Control unit for refrigerating machine

Information

  • Patent Grant
  • 6311506
  • Patent Number
    6,311,506
  • Date Filed
    Wednesday, July 7, 1999
    27 years ago
  • Date Issued
    Tuesday, November 6, 2001
    24 years ago
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)
Number Name Date Kind
3368364 Norton et al. Feb 1968
3555843 Cook Jan 1971
4749312 Raibaud Jun 1988
4926733 Jason May 1990
4957085 Sverdlin Sep 1990
5076068 Mikhail Dec 1991
5183101 Penaluna et al. Feb 1993
5551249 Van Steenburgh, Jr. Sep 1996
Foreign Referenced Citations (1)
Number Date Country
60-2777 Jan 1985 JP