, if the hot gas is undesirably bypassed where the preset temperature of the brine
17
is low, the refrigerating capability drops conspicuously.
The chiller
10
according to the present invention is required to exhibit a refrigerating power of more than 1 kW when the temperature of the brine
17
is −20° C., and to exhibit a refrigerating power of 2 kW or more where the temperature of the brine
17
is 0° C.
FIG. 10
shows the relation between the brine temperature and the cooling power where the hot gas is not bypassed (indicated by the broken line) and bypassed (indicated by the solid line). As can be seen from the graph of
FIG. 10
, where the brine
17
has a high temperature of 0° C., a refrigerating power of 2 kW or more is secured, whether the hot gas is bypassed or not. Thus, the required performance is satisfied.
However, as the temperature of the brine
17
becomes lower, the refrigerating power drops conspicuously where the hot gas is bypassed. Where the temperature of the brine
17
is −20° C., the power is much lower than the required power of 1 kW. Consequently, it is impossible to meet the required performance.
If the compressor
10
is replaced by one having a sufficiently large capacity, the refrigerating performance may be enhanced, and the required refrigerating power may be secured even if the hot gas is bypassed.
However, increasing the capacity of the compressor
10
to a sufficiently large value will incur an increase in cost. Furthermore, the equipment will become bulky, which in turn will occupy more space. Moreover, the electric power consumption will increase. Accordingly, increasing the capacity of the compressor
10
is not acceptable.
SUMMARY OF THE INVENTION
In view of the foregoing circumstances, the present invention has been made. It is a first object of the present invention to provide a control unit capable of imparting required refrigerating capability to a refrigerating machine without incurring an increase in cost, size, or electric power consumption.
The prior art pressure regulating valve
19
has intrinsic problems. That is, if the vapor pressure is higher than a given pressure, the valve
19
is slightly open, because the valve mechanically operates in response to the vapor pressure as mentioned above. If the hot gas is undesirably bypassed by the opening of the valve
19
, the refrigerating capability will be deteriorated. Especially, if the vapor pressure is low, the amount of refrigerant circulated becomes small and so the refrigerating power decreases conspicuously.
It is a second object of the invention to provide a control unit that causes pressure regulating valve
19
of a refrigerating machine to operate more precisely in response to vapor pressure than that of the prior art, thus preventing the refrigerating capability from deteriorating.
A first embodiment of the present invention achieves the first object described above and provides a control unit for use with a refrigerating machine in which a compressor, a condenser, and an evaporator are connected in series via a conduit. The refrigerating machine further includes a hot gas bypass line for bypassing hot gas discharged from the compressor. A pressure regulating valve is installed in the hot gas bypass line to open the hot gas bypass line, if the vapor pressure of a refrigerant inside the evaporator becomes equal to or lower than a given pressure, thus passing the hot gas. If the vapor pressure of the refrigerant in the evaporator becomes higher than the given pressure, the pressure regulating valve closes the hot gas bypass line to cut off the hot gas. The refrigerant exchanges heat with a brine passing through the evaporator to maintain the brine at a preset temperature.
A temperature-responsive valve is mounted in the hot gas bypass line. If the temperature of the brine is equal to or higher than the given temperature, the temperature-responsive valve opens the hot gas bypass line. If the temperature of the brine is lower than the given temperature, the temperature-responsive valve closes the hot gas bypass line.
In the first embodiment of the invention described above, as shown in
FIG. 1
, a temperature-responsive valve
20
is mounted in a hot gas bypass line
18
. If the preset temperature Tr of the brine
17
rises equal to or higher than a given temperature (0° C.), the valve
20
opens the hot gas bypass line
18
. If the preset temperature Tr of the brine
17
is lower than the given temperature (0° C.), the valve
20
closes the hot gas bypass line
18
.
Therefore, when the preset temperature of the brine is equal to or higher than the given temperature of 0° C., the hot gas bypass line
18
is opened. The pressure regulating valve
19
operates and bypasses the hot gas. At this time the temperature of the brine and the refrigerating power have a relation as indicated by the solid line in FIG.
10
. Accordingly, when the preset temperature Tr of the brine
17
is 0° C. or more, the refrigerating power exceeds the required refrigerating power of 2 kW. Where the preset temperature Tr of the brine
17
is lower than the given temperature 0° C., the hot gas bypass line
18
is closed. The pressure regulating valve
19
does not function and thus does not bypass the hot gas. At this time, the brine temperature and the refrigerating power have a relation indicated by the broken line in FIG.
10
. Therefore, even if the preset temperature Tr of the brine
17
is −20° C., the refrigerating power is in excess of the required refrigerating power of 1 kW.
As described thus far, in the first embodiment of the present invention, a refrigerating power exceeding the required performance can be secured while maintaining the function of bypassing the hot gas.
A second embodiment of the present invention is based on the first embodiment described above and characterized in that the aforementioned temperature-responsive valve is a control valve that is opened and closed in response to an ON/OFF input command signal.
A third embodiment of the present invention is intended to achieve the aforementioned first object of the present invention and provides a refrigerating machine in which a compressor, a condenser, and an evaporator are connected in series via a conduit. The refrigerating machine has a hot gas bypass line for bypassing hot gas discharged from the compressor. A pressure regulating valve is mounted in the hot gas bypass line to open the hot gas bypass line, if the vapor pressure of the refrigerant inside the evaporator becomes equal to or lower than a given pressure, thus passing the hot gas. If the vapor pressure of the refrigerant inside the evaporator becomes higher than the given pressure, the pressure regulating valve closes the hot gas bypass line, cutting off the hot gas. The refrigerant exchanges heat with the brine passing through the evaporator to maintain the brine at a preset temperature.
A temperature-responsive valve is mounted in the hot gas bypass line. If the actual temperature of the brine is equal to or higher than the given temperature, the temperature-responsive valve opens the hot gas bypass line. If the actual temperature of the brine is lower than the given temperature, the temperature-responsive valve closes the hot gas bypass line.
A fourth embodiment of the invention is based on the third embodiment described above and characterized in that the aforementioned temperature-responsive valve is a control valve which is opened and closed in response to an ON/OFF input command signal.
A fifth embodiment of the invention achieves the second object of the invention described above and provides a refrigerating machine in which a compressor, a condenser, and an evaporator are connected in series via a conduit. The refrigerating machine has a hot gas bypass line for bypassing hot gas discharged from the compressor. A pressure regulating valve is mounted in the hot gas bypass line to open the hot gas bypass line, if the vapor pressure of the refrigerant inside the evaporator becomes equal to or lower than a given pressure, thus passing the hot gas. If the vapor pressure of the refrigerant inside the evaporator becomes higher than the given pressure, the regulating valve closes the hot gas bypass line, cutting off the hot gas.
A pressure detection means is mounted to detect the vapor pressure of the refrigerant inside the evaporator. Instead of the pressure regulating valve, a pressure-responsive valve is mounted in the hot gas bypass line. If the vapor pressure detected by the pressure detection means becomes equal to or lower than the given pressure, the temperature-responsive valve opens the hot gas bypass line. If the vapor pressure detected by the pressure-responding means becomes higher than the given pressure, the temperature-responsive valve closes the hot gas bypass line.
In accordance with the fifth embodiment described above, as shown in
FIG. 5
, a pressure detection means
25
is mounted to detect vapor pressure P of a refrigerant
16
inside an evaporator
11
. A pressure-responsive valve
23
is mounted in a hot gas bypass line
18
instead of the pressure regulating valve
19
. When the vapor pressure P detected by the pressure detection means
25
becomes equal to or lower than a given pressure (e.g., atmospheric pressure), the valve
23
opens the hot gas bypass line
18
. When the vapor pressure P detected by the pressure detection means
25
becomes higher than the given pressure (e.g., atmospheric pressure), the valve
23
closes the hot gas bypass line
18
.
In accordance with the fifth embodiment described above, when the vapor pressure P detected by the pressure detection means
25
becomes equal to or lower than the given pressure (e.g., atmospheric pressure), the pressure-responsive valve
23
is opened. Thus, the vapor pressure P is kept higher than the given pressure (e.g., atmospheric pressure). Therefore, it can prevent the phenomenon of the fluid back (i.e., the vapor pressure becomes equal to or lower than the atmospheric pressure, and the refrigerant
16
does not sufficiently vaporize inside the evaporator
11
and returns to the compressor
12
while kept in a liquid state) of the liquid in the same way as the prior art pressure regulating valve
19
. Hence, damage to the compressor
12
and other dangers can be prevented.
In accordance with the fifth embodiment of the invention, the pressure-responsive valve
23
is precisely opened and closed in response to the vapor pressure P detected by the pressure detection means
25
. Therefore, if the vapor pressure P becomes higher than the given pressure (e.g., atmospheric pressure), the valve
23
is prevented from being opened. Consequently, unwanted bypassing of the hot gas is circumvented. Hence, the refrigerating power can be prevented from deteriorating.
A sixth embodiment of the present invention is based on the fifth embodiment described above and characterized in that the aforementioned pressure-responsive valve is a control valve that is opened and closed in response to an ON/OFF input command signal.
A seventh embodiment of the invention is based on the fifth embodiment described above and characterized in that the aforementioned pressure-responsive valve is a control valve that is opened and closed by an amount corresponding to the contents of a command.
An eighth embodiment of the present invention achieves the second object described above and provides a refrigerating machine in which a compressor, a condenser, and an evaporator are connected in series via a conduit. The refrigerating machine has a hot gas bypass line for bypassing hot gas discharged from the compressor. A pressure regulating valve is mounted in the hot gas bypass line to open the hot gas bypass line, if the vapor pressure of the refrigerant inside the evaporator becomes equal to or lower than a given pressure, thus passing the hot gas. If the vapor pressure of the refrigerant inside the evaporator becomes higher than the given pressure, the regulating valve closes the hot gas bypass line, cutting off the hot gas.
A temperature detection means is mounted to detect the temperature of the refrigerant inside the evaporator. Instead of the pressure regulating valve, a temperature-responsive valve is mounted in the hot gas bypass line. If the temperature of the refrigerant detected by the temperature detection means becomes equal to or lower than a given temperature, the temperature-responsive valve opens the hot gas bypass line. If the temperature of the refrigerant detected by the temperature detection means becomes higher than the given temperature, the temperature-responsive valve closes the hot gas bypass line.
A ninth embodiment of the present invention is based on the eighth embodiment of the invention and characterized in that the aforementioned temperature-responsive valve is a control valve that is opened and closed in response to an ON/OFF input command signal.
A tenth embodiment of the invention is based on the eighth embodiment of the invention and characterized in that the temperature-responsive valve is a control valve that is opened and closed by an amount corresponding to contents of a command.
Other objects and features of the invention will appear in the course of the description thereof, which follows.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1
is a line diagram of a control unit and a refrigerating machine for use with the control unit in accordance with the present invention;
FIG. 2
is a line diagram of a modification of the refrigerating machine and control unit shown in
FIG. 1
;
FIG. 3
is a flowchart illustrating a sequence of operations executed by a controller shown in
FIG. 2
;
FIG. 4
is a flowchart illustrating a sequence of operations executed by the controller shown in
FIG. 5
;
FIG. 5
is a line diagram of another control unit and a refrigerating machine for use with the control unit in accordance with the invention;
FIG. 6
is a line diagram of a modification of the refrigerating machine and control unit shown in
FIG. 5
;
FIG. 7
is a flowchart illustrating a sequence of operations executed by a controller shown in
FIG. 6
;
FIG. 8
is a conceptual diagram of a temperature control unit as a whole system according to the preferred embodiments of the invention;
FIGS.
9
(
a
),
9
(
b
), and
9
(
c
) are line diagrams of modifications of the structure of hot gas bypass lines;
FIG. 10
is a graph in which refrigerating power is plotted against the temperature of a brine; and
FIG. 11
is a line diagram of the prior art refrigeration machine.
DETAILED DESCRIPTION OF THE INVENTION
FIG. 8
conceptually illustrates the whole system of a refrigerating machine and a control unit in accordance with the present invention, which is a temperature control machine including a chiller
10
acting as a refrigerating machine.
This temperature control machine consists mainly of the chiller
10
, an object
1
whose temperature is to be controlled, and a circulatory fluid line
3
between the chiller
10
and the controlled object
1
.
For example, the controlled object
1
is a vacuum chamber for surface-processing semiconductor wafers under a desired temperature. A heat storage tank, a halogen lamp, and so on (none of which are shown in
FIG. 8
) needed for the temperature control are mounted in th e circulatory fluid line
3
.
In the chiller
10
described above, a compressor
12
, a condenser
13
, an expansion valve
14
, and an evaporator
11
are connected in series via a conduit or liquid line
15
. A refrigerant
16
is flowed through this conduit
15
to carry out refrigeration cycles.
In particular, the refrigerant
16
is compressed at a high temperature and at a high pressure in the compressor
12
. The vapor of the refrigerant that is made to have high temperature and high pressure by the operation of the compressor
12
is discharged from the discharge port
12
a
of the compressor
12
and sent to the condenser
13
. The vapor of the refrigerant gives heat to the outside air through the condenser
13
. The refrigerant vapor is cooled with cooling water into liquid that is saturated or subcooling. The liquid refrigerant is sent to a thermostatic expansion valve (TEV)
14
, where the liquid refrigerant undergoes throttled expansion and becomes a low-pressure wet vapor, which in turn is sent to the evaporator
11
. In this evaporator
11
, the refrigerant
16
exchanges heat with the brine
17
that is cooled fluid. That is, the refrigerant
16
takes heat from the brine
17
circulated through the circulatory fluid line
3
, evaporates, and becomes dry saturated vapor or superheated vapor. The refrigerant
16
is returned into the suction port
12
b
of the compressor
12
. The refrigerating cycle carried out in the chiller
10
has been described thus far.
The brine
17
is cooled in this way and maintained at a preset temperature. The brine
17
is heated by a halogen lamp (not shown) or the like. In this manner, the controlled object
1
is controlled so as to achieve a target temperature.
In this embodiment, a thermostatic expansion valve is used as the expansion valve
14
. Of course, a hand expansion valve or a constant-pressure expansion valve may be used instead. Furthermore, a capillary tube may be employed instead of the expansion valve
14
.
HCFC-22 is used as the refrigerant
16
. Of course, ammonia, R-12, R-22, R-500, R-404A, R-407C, R-410A, or other refrigerant may also be used.
Liquids used for the brine
17
can include Fluorinert®, which is an electronic liquid used as a heat transfer media that is an excellent dielectric material and is safe for use in a recirculating chiller environment. Of course, ethylene glycol, oil, water, and other liquids can also be used for the brine
17
. Furthermore, nitrogen, air, helium, and other gases may be used. In summary, any brine suitable for the target temperature to be controlled can be appropriately selected. The condenser
13
can be water-cooled with cooling water. Besides, it can be an air-cooled condenser.
FIG. 1
particularly shows the line structure of the chiller
10
in the present embodiment. This chiller
10
has a hot gas bypass line
18
for placing the discharge port
12
a
of the compressor
12
in communication with the line between the thermostatic expansion valve
14
and the evaporator
11
to bypass the hot gas discharged from the compressor
12
into the entrance of the evaporator
11
.
A pressure regulating valve
19
is mounted in the hot gas bypass line
18
to open the bypass line
18
, if the vapor pressure of the refrigerant
16
in the evaporator becomes equal to or lower than a given pressure (e.g., atmospheric pressure), thus permitting passage of the hot gas. If the vapor pressure of the refrigerant
16
inside the evaporator
11
becomes higher than the given pressure (atmospheric pressure), the valve
19
closes the bypass line
18
, thus cutting off the hot gas. The pressure regulating valve
19
is a valve operating according to the difference between the pressure of the entering vapor pressure and the force of a spring. In this embodiment, the given pressure that is a threshold value at which the hot gas bypass line
18
begins to be opened or closed is the atmospheric pressure. However, threshold values other than the atmospheric pressure may also be established.
In the present embodiment, a solenoid valve
20
is mounted in the hot gas bypass line
18
and in the line between the pressure regulating valve
19
and the discharge port
12
a
of the compressor
12
. If the preset temperature Tr of the brine
17
becomes equal to or higher than the given temperature (0° C.), the solenoid valve
20
opens the hot gas bypass line
18
. If the preset temperature Tr becomes lower than the given temperature (0° C.), the solenoid valve
20
closes the hot gas bypass line
18
.
As is well known in the art, the solenoid valve
20
is opened and closed by an electromagnetic force produced when a coil is electrically energized. In the present embodiment, an ON/OFF command current sent from an external controller
21
activates or deactivates the solenoid valve
20
, thus opening or closing the hot gas bypass line
18
.
The controller
21
, which is shown in
FIG. 1
, controls the refrigerating machine as follows.
The preset temperature Tr of the brine
17
is entered into the controller
21
through an entry means such as a keyboard.
The controller
21
makes a decision as to whether the entered preset temperature Tr of the brine
17
is equal to or higher than the given temperature (0° C.).
If the entered preset temperature Tr is equal to or higher than the given temperature (0° C.), an ON command current is supplied to the solenoid valve
20
for activating it. As a result, the solenoid valve
20
is activated, thus opening the hot gas bypass line
18
.
If the preset temperature Tr of the brine
17
entered into the controller
21
is lower than the given temperature (0° C.), an OFF command current is supplied to the solenoid valve
20
for deactivating it. In consequence, the solenoid valve
20
is deactivated, closing the hot gas bypass line
18
.
The advantages of the present invention are next described by referring again to FIG.
10
.
The chiller
10
used in this embodiment is required to show a refrigerating power of 1 kW or more where the temperature of the brine
17
is −20° C. and a refrigerating power of 2 kW or more where the temperature of the brine
17
is 0° C.
In the present embodiment, where the preset temperature Tr of the brine
17
is equal to or higher than 0° C., the hot gas bypass line
18
is opened. Therefore, the pressure regulating valve
19
adjusts the refrigerating power under the presence of the hot gas bypass line.
At this time (in the presence of the hot gas bypass line), the brine temperature and the refrigerating power have a relation as indicated by the solid line in FIG.
10
. Therefore, when the preset temperature Tr of the brine
17
is 0° C., the refrigerating power exceeds the required refrigerating power of 2 kW.
Where the preset temperature Tr of the brine
17
is lower than 0° C., the hot gas bypass line
18
is closed, and the refrigerating power adjusting function of the pressure regulating valve
19
does not function in the absence of the hot gas bypass line. Under this condition, the brine temperature and the refrigerating power have a relation as indicated by the broken line in FIG.
10
. Therefore, where the preset temperature Tr of the brine
17
is −20° C., the refrigerating power is in excess of the required refrigerating power of 1 kW.
As described thus far, in the present embodiment, a refrigerating power exceeding the required performance can be secured while maintaining the function of bypassing the hot gas.
A modification of the machine shown in
FIG. 1
is next described by referring to FIG.
2
.
In the machine shown in
FIG. 2
, the solenoid valve
20
is not controlled according to the preset temperature Tr of the brine
17
. Rather, the solenoid valve
20
is controlled according to the actual temperature T of the brine
17
.
In the present embodiment, a temperature sensor
22
is mounted in the circulatory fluid line
3
through which the brine
17
is circulated, to detect the actual temperature T of the brine
17
.
The actual temperature T of the brine
17
detected by the temperature sensor
22
is input to the controller
21
.
The controller
21
performs processing as illustrated in FIG.
3
.
In particular, a decision is made as to whether the actual temperature T of the brine
17
is equal to or higher than the given temperature (0° C.) (step
101
).
If the result of the decision is YES (i.e., the actual temperature T of the brine
17
is equal to or higher than the given temperature (0° C.)), control goes to step
102
, where an ON command current is produced to the solenoid valve
20
to activate it. As a result, the solenoid valve
20
is activated, and the hot gas bypass line
18
is opened.
On the other hand, if the result of the decision made in step
101
is NO (i.e., the detected temperature T of the brine
17
entered into the controller
21
is lower than the given temperature (0° C.)), an OFF command current is delivered to the solenoid valve
20
to deactivate it. As a result, the solenoid valve
20
is deactivated, and the hot gas bypass line
18
is closed.
Also in this embodiment shown in
FIG. 2
, a refrigerating power exceeding the required performance can be obtained while maintaining the function of bypassing the hot gas, in the same way as in the embodiment shown in FIG.
1
.
In the embodiment shown in
FIGS. 1 and 2
, the solenoid valve
20
is mounted in the hot gas bypass line
18
between the pressure regulating valve
19
and the discharge port
12
a
of the compressor
12
. Of course, the solenoid valve
20
may be installed in the line between the pressure regulating valve
19
and the entrance of the evaporator
11
.
The prior art pressure regulating valve
19
has intrinsic problems. That is, if the vapor pressure is higher than a given pressure (atmospheric pressure), the valve
19
is slightly open, because the valve mechanically operates in response to the difference between the vapor pressure and the spring force as mentioned above. If the hot gas is undesirably bypassed by the opening of the valve
19
, the refrigerating capability will be deteriorated. Especially, if the vapor pressure is low, the amount of refrigerant
16
circulated is small and so the refrigerating capability decreases conspicuously.
Accordingly, in the embodiments described below, the pressure regulating valve
19
is made to operate more precisely than the prior art pressure adjusting valve to prevent the refrigerating power from deteriorating.
In the chiller
10
shown in
FIG. 5
, a proportional valve
23
operating according to vapor pressure detected by a pressure sensor
25
is used instead of the prior art pressure regulating valve
19
.
That is, in this chiller
10
shown in
FIG. 5
, the proportional valve
23
is mounted in the hot gas bypass line
18
instead of the pressure regulating valve
19
.
This proportional valve
23
is driven by an electric motor
24
, and its degree of opening is adjusted according to the amount of motion of the motor
24
. This motor
24
is driven according to a command current delivered from the controller
21
.
A pressure sensor
25
is mounted in the line
15
between the evaporator
11
and the suction port
12
b
of the compressor
12
to detect the vapor pressure P of the refrigerant
16
inside the evaporator
11
. The vapor pressure is the pressure of gas evaporated from the refrigerant
16
inside the evaporator
11
.
The vapor pressure P detected by the pressure sensor
25
is applied to the controller
21
.
The controller
21
performs processing as illustrated in FIG.
4
.
First, a decision is made as to whether the actual vapor pressure P detected by the pressure sensor
25
is lower than a given pressure Pmin (e.g., atmospheric pressure corresponding to 0 kg/cm
2
on a pressure gauge) (step
201
).
If the result of the decision made in step
201
is YES (i.e., the actual vapor pressure P is lower than the atmospheric pressure Pmin (corresponding to 0 kg/cm
2
on the pressure gauge), an opening command current is delivered to the motor
24
to increase the amount of opening of the proportional valve
23
by a given amount, thus driving it. The proportional valve
23
is opened by a given amount. This increases the area of the opening of the hot gas bypass line
18
(step
202
).
On the other hand, if the result of the decision made in step
201
is NO (i.e., the actual vapor pressure P is equal to or higher than the atmospheric pressure Pmin (corresponding to 0 kg/cm
2
on the pressure gauge), then control goes to step
203
, where a decision is made as to whether the actual vapor pressure P detected is higher than a pressure Pmax (corresponding to 0.5 kg/cm
2
on the pressure gauge) that is sufficiently higher than the pressure Pmin.
If the result of the decision made in step
203
is NO (i.e., the actual vapor pressure P read by the gauge is equal to or lower than the pressure Pmax (0.5 kg/cm
2
) that is sufficiently higher than the atmospheric pressure, then the command current to the motor
24
is made to cease for a given time. Thus, the motor is in a standby state. That is, the degree of opening of the proportional valve
23
is maintained as it is. The degree of opening of the hot gas bypass line
18
is maintained for the given time (step
205
).
Then, control goes back to step
201
.
If the result of the decision made in step
203
is YES (i.e., the actual vapor pressure P is higher than Pmax (corresponding to 0.5 kg/cm
2
on the pressure gauge) that is sufficiently higher than the atmospheric pressure, a closing command current is delivered to the motor
24
to reduce the amount of opening of the proportional valve
23
by a given amount. As a result, the motor
24
is driven, closing the proportional valve
23
by the given amount. This reduces the area of the opening of the hot gas bypass line
18
(step
204
).
As described thus far, in the present embodiment, if the vapor pressure P detected by the pressure sensor
25
becomes equal to or lower than the given pressure (atmospheric pressure), the proportional valve
23
is opened. Therefore, the vapor pressure P is maintained higher than the given pressure (atmospheric pressure). Consequently, liquid the phenomenon of the fluid back (i.e., the vapor pressure becomes equal to or lower than the atmospheric pressure, the refrigerant
16
does not sufficiently vaporize in the evaporator
11
, and returns to the compressor
12
while maintained in a liquid state) can be prevented in the same way as the prior art pressure regulating valve
19
. That is, damage to the compressor
12
and other dangers can be prevented.
Furthermore, in accordance with the present embodiment, the proportional valve
23
is actuated precisely according to the vapor pressure P detected by the pressure sensor
25
. Therefore, if the vapor pressure P becomes higher than the given pressure (atmospheric pressure), the proportional valve
23
is prevented from being undesirably opened. Hence, the hot gas is prevented from being undesirably bypassed. In consequence, the refrigerating capability is prevented from deteriorating.
In this embodiment, the threshold value Pmin at which the proportional valve
23
is started to be opened is set to the atmospheric pressure. The threshold value may also be set to other values.
In the control illustrated in
FIG. 4
, the proportional valve
23
is opened or closed in equal increments. The proportional valve
23
may be so controlled as to achieve a target opening. In this case, in step
202
of
FIG. 4
, the proportional valve
23
is opened to a first target opening, or a large opening. In step
204
, the valve
23
is closed to a second target opening, or a small opening.
A modification of the machine shown in
FIG. 5
is next described by referring to FIG.
6
.
In the machine shown in
FIG. 6
, a solenoid valve
20
is used instead of the proportional valve
23
.
A controller
21
performs processing as illustrated in FIG.
7
.
First, a decision is made as to whether the actual vapor pressure P detected by the pressure sensor
25
is lower than a given pressure Pmin that is the atmospheric pressure corresponding to 0 kg/cm
2
on a pressure gauge (step
301
).
If the result of the decision made in step
301
is YES (i.e., the actual vapor pressure P is lower than the atmospheric pressure Pmin (corresponding to 0 kg/cm
2
on the pressure gauge), control proceeds to step
302
, where an ON command current is sent to the solenoid valve
20
to turn on the valve. As a result, the solenoid valve
20
is activated, opening the hot gas bypass line
18
(step
302
).
If the result of the decision made in step
301
is NO (i.e., the actual vapor pressure P is equal to or higher than the atmospheric pressure Pmin (corresponding to 0 kg/cm
2
on the pressure gauge), control goes to step
303
, where a decision is made as to whether the detected actual vapor pressure P is higher than a pressure Pmax (corresponding to 0.5 kg/cm
2
on the pressure gauge), the pressure Pmax being sufficiently higher than the pressure Pmin (step
303
).
If the result of the decision made in step
303
is NO (i.e., the actual vapor pressure P is equal to or lower than the pressure Pmax (corresponding to 0.5 kg/cm
2
on the pressure gauge), the pressure Pmax being sufficiently higher than the pressure Pmin, then the command current to the solenoid valve
20
is made to cease for a given time. The valve waits until the next command current is supplied. That is, the state of the solenoid valve
20
, whether it is open or closed, is maintained. The state of the hot gas bypass line
18
, whether it is open or closed, is maintained for the given time (step
305
).
Then control goes back to step
301
.
If the result of the decision made in step
303
is YES (i.e., the actual vapor pressure P is higher than the pressure Pmax (corresponding to 0.5 kg/cm
2
on the pressure gauge), the pressure Pmax being sufficiently higher than the atmospheric pressure, an OFF command current is delivered to the solenoid valve
20
to deactivate it. As a result, the solenoid valve
20
is deactivated, thus closing the hot gas bypass line
18
(step
304
).
Also in the embodiment illustrated in
FIG. 6
, the solenoid valve
20
is operated precisely according to the vapor pressure P detected by the pressure sensor
25
, in the same manner as the embodiment illustrated in FIG.
5
. Therefore, the vapor pressure can be maintained higher than the atmospheric pressure in the same way as the prior art pressure regulating valve
19
. Liquid the phenomenon of the fluid back and other inconveniences can be prevented. Furthermore, the hot gas is prevented from being undesirably bypassed; otherwise, the refrigerating capability would be deteriorated.
In this embodiment, the threshold value Pmin at which the solenoid valve
20
is started to be opened is set to the atmospheric pressure. Other threshold values may also be employed.
In the embodiments illustrated in
FIGS. 5 and 6
, the vapor pressure P is directly detected by the pressure sensor
25
. Instead, a temperature sensor may be installed in the line
15
between the evaporator
11
and the suction port
12
b
of the compressor
12
and between the thermostatic expansion valve and the evaporator to indirectly detect the vapor pressure P, because the vapor pressure P is uniquely determined by the temperature of the refrigerant
16
prior to passing through the evaporator
11
.
In this case, the temperature detected by the temperature sensor is applied to the controller
21
as shown in
FIGS. 5 and 6
. As illustrated in
FIGS. 4 and 7
, a temperature Tmin corresponding to the pressure Pmin is used instead of the pressure Pmin. Instead of the pressure Pmax, a temperature Tmax corresponding to the pressure Pmax is used. Similar processing is carried out.
In the embodiments described thus far, the discharge port
12
a
of the compressor
12
is placed in the hot gas bypass line
18
to connect the discharge port with the line between the thermostatic expansion valve
14
and the entrance of the evaporator
11
. The hot gas bypass line may also be arranged as shown in FIGS.
9
(
a
)-
9
(
c
).
In FIG.
9
(
a
), the discharge port
12
a
of the compressor
12
is placed in the hot gas bypass line
18
that places the discharge port
12
a
in communication with the line between the evaporator
11
and the suction port
12
b
of the compressor
12
.
In FIG.
9
(
b
), the discharge port
12
a
of the compressor
12
is connected with the hot gas bypass line
18
that places the discharge port
12
a
in communication with the vicinity of the outlet of the evaporator
11
.
In FIG.
9
(
c
), the discharge port
12
a
of the compressor
12
is connected with the hot gas bypass line
18
that places the discharge port
12
a
in communication with the line between the evaporator
11
and the suction port
12
b
of the compressor
12
. An expansion valve
14
′ for cooling the hot gas is added.
The refrigerating machine in accordance with the present embodiment is intended to cool the brine
17
passing through the evaporator
11
. The invention can also be applied to a heat pump having the condenser
11
to give heat to the outside air. That is, the refrigerating machine in accordance with the present invention embraces heat pumps as well as refrigerating machines.
Claims
- 1. A control unit for use with a refrigerating machine having a compressor, a condenser, and an evaporator that are connected in series via a conduit, said refrigerating machine having a refrigerant for exchanging heat with a brine passing through the evaporator to maintain said brine at a preset temperature, said control unit comprising:a hot gas bypass line providing a bypass line for hot gas discharged from said compressor such that said hot gas is supplied to a line between said condenser and said evaporator; a pressure regulating valve mounted in said hot gas bypass line to open said hot gas bypass line, if vapor pressure of the refrigerant inside said evaporator becomes equal to or lower than a given pressure, thereby passing the hot gas, and to close said hot gas bypass line, if the vapor pressure of the refrigerant inside said evaporator becomes higher than said given pressure, thereby cutting off said hot gas; and a temperature-responsive valve mounted in said hot gas bypass line to open said hot gas bypass line, if the preset temperature of said brine becomes equal to or higher than a given temperature, and to close said hot gas bypass line, if the preset temperature of said brine becomes lower than the given temperature.
- 2. The control unit of claim 1, wherein said temperature-responsive valve is a control valve opened and closed according to an ON/OFF command.
- 3. A control unit for use with a refrigerating machine having a compressor, a condenser, and an evaporator that are connected in series via a conduit, said refrigerating machine having a refrigerant for exchanging heat with a brine passing through the evaporator to maintain said brine at a preset temperature, said control unit comprising:a hot gas bypass line providing a bypass line for hot gas discharged from said compressor such that said hot gas is supplied to a line between said condenser and said evaporator; a pressure regulating valve mounted in said hot gas bypass line to open said hot gas bypass line, if vapor pressure of the refrigerant inside said evaporator becomes equal to or lower than a given pressure, thereby passing the hot gas, and to close said hot gas bypass line, if the vapor pressure of the refrigerant inside said evaporator becomes higher than said given pressure, thereby cutting off said hot gas; and a temperature-responsive valve mounted in said hot gas bypass line to open said hot gas bypass line, if actual temperature of said brine is set up equal to or higher than a given temperature, and to close said hot gas bypass line, if the actual temperature of said brine is set up lower than the given temperature.
- 4. The control unit of claim 3, wherein said temperature-responsive valve is a control valve opened and closed according to an ON/OFF command.
Priority Claims (1)
| Number |
Date |
Country |
Kind |
| 10-194329 |
Jul 1998 |
JP |
|
US Referenced Citations (8)
Foreign Referenced Citations (1)
| Number |
Date |
Country |
| 60-2777 |
Jan 1985 |
JP |