Patent Application
20120055184
The present invention relates to a centrifugal-chiller equipped with a variable-speed centrifugal-compressor and a constant-speed centrifugal-compressor and to a method for controlling the same.
Known heat source systems for use in supplying chilled water in semiconductor factories and zoned air conditioning are equipped with centrifugal-chillers. The centrifugal-chillers are equipped with centrifugal-compressors for compressing refrigerant. In general, one centrifugal-compressor is provided for one centrifugal-chiller. However, in the case where manufacturing costs can be reduced by using available general-purpose centrifugal-compressors or to cope with high capacity where sufficient performance cannot be achieved by one centrifugal-compressor, two centrifugal-compressors are sometimes provided for one centrifugal-chiller. In this case, however, centrifugal-compressors having the same capacity are generally disposed in parallel in consideration of ease of maintenance or operation.
On the other hand, for package air conditioners based on a principle different from that of the centrifugal-chillers, a known approach is to dispose two compressors in parallel. These compressors are a combination of a variable-speed compressor whose rotational frequency can be varied using an inverter and a constant-speed compressor operated at a constant rotational speed.
However, the compressors described in the foregoing Patent Literatures assume a scroll compressor or a rotary compressor and fundamentally differ in the principle of operation from a centrifugal-compressor, which is an aerodynamic rotary machine. Thus, an approach completely different from the scroll compressor and the rotary compressor is required in consideration of enhancing the efficiency of centrifugal-chillers. For example, a centrifugal-chiller that uses a variable-speed centrifugal-compressor whose rotational frequency can be varied using an inverter shows a high COP (coefficient of performance of the centrifugal-chiller) in regions at a low cooling-water temperature (outside-air wet-bulb temperature) and shows an extremely high COP in regions at a low cooling-water temperature and a low compressor load factor. Furthermore, it has the characteristic that the COP is decreased by an amount corresponding to an inverter loss at a high cooling-water temperature and a high compressor load factor as compared with the constant-speed compressor operated at a constant rotational speed. On the other hand, a centrifugal-chiller that uses a constant-speed centrifugal-compressor shows a low COP at a low compressor load factor and shows a high COP at a high compressor load factor. Thus, with the use of two compressors, that is, one variable-speed centrifugal-compressor and one constant-speed centrifugal-compressor, for one centrifugal-chiller energy-saving combinations and operation control methods can be expected.
Furthermore, in the case where the capacity of the centrifugal-chiller is so large that two centrifugal-compressors are needed, two constant-speed centrifugal-compressors may be provided; however, enhancement of the efficiency cannot be expected at a low compressor load factor. On the other hand, two variable-speed centrifugal-compressors may be provided, in which case two inverters are needed, thus posing problems in terms of cost and maintenance. Thus, a combination of one variable-speed centrifugal-compressor and one constant-speed centrifugal-compressor may be provided. At present, however, there are no proposals to optimally enhance the efficiency of such a combination of centrifugal-compressors.
The present invention is made in consideration of such circumstances and provides a centrifugal-chiller equipped with one variable-speed centrifugal-compressor and one constant-speed centrifugal-compressor to allow a high efficiency operation, as well as a method for controlling the same.
To solve the above problems, a centrifugal-chiller and a method for controlling the same of the present invention adopt the following solutions.
A centrifugal-chiller according to a first aspect of the present invention includes a variable-speed centrifugal-compressor whose rotational frequency can be varied by an inverter and which compresses a refrigerant; a constant-speed centrifugal-compressor connected in parallel with the variable-speed centrifugal-compressor and operated at a constant rotational speed to compress the refrigerant; a condenser that condenses the refrigerant compressed by the variable-speed centrifugal-compressor and/or the constant-speed centrifugal-compressor into a liquid using cooling water supplied thereto; an expansion valve that expands the refrigerant that is condensed into a liquid by the condenser; an evaporator that evaporates the refrigerant expanded by the expansion valve; and a control unit that controls the operations of the variable-speed centrifugal-compressor and the constant-speed centrifugal-compressor, wherein in the case where a required load factor of the centrifugal-chiller is less than a predetermined value, the control unit selects a variable-speed-compressor priority operating mode in which only the variable-speed centrifugal-compressor is activated, and in the case where the required load factor of the centrifugal-chiller is the predetermined value or greater, the control unit selects a combined-use operating mode in which the variable-speed centrifugal-compressor and the constant-speed centrifugal-compressor are activated.
A centrifugal-chiller that uses a variable-speed centrifugal-compressor whose rotational frequency can be varied by an inverter has the characteristic of showing a relatively high COP (coefficient of performance of the centrifugal-chiller) at a low compressor load factor, and showing a decreased COP at a high compressor load factor. This tendency is notable at a low cooling water temperature as in the winter season.
On the other hand, a centrifugal-chiller that uses a constant-speed centrifugal-compressor operated at a constant rotational speed shows a low COP at a low compressor load factor and shows a high COP at a high compressor load factor. This tendency is notable at a high cooling water temperature as in the summer season.
In the centrifugal-chiller according to the first aspect of the present invention, in the case where the load factor of the centrifugal-chiller is less than a predetermined value, the variable-speed-compressor priority operating mode in which only the variable-speed centrifugal-compressor whose compressor load factor is less than the predetermined value is selected, and in the case where the load factor of the centrifugal-chiller is the predetermined value or greater, the combined-use operating mode in which both the variable-speed and the constant-speed centrifugal-compressors are activated is selected because the compressor load factors of the individual compressors are the predetermined value or greater in consideration of the characteristics. In the case of operation of only one compressor, the centrifugal-chiller load factor corresponds to the load factor of the compressor, and in the case of operation of two compressors, it corresponds to the sum of the load factors of the compressors.
In general, in a state in which the cooling water temperature is relatively low as in the winter season or in the intermediate seasons, the centrifugal-chiller load factor frequently becomes low and the compressor load factor becomes less than a predetermined value, in which case, a high-efficiency operation is achieved only by the variable-speed centrifugal-compressor by selecting the variable-speed-compressor priority operating mode. On the other hand, since the centrifugal-chiller load factor rises, so that the compressor load factor becomes the predetermined value or greater in the summer season during which the cooling water temperature is relatively high, a high-efficiency operation can be achieved by shifting to the combined-use operating mode. Thus, a centrifugal-chiller that shows a high COP across wide compressor load factors can be achieved by combining the variable-speed-compressor priority operating mode and the combined-use operating mode.
In the centrifugal-chiller according to the first aspect of the present invention described above, the predetermined value of the load factor of the centrifugal-chiller may be set to 30% or greater and less than 50%.
The predetermined value of the load factor of the centrifugal-chiller, that is, a threshold for switching between the variable-speed-compressor priority operating mode and the combined-use operating mode, is set to 30% or greater and less than 50%. This allows the variable-speed centrifugal-compressor to be operated mainly in the variable-speed-compressor priority operating mode in which the load factor of the centrifugal-chiller is set low, thus allowing the variable-speed centrifugal-compressor having a relatively low capacity to be selected. That is, it suffices that the variable-speed centrifugal-compressor have a capacity corresponding to a centrifugal-chiller load factor of 30% or higher and less than 50%. Accordingly, it suffices to employ a variable-speed centrifugal-compressor having a capacity of about half or less than that of the constant-speed centrifugal-compressor, which allows a general-purpose inverter to be used, thus allowing the centrifugal-compressor to be configured at low cost.
The predetermined value of the compressor load factor, which serves as a threshold, is preferably set to the lower limit of a region in which the efficiency of the constant-speed centrifugal-compressor is a predetermined value or greater (for example, within 20% of the highest efficiency). This can prevent the constant-speed centrifugal-compressor from being activated at a low compressor load factor which would decrease the efficiency of the centrifugal-chiller.
The capacity of the constant-speed centrifugal-compressor is selected so that the sum of it and the capacity of the variable-speed centrifugal-compressor satisfies the centrifugal-chiller load factor of 100%. For example, in the case where the variable-speed centrifugal-compressor has a capacity corresponding to centrifugal-centrifugal-chiller load factor of 30%, the constant-speed centrifugal-compressor is set to a capacity corresponding to a centrifugal-centrifugal-chiller load factor of 70%.
In the centrifugal-chiller according to the first aspect of the present invention described above, an inlet guide vane that controls the flow rate of the refrigerant flowing to an impeller of the constant-speed centrifugal-compressor may be provided upstream of the impeller in the flow of the refrigerant; and a wall facing the inlet guide vane may have a sealing portion that minimizes leakage of the refrigerant through the gap between the inlet guide vane and the wall when the inlet guide vane is fully closed.
The constant-speed centrifugal-compressor is not activated when the variable-speed-compressor priority operating mode is selected. Since the constant-speed centrifugal-compressor is connected in parallel with the variable-speed centrifugal-compressor, a pressure difference in refrigerant is generated in front of and behind the constant-speed centrifugal-compressor even in the variable-speed-compressor priority operating mode. When the refrigerant leaks from the high pressure side to the low pressure side due to the pressure difference, a refrigerant flow that does not contribute to refrigeration is generated, and thus, the performance of the chiller deteriorates.
Thus, the centrifugal-chiller according to the first aspect of the present invention has a sealing section that minimizes refrigerant leakage between the inlet guide vane and the wall, thereby minimizing refrigerant leakage when the inlet guide vane is fully closed. Thus, even in the variable-speed-compressor priority operating mode, the amount of refrigerant leaked via the constant-speed centrifugal-compressor is minimized, so that deterioration in the performance of the chiller can be prevented. Furthermore, since the refrigerant leakage in the constant-speed centrifugal-compressor is minimized, there is no need to provide additional automatic on/off valve in the refrigerant piping.
An example of the sealing section is a labyrinth seal formed at the wall side.
A method for controlling a centrifugal-chiller according to a second aspect of the present invention is a method for controlling a centrifugal-chiller including a variable-speed centrifugal-compressor whose rotational frequency can be varied by an inverter and which compresses a refrigerant; a constant-speed centrifugal-compressor connected in parallel with the variable-speed centrifugal-compressor and operated at a constant rotational speed to compress the refrigerant; a condenser that condenses the refrigerant compressed by the variable-speed centrifugal-compressor and/or the constant-speed centrifugal-compressor into a liquid using cooling water supplied thereto; an expansion valve that expands the refrigerant that is condensed into a liquid by the condenser; and an evaporator that evaporates the refrigerant expanded by the expansion valve, the method controlling the operations of the variable-speed centrifugal-compressor and the constant-speed centrifugal-compressor, wherein in the case where a required load factor of the centrifugal-chiller is less than a predetermined value, the control unit selects a variable-speed-compressor priority operating mode in which only the variable-speed centrifugal-compressor is activated, and in the case where the required load factor of the centrifugal-chiller is the predetermined value or greater, the control unit selects a combined-use operating mode in which the variable-speed centrifugal-compressor and the constant-speed centrifugal-compressor are activated.
A centrifugal-chiller that uses a variable-speed centrifugal-compressor whose rotational frequency can be varied by an inverter has the characteristic of showing a relatively high COP (coefficient of performance of the centrifugal-chiller) at a low compressor load factor, and showing a decreased COP at a high compressor load factor. This tendency is notable at a low cooling water temperature as in the winter season.
On the other hand, a centrifugal-chiller that uses a constant-speed centrifugal-compressor operated at a constant rotational speed shows a low COP at a low compressor load factor and shows a high COP at a high compressor load factor. This tendency is notable at a high cooling water temperature as in the summer season.
In the method for controlling the centrifugal-chiller according to the second aspect of the present invention, in the case where the load factor of the centrifugal-chiller is less than a predetermined value, the variable-speed-compressor priority operating mode in which only the variable-speed centrifugal-compressor whose compressor load factor is less than the predetermined value is selected, and in the case where the load factor of the centrifugal-chiller is the predetermined value or greater, the combined-use operating mode in which both the variable-speed and the constant-speed centrifugal-compressors are activated is selected because the compressor load factors of the individual compressors are the predetermined value or more in consideration of the characteristics. The centrifugal-chiller load factor corresponds to a compressor load factor in the case of operation of only one compressor and corresponds to the sum of compressor load factors in the case of the operation of two compressors.
In general, in a state in which the cooling water temperature is relatively low as in the winter season or in the intermediate seasons, the centrifugal-chiller load factor frequently becomes low and the compressor load factor becomes less than a predetermined value, in which case, a high-efficiency operation is achieved only by the variable-speed centrifugal-compressor by selecting the variable-speed-compressor priority operating mode. On the other hand, since the centrifugal-chiller load factor rises, so that the compressor load factor becomes the predetermined value or greater in the summer season during which the cooling water temperature is relatively high, a high-efficiency operation can be achieved by shifting to the combined-use operating mode. Thus, a centrifugal-chiller that shows a high COP across wide compressor load factors can be achieved by combining the variable-speed-compressor priority operating mode and the combined-use operating mode.
The centrifugal-chiller and the method for controlling the same according to the present invention provide the following operational advantages.
In the case where the load factor of the centrifugal-chiller is less than a predetermined value, a variable-speed-compressor priority operating mode in which only the variable-speed centrifugal-compressor is activated is selected, and in the case where the load factor of the centrifugal-chiller is the predetermined value or greater, a combined-use operating mode in which the variable-speed centrifugal-compressor and the constant-speed centrifugal-compressor are activated is selected, and thus, a centrifugal-chiller that shows a high COP across wide compressor load factors can be achieved.
When the cooling water temperature is low as in the winter season during which the cooling water temperature is a predetermined value or less, the variable-speed-compressor priority operating mode is selected, and thus, higher efficiency is achieved.
When the cooling water temperature is high as in the summer season during which the cooling water temperature is a predetermined value or greater, the combined-use operating mode is selected, and thus, higher efficiency is achieved.
For the intermediate seasons during which the cooling water temperature is not high as in the summer season and not low as in the winter season, the variable-speed-compressor priority operating mode is selected in the case where the load factor of the centrifugal-chiller is less than a predetermined value, and the combined-use operating mode is selected in the case where the load factor of the centrifugal-chiller is the predetermined value or greater, and a further increased efficiency is achieved.
A sealing section that minimizes refrigerant leakage is provided between the inlet guide vane and the wall, thereby minimizing refrigerant leakage when the inlet guide vane is fully closed. Thus, even in the variable-speed-compressor priority operating mode, the amount of refrigerant leaked via the constant-speed centrifugal-compressor is minimized, so that deterioration in the performance of the chiller can be prevented.
An embodiment of the present invention will be described hereinbelow with reference to the drawings.
The centrifugal-chillers 3 are each equipped with two centrifugal-compressors 7 and 8 that compress a refrigerant, a condenser 9 that condenses the refrigerant compressed by the centrifugal-compressors 7 and 8 to liquefy it, an expansion valve (not shown) that expands the refrigerant condensed and liquefied by the condenser 9, and an evaporator 11 that evaporates the refrigerant expanded by the expansion valve.
One centrifugal-compressor 7 of the two is driven by an electric motor 13 whose rotational frequency can be varied by an inverter. Thus, the centrifugal-compressor 7 is a variable-speed centrifugal-compressor.
The other centrifugal-compressor 8 is a constant-speed centrifugal-compressor that is operated at a fixed rotational speed by an electric motor 14.
Cooling water supplied by a cooling-water pump 15 is guided to the condenser 9. The cooling-water pump 15 is driven by an electric motor (not shown) whose rotational frequency can be varied by an inverter. The inlet temperature of the cooling water supplied to the condenser 9 and the output temperature of the cooling water flowing out from the condenser 9 are measured by temperature sensors (not shown), and the output values are transmitted to a control unit, to be described later.
The individual cooling-water pumps 15 suck cooling water guided from a cooling-water return header 17 and discharge it toward the condenser 9. The cooling water discharged from the condenser 9 side is guided to a cooling-water supply header 19. All of the centrifugal-chillers 3 and all of the cooling towers 5 are connected in common to the cooling-water return header 17. All of the centrifugal-chillers 3 and all of the cooling towers 5 are connected in common also to the cooling-water supply header 19.
Cooling water supplied by a chilled water pump 21 is guided to the evaporator 11. The chilled-water pump 21 is driven by an electric motor (not shown) whose rotational frequency can be varied by an inverter. The inlet temperature of the chilled water supplied to the evaporator 11 and the output temperature of the chilled water flowing out from the evaporator 11 are measured by temperature sensors (not shown), and the output values are transmitted to the control unit, to be described later. The flow rate of the chilled water is also measured by a flowmeter, and the output value is transmitted to the control unit, to be described later. The control unit calculates a load consumed by an external load by multiplying the difference between the chilled-water inlet and outlet temperatures, the cooling-water flow rate, the specific heat of the chilled water, and the specific gravity of the chilled water together.
The individual chilled water pumps 21 suck chilled water guided from a chilled-water return header 23 and discharge it toward the evaporator 11. The chilled water discharged from the evaporator 11 side is guided to a chilled-water supply header 25. All of the centrifugal-chillers 3 are connected in common to the chilled-water return header 23. All of the centrifugal-chillers 3 are connected in common also to the chilled-water supply header 25.
The chilled-water return header 23 and the chilled-water supply header 25 are connected to the external load (not shown). The external load is supplied with chilled water (for example, at 7° C.) cooled by the evaporator 11 through the chilled-water supply header 25, and the chilled water that is used by the external load and has its temperature increased (for example, to 12° C.) is returned to the evaporator 11 side through the chilled-water return header 23.
The cooling towers 5 are each provided with a cooling tower fan 30, a water spray header 32, and a cooling-water reservoir tank 34.
The cooling tower fan 30 is used to introduce outside air into the cooling tower 5 and is driven by an electric motor 36. The electric motor 36 preferably has a rotational frequency that can be varied by an inverter.
The water spray header 32 sprays cooling water into outside air from above to bring it into contact with the outside air, thereby cooling the cooling air using not only sensible heat but also latent heat of vaporization. A cooling-water supply on/off valve 38 is provided between the water spray header 32 and the cooling-water supply header 19.
The cooling-water reservoir tank 34 reserves the cooled cooling water sprayed and cooled by the outside air. The cooling water reserved in the cooling-water reservoir tank 34 is guided to the cooling-water return header 17 via a cooling-water return on/off valve 40.
The cooling towers 5 are each activated and stopped by opening and closing the cooling-water supply on/off valve 38 and the cooling-water return on/off valve 40. Thus, the number of cooling towers 5 to be activated can be changed.
The cooling towers 5 are each provided with a humidity sensor (not shown). The humidity sensor measures an outside-air wet-bulb temperature. The output of the humidity sensor is sent to the control unit, to be described later. The outside-air wet-bulb temperature may be determined from a dry-bulb temperature, a relative humidity, and an outside air pressure, instead of using the humidity sensor.
The heat source system is equipped with the control unit (not shown), and the control unit controls the operations of the centrifugal-compressors 7 and 8, the expansion valves, the cooling-water pumps 15, the cooling tower fans 30, the cooling-water supply on/off valves 38, the cooling-water return on/off valves 40, and the chilled water pumps 21.
The above-configured heat source system 1 operates as follows.
The centrifugal-compressors 7 and 8 are activated in accordance with an instruction from the control unit to compress the refrigerant. The order of activation of the centrifugal-chillers 7 and 8 will be described later.
The refrigerant compressed by the centrifugal-chillers 7 and 8 is guided to the condenser 9 and cooled by cooling water supplied from the cooling-water return header 17 by the cooling-water pump 15 to be condensed to a liquid. The cooling water that has been given latent heat of condensation by the condenser 9 to raise its temperature is guided to the cooling-water supply header 19 and is guided to the water spray header 32 via the cooling-water supply on/off valve 38. The cooling water is sprayed into the outside air from the water spray header 32 and is cooled by coming into contact with the outside air guided by the cooling tower fan 30. The cooled cooling water is temporarily reserved in the cooling-water reservoir tank 34 and is then guided to the cooling-water return header 17 via the cooling-water return on/off valve 40. Thus, the cooling water circulates between the condenser 9 and the cooling tower 5
The liquid refrigerant condensed into a liquid by the condenser 9 is expanded by the expansion valve (not shown) and is then guided to the evaporator 11. The evaporator 11 evaporates the liquid refrigerant to absorb latent heat of vaporization from the chilled water to cool the chilled water. The chilled water is guided from the chilled-water return header 23 to the evaporator 11 by the chilled water pump 21, is cooled to a desired temperature (for example, 7° C.) by the evaporator 11, and is guided to the chilled-water supply header 25. The chilled-water supply header 25 is connected to the external load (not shown), where the chilled water is used by the external load and has its temperature increased to a predetermined temperature (for example, 12° C.) and is then returned to the chilled-water return header 23.
The refrigerant evaporated by the evaporator 11 is guided to the intake ports of the centrifugal-compressors 7 and 8, where it is compressed again.
Next, a method for activating the centrifugal-compressors 7 and 8 will be described using
In the drawing, broken lines indicate the variable-speed centrifugal-compressor 7, and two-dot chain lines indicate the constant-speed centrifugal-compressor 8. The curved lines indicate COPs at cooling-water inlet temperatures (the temperatures of cooling water flowing into the condenser 9), specifically, 12° C., 20° C., and 32° C. The cooling-water inlet temperature, 12° C., represents the winter season, 20° C. represents daytime in intermediate seasons and night in the summer season (hereinafter simply referred to as “intermediate seasons”), and 32° C. represents daytime in the summer season (hereinafter simply referred to as “summer season”).
As shown in the drawing, the centrifugal-chiller that uses the centrifugal-compressor 7 has the characteristic of showing a relatively high COP at a low centrifugal-chiller load factor and showing a decreased COP at a high centrifugal-chiller load factor, at a low cooling water temperature (for example, 12° C.), as in the winter season. On the other hand, the centrifugal-chiller that uses the constant-speed centrifugal-compressor 8 shows a significantly decreased COP at a low centrifugal-chiller load factor and a constant high COP at a high centrifugal-chiller load factor, at a high cooling water temperature (for example, 30° C.).
This embodiment performs operation control as follows on the basis of the characteristics of the centrifugal-compressors described above.
In the case where the load factor of the centrifugal-chiller is less than a predetermined value (for example, 30%), only the variable-speed centrifugal-compressor 7 is activated (variable-speed-compressor priority operating mode), and in the case where the load factor of the centrifugal-chiller is the predetermined value or greater, both the centrifugal-compressors 7 and 8 are activated to the rating (combined-use operating mode). The threshold load factor of the centrifugal-chiller is not limited to 30% and is suitably set depending on the characteristics of the centrifugal-chiller. However, it is preferable to set the threshold value between 30% or more and less than 50%.
In the case where the load factor of the centrifugal-chiller, which serves as the threshold for switching between the operations of the centrifugal-compressors, is set to 30%, a capacity of about 30% of the rated output is selected for the variable-speed centrifugal-compressor 7, and a capacity of about 70% of the rating is selected for the constant-speed centrifugal-compressor 8.
In the region where the centrifugal-chiller load factor is 30% or less, COPs of the variable-speed centrifugal-compressor 7 higher than the COPs of the constant-speed centrifugal-compressor 8 are selected, as indicated by the bold solid lines in the drawing. In general, a centrifugal-chiller load factor of less than 30% is for operation in the winter season (region A) and the intermediate seasons (region B). Accordingly, a centrifugal-chiller load factor of less than 30% allows high-efficiency operation to be achieved by selecting the variable-speed centrifugal-compressor 7.
In the region where the centrifugal-chiller load factor is 30% or higher and 100% or less, the intermediate values of the COPs of the constant-speed centrifugal-compressor 8 and the variable-speed centrifugal-compressor 7 are selected as indicated by the bold solid lines in the drawing. The region where the centrifugal-chiller load factor is 30% or more and 100% or less is for operation in the intermediate seasons (region B) and the summer season (region C). Since the COP of the constant-speed centrifugal-compressor 8 is sufficiently improved at cooling-water inlet temperatures in the intermediate seasons and the summer season when the load factor of the centrifugal-chiller exceeds 30%, high-efficiency operation can be achieved even by combined-use operation of the centrifugal-chillers 7 and 8.
Thus, this embodiment can achieve the centrifugal-chiller 3 that shows high COPs across wide load factors of the centrifugal-chiller by combining the variable-speed-compressor priority operating mode and the combined-use operating mode.
Furthermore, the load factor of the centrifugal-chiller, which serves as a threshold for switching between the variable-speed-compressor priority operating mode and the combined-use operating mode, is set to 30% or higher and less than 50%. This allows the variable-speed centrifugal-compressor 7 to be operated mainly in the variable-speed-compressor priority operating mode in which the load factor of the centrifugal-chiller is set low, thus allowing the variable-speed centrifugal-compressor 7 having a relatively low capacity to be selected. That is, it suffices that the variable-speed centrifugal-compressor 7 have a capacity corresponding to a centrifugal-chiller load factor of 30% or more and less than 50%. Accordingly, it suffices to employ a variable-speed centrifugal-compressor having a capacity of about half or less compared with that of the constant-speed centrifugal-compressor 8, which allows a general-purpose inverter to be used, thus allowing the centrifugal-compressor to be configured at low cost.
Next, the configuration of an inlet guide vane provided in the constant-speed centrifugal-compressor 8 will be described using
An inlet guide vane 50 is provided upstream of an impeller (not shown) of the constant-speed centrifugal-compressor 8 and controls the flow rate of the refrigerant flowing to the impeller. The inlet guide vane 50 is provided between a central shaft 52 and a peripheral ring 54, in which a plurality of vanes 56 are disposed in a radiating pattern. The vanes 56 are plate-like members each having a substantially sector shape. The individual vanes 56 rotate about a rotation axis 58 passing through the center of the central shaft 52. The state in
The labyrinth seals are provided between the individual vanes 56 and the peripheral ring 54 and the central shaft 52 in this manner to minimize refrigerant leakage in the fully closed state. Thus, even in the case were a pressure difference in refrigerant is generated in front and behind the constant-speed centrifugal-compressor 8 due to the variable-speed centrifugal-compressor 7 disposed in parallel even though the constant-speed centrifugal-compressor 8 is not activated, as in the variable-speed-compressor priority operating mode, the inlet guide vane is fully closed to minimize refrigerant leakage. Thus, even in the variable-speed-compressor priority operating mode, the amount of refrigerant leaked via the constant-speed centrifugal-compressor is minimized, so that deterioration in the performance of the chiller can be prevented. Furthermore, since the refrigerant leakage in the constant-speed centrifugal-compressor 8 is minimized, there is no need to provide an additional on/off valve in refrigerant piping.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2009-087515 | Mar 2009 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2010/055663 | 3/30/2010 | WO | 00 | 9/1/2011 |
