Patent Grant
10746182
The present invention relates to a multi-stage compressor system, a control device, a malfunction determination method, and a program.
Priority is claimed on Japanese Patent Application No. 2014-136051, filed Jul. 1, 2014, the content of which is incorporated herein by reference.
A compressor which compresses gases and supplies the compressed gases to machines or the like connected to a downstream side of a gas system is known. As this compressor, there is a compressor in which a gas flow rate for a compressor body is adjusted by arranging an inlet guide vane (IGV) at an upstream side and adjusting the degree of opening of the IGV.
In Patent Document 1, technology of appropriately controlling a degree of opening of the IGV and performing an optimum operation even when a performance difference occurs between two first-stage compressor bodies among a plurality of compressor bodies is disclosed as related technology.
[Patent Document 1]
Japanese Unexamined Patent Application, First Publication No. 2013-170573
By the way, in a multi-stage compressor as disclosed in Patent Document 1 when a flow rate meter provided in a first compressor is in an abnormal state and a result of measuring a gas flow rate higher than an actual gas flow rate is shown, an operation is performed at a low gas flow rate by correcting flow rate deviation on the basis of a result of erroneously measuring the gas flow rate. Thus, it is likely to be in a surge state. In this case, because the flow rate meter is in the abnormal state, anti-surge control for preventing the surge state using the flow rate meter is also likely not to be normally operated.
In addition, when a phenomenon in which an amount of leakage of a gas is increased by the breakdown or the like of the seal part occurs in the multi-stage compressor as disclosed in Patent Document 1, the leakage of the gas is unlikely to be detected.
Also, a method based on redundancy or the like is considered to detect a malfunction of a measuring instrument such as a flow rate meter. However, when the method based on redundancy is used, the cost is likely to increase.
Thus, technology capable of detecting a malfunction in the multi-stage compressor system without making a measuring instrument redundant is required.
The present invention provides a multi-stage compressor system, a control device, a malfunction determination method, and a program capable of solving the above-described problem.
According to a first aspect of the present invention, a multi-stage compressor system is a system of a multi-stage compressor in which compressors are connected in series in a plurality of stages, the multi-stage compressor system including: a control unit configured to determine whether a malfunction is present in the system by comparing a suction flow rate of a first-stage compressor measured by a first sensor with a downstream flow rate from an outlet of the multi-stage compressor measured by a second sensor.
According to a second aspect of the present invention, in the multi-stage compressor system, the multi-stage compressor includes a pair of first-stage compressors and subsequent-stage compressors, wherein the subsequent-stage compressors serially connected to the first-stage compressors compress fluids compressed by the pair of first-stage compressors.
According to a third aspect of the present invention, in the multi-stage compressor system, a measurement value of each of the first sensor and the second sensor is corrected according to at least one of a temperature of a fluid, a pressure of the fluid, and a molecular weight of the fluid in which the first sensor and the second sensor measure.
According to a fourth aspect of the present invention, in the multi-stage compressor system, a third sensor configured to measure an amount of drainage downstream generated from a compressed fluid from an outlet of the first-stage compressor is provided, and measurement values of the first sensor and the second sensor are corrected according to the amount of drainage measured by the third sensor.
According to a fifth aspect of the present invention, in the multi-stage compressor system, a pressure of a fluid is measured at an upstream side of the first sensor and a temperature of the fluid is measured at a downstream side of the first sensor.
According to a sixth aspect of the present invention, a control device is a control device for a multi-stage compressor in which compressors are connected in series in a plurality of stages, the control device including: a control unit configured to determine whether a malfunction is present in the system by comparing a suction flow rate of a first-stage compressor measured by a first sensor with a downstream flow rate from an outlet of the multi-stage compressor measured by a second sensor.
According to a seventh aspect of the present invention, in the control device, the multi-stage compressor includes a pair of first-stage compressors and subsequent-stage compressors, wherein the subsequent-stage compressors serially connected to the first-stage compressors compress fluids compressed by the pair of first-stage compressors.
According to an eighth aspect of the present invention, in the control device, a measurement value of each of the first sensor and the second sensor is corrected according to at least one of a measured temperature of a fluid, a measured pressure of the fluid, and a measured molecular weight of the fluid around the sensor.
According to a ninth aspect of the present invention, in the control device, a third sensor configured to measure an amount of drainage downstream generated from a compressed fluid from an outlet of the first-stage compressor is provided, and measurement values of the first sensor and the second sensor are corrected according to the amount of drainage measured by the third sensor.
According to a tenth aspect of the present invention, in the control device, a pressure of a fluid is measured at an upstream side of the first sensor and a temperature of the fluid is measured at a downstream side of the first sensor.
According to an eleventh aspect of the present invention, a malfunction determination method is a malfunction determination method for use in a system of a multi-stage compressor in which compressors are connected in series in a plurality of stages, the malfunction determination method including: determining, by a control unit, whether a malfunction is present in the system by comparing a suction flow rate of a first-stage compressor measured by a first sensor with a downstream flow rate from an outlet of the multi-stage compressor measured by a second sensor.
According to a twelfth aspect of the present invention, in the malfunction determination method, the multi-stage compressor includes a pair of first-stage compressors and subsequent-stage compressors, wherein the subsequent-stage compressors serially connected to the first-stage compressors compress fluids compressed by the pair of first-stage compressors.
According to a thirteenth aspect of the present invention, in the malfunction determination method, a measurement value of each of the first sensor and the second sensor is corrected according to at least one of a temperature of a fluid, a pressure of the fluid, and a molecular weight of the fluid in which the first sensor and the second sensor measure.
According to a fourteenth aspect of the present invention, in the malfunction determination method, a third sensor configured to measure an amount of drainage downstream generated from a compressed fluid from an outlet of the first-stage compressor is provided, and measurement values of the first sensor and the second sensor are corrected according to the amount of drainage measured by the third sensor.
According to a fifteenth aspect of the present invention, in the malfunction determination method, a pressure of a fluid is measured at an upstream side of the first sensor and the temperature of the fluid is measured at a downstream side of the first sensor.
According to a sixteenth aspect of the present invention, a program is a program configured to cause a computer of a control device for controlling a multi-stage compressor in which compressors are connected in series in a plurality of stages to function as: a control means configured to determine whether a malfunction is present in the system by comparing a suction flow rate of a first-stage compressor measured by a first sensor with a downstream flow rate from an outlet of the multi-stage compressor measured by a second sensor.
According to a seventeenth aspect of the present invention, the program causes the computer to function as: a means configured to correct a measurement value of each of the first sensor and the second sensor according to at least one of a measured temperature of a fluid, a measured pressure of the fluid, and a measured molecular weight of the fluid around the sensor.
According to an eighteenth aspect of the present invention, the program causes the computer to function as: a means configured to correct measurement values of the first sensor and the second sensor according to the amount of drainage measured by a third sensor configured to measure an amount of drainage downstream generated from a compressed fluid from an outlet of the first-stage compressor.
According to the multi-stage compression system, the control device, the malfunction determination method, and the program described above, it is possible to detect a malfunction in a multi-stage compressor system without making a measuring instrument redundant.
As shown in
The multi-stage compressor 10 includes a first-stage compressor body 101, a last-stage compressor body 102, and a second-stage compressor body 103.
The first-stage compressor body 101 is a first-stage compressor body of the multi-stage compressor 10. The first-stage compressor body 101 takes in a gas and generates a compressed gas.
The last-stage compressor body 102 is a compressor body of a last stage of the multi-stage compressor 10. The last-stage compressor body 102 takes in a gas compressed in a previous stage and generates a compressed gas.
The second-stage compressor body 103 is connected to the first-stage compressor body 101 in series. The second-stage compressor body 103 takes in the gas compressed by the first-stage compressor body 101. The second-stage compressor body 103 compresses the taken in gas and discharges the compressed gas to a third-stage compressor body of a subsequent stage connected in series. Likewise, a compressor body of a stage subsequent to the third-stage compressor body is connected in series. Also, each compressor body of a stage subsequent to the third-stage compressor body similarly takes in a compressed gas, compresses the taken in gas, and outputs the compressed gas to a subsequent-stage compressor body.
The first sensor 20a measures a flow rate of a gas taken in by the first-stage compressor body 101.
The second sensor 20b measures a flow rate of a gas discharged by the last-stage compressor body 102.
The control unit 30 compares a gas flow rate measured by the first sensor 20a with a gas flow rate measured by the second sensor 20b and determines whether two measurement values are the same within a predetermined error range.
When it is determined that the two measurement values are the same within the predetermined error range, the control unit 30 determines that the multi-stage compressor system 1 is normal.
Also, when it is determined that the two measurement values are not the same within the predetermined error range, the control unit 30 determines that a malfunction is occurring in the multi-stage compressor system 1.
Also, when the multi-stage compressor system 1 is normal, this determination is based on the fact that all the gas taken in by the first-stage compressor body 101 is discharged by passing through the second-stage compressor body 103, the subsequent-stage compressor body, and the last-stage compressor body 102. When a measurement value of a flow rate of a gas taken in by the first-stage compressor body 101 is different from a measurement value of a flow rate of a gas discharged by passing through the second- and subsequent-stage compressor bodies including the last-stage compressor body 102, a malfunction of the measuring instrument is first considered. When no malfunction is found in the measuring instrument, the gas between the first-stage compressor body 101 and the second- and subsequent-stage compressor bodies is likely to have been leaked. When the gas is leaked between the first-stage compressor body 101 and the second- and subsequent-stage compressor bodies, there is a possibility of a breakdown of a seal part of the compressor.
When a flow rate measurement result from the first sensor 20a and a flow rate measurement result from the second sensor 20b are different, the control unit 30 notifies the user that some malfunction might be occurring in the multi-stage compressor system 1 via the notification unit 40. For example, the notification unit 40 is a display, a speaker, a vibration device, or the like. The notification unit 40 may display “Please confirm whether the measuring device is normal.” or “Gas is likely leaking.” or provide a notification by sound. Also, the notification unit 40 may cause the malfunction of the multi-stage compressor system 1 to be known by vibration.
Also, the control unit 30 may stop flow rate deviation correction when it is determined that a malfunction is likely to have occurred in the multi-stage compressor system 1. Also, the control unit 30 may control a blowoff valve 108 to be opened to a fixed degree of opening in order to prevent a surge operation. In addition, the control unit 30 may stop the system.
As described above, in the multi-stage compressor system 1, the control unit 30 compares the flow rates of gases taken in by the first-stage compressor body 101, which is measured by the first sensor 20a, with the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the second sensor 20b. When the flow rates of gases taken in by the first-stage compressor body 101, which is measured by the first sensor 20a, are different from the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the second sensor 20b, the control unit 30 determines that there is a possibility of a sensor malfunction or gas leakage in the multi-stage compressor system 1. The control unit 30 notifies the user of a possibility of some occurring malfunction in the multi-stage compressor system 1 via the notification unit 40.
Thus, the multi-stage compressor system 1 can detect a malfunction in the multi-stage compressor system 1 without making the measuring instrument redundant.
The multi-stage compressor system 1a according to the second embodiment includes a multi-stage compressor 10a and a compressor control device 200a (a control device).
The multi-stage compressor 10a includes first-stage compressor bodies 101 (101a and 101b) arranged in series from an upstream side of a flow of a gas to a downstream side, a second-stage compressor body 103, and a last-stage compressor body 102. The first-stage compressor body 101 is formed of a pair including the first-stage compressor body 101a and the first-stage compressor body 101b.
The first-stage compressor bodies 101 (101a and 101b), the second-stage compressor body 103, and the last-stage compressor body 102 are coupled via a shaft 106. The first-stage compressor bodies 101a and 101b are arranged to form a pair in parallel on the upstream side of the shaft 106. On the downstream side of the shaft 106, the second-stage compressor body 103 and the last-stage compressor body 102 are arranged in parallel. A motor 104 is connected to a middle portion of the shaft 106. Each compressor body and the motor 104 are connected to the shaft 106 via a gearbox 105.
Supply lines 130a and 130b are pipes for supplying gases to the first-stage compressor bodies 101a and 101b. The supply line 130a is connected to an inlet of the first-stage compressor body 101a. Also, the supply line 130b is connected to an inlet of the first-stage compressor body 101b. The first-stage compressor body 101a generates a compressed gas by taking in the gas via the supply line 130a and compressing the gas. The first-stage compressor body 101b generates a compressed gas by taking in the gas via the supply line 130b and compressing the gas.
A first connection line 132 is a pipe for supplying the compressed gas generated by the first-stage compressor bodies 101a and 101b to the second-stage compressor body 103. The first connection line 132 is connected to an outlet of the first-stage compressor body 101a and an outlet of the first-stage compressor body 101b. Also, the first connection line 132 is connected to an inlet of the second-stage compressor body 103. The first connection line 132 includes a merging portion and the compressed gases discharged by the two first-stage compressor bodies 101a and 101b are merged in the merging portion. The first connection line 132 supplies the merged compressed gases to the second-stage compressor body 103.
The second-stage compressor body 103 generates a compressed gas by further compressing the compressed gas taken in via the first connection line 132. A second connection line 133 is a pipe for supplying the compressed gas generated by the second-stage compressor body 103 to the last-stage compressor body 102. The second connection line 133 is connected to an outlet of the second-stage compressor body 103 and an inlet of the last-stage compressor body 102. The second connection line 133 supplies the compressed gas to the last-stage compressor body 102.
The last-stage compressor body 102 generates a compressed gas by further compressing the compressed gas taken in via the second connection line 133. A discharge line 131 is a pipe for supplying the compressed gas generated by the last-stage compressor body 102 to a downstream process. The discharge line 131 is connected to an outlet of the last-stage compressor body 102 and an inlet of the downstream process. The discharge line 131 supplies the compressed gas to the downstream process.
An inlet guide vane (hereinafter, IGV) 107a is provided in the supply line 130a around the inlet of the first-stage compressor body 101a. An IGV 107b is provided in the supply line 130b around the inlet of the first-stage compressor body 101b. The IGV 107a provided in the supply line 130a controls a flow rate of the gas flowing into the first-stage compressor body 101a. The IGV 107b provided in the supply line 130b controls the flow rate of the gas flowing into the first-stage compressor body 101b.
The discharge line 131 around an outlet of the last-stage compressor body 102 is provided with the blowoff valve 108. When the compressor is a compressor in which the gas to be compressed is air, the blowoff valve 108 provided in the discharge line 131 discharges air into the atmosphere via a blowoff line 136. Also, when the gas is nitrogen or the like, a recycle valve can be used. In this case, the blowoff valve 108 can return the gas to the supply line 130a via a recycle line by which the blowoff line 136 is connected to the supply line 130a. Also, the blowoff valve 108 can return the gas to the supply line 130b via the recycle line in which the blowoff line 136 is connected to the supply line 130a.
Because the IGV 107a, the IGV 107b, and the blowoff valve 108 control the outlet pressure of the compressor or avoid surging, its degree of opening is controlled.
An inlet flow rate determination unit 114a is arranged at the supply line 130a. The inlet flow rate determination unit 114a determines the inlet gas flow rate of a gas flowing into the first-stage compressor body 101a and generates an inlet flow rate determination value. An inlet flow rate determination unit 114b is arranged at the supply line 130b. The inlet flow rate determination unit 114b determines an inlet gas flow rate of a gas flowing into the first-stage compressor body 101b and generates an inlet flow rate determination value.
A post-merger pressure determination unit 110 is arranged in the downstream side of the merging portion of the first connection line 132. The post-merger pressure determination unit 110 generates a post-merger pressure determination value by determining a pressure after the merging of the gases flowing out of the first-stage compressor bodies 101a and 101b. A cooler 109a is arranged at the first connection line 132. The cooler 109a cools the gas flowing inside the first connection line 132.
A cooler 109b is arranged at the second connection line 133. The cooler 109b cools the gas flowing inside the second connection line 133.
An outlet pressure determination unit 111 is arranged at the discharge line 131. The outlet pressure determination unit 111 generates an outlet pressure determination value by determining the pressure of the gas flowing out of the last-stage compressor body 102. Also, an outlet flow rate determination unit 115 is arranged at the discharge line 131. The outlet flow rate determination unit 115 generates an outlet flow rate determination value by determining the flow rate of the gas flowing out of the last-stage compressor body 102.
Next, a configuration of the compressor control device 200a in the second embodiment of the present invention will be described.
The compressor control device 200a in the second embodiment of the present invention includes a control unit 30a, a notification unit 40, IGV opening degree control units 50 (50a and 50b), and a blowoff valve opening degree control unit 53.
The IGV opening degree control unit 50a controls a degree of opening of the IGV 107a. The IGV opening degree control unit 50b controls a degree of opening of the IGV 107b. Configurations of the IGV opening degree control unit 50a and the IGV opening degree control unit 50b are identical.
The IGV opening degree control unit 50a includes an IGV opening degree command value generation unit 51 and an IGV opening degree command value correction unit 52a. The IGV opening degree control unit 50b includes an IGV opening degree command value generation unit 51 and an IGV opening degree command value correction unit 52b. The IGV opening degree command value generation unit 51 is common between the IGV opening degree control unit 50a and the IGV opening degree control unit 50b.
The IGV opening degree command value generation unit 51 generates and outputs an IGV opening degree command value indicating a degree of opening of the IGV 107a. The IGV opening degree command value generation unit 51 generates and outputs an IGV opening degree command value indicating a degree of opening of the IGV 107b. The IGV opening degree command value generation unit 51 includes a pressure controller 129 and a function generator 116.
The IGV opening degree command value correction units 52a and 52b correct an IGV opening degree command value output by the IGV opening degree command value generation unit 51.
The IGV opening degree command value correction unit 52a includes a flow rate indicator 125a which outputs an input inlet flow rate determination value as it is, a pressure indicator 126 which outputs an input post-merger pressure determination value as it is, and a function generator 117a which outputs an IGV opening degree correction value.
The IGV opening degree command value correction unit 52b includes a flow rate indicator 125b which outputs an input inlet flow rate determination value as it is, the pressure indicator 126 which outputs an input post-merger pressure determination value as it is, and a function generator 117b which outputs an IGV opening degree correction value.
The pressure indicator 126 is common between the IGV opening degree command value correction units 52a and 52b, but the present invention is not limited thereto.
The blowoff valve opening degree control unit 53 controls a degree of opening of the blowoff valve 108. The blowoff valve opening degree control unit 53 includes upstream-side anti-surge control units 54 (54a and 54b), an outlet pressure control unit 55, a downstream-side anti-surge control unit 56, and a command value selection unit 112.
Here, anti-surge control is control for maintaining a flow rate at a fixed value or more in order to prevent the compressor from being damaged by so-called surging caused by a decrease in the flow rate in the compressor.
The upstream-side anti-surge control unit 54a controls a degree of opening of the blowoff valve 108 in order to prevent surging from occurring in the first-stage compressor body 101a. The upstream-side anti-surge control unit 54b controls a degree of opening of the blowoff valve 108 in order to prevent surging from occurring in the first-stage compressor body 101b. Here, configurations of the upstream-side anti-surge control unit 54a and the upstream-side anti-surge control unit 54b are identical.
The upstream-side anti-surge control unit 54a includes a pressure indicator 126 which outputs an input post-merger outlet pressure determination value as it is, a function generator 118a which outputs an inlet flow rate target value, a flow rate indicator 125a which outputs an input inlet flow rate determination value as it is, and a flow rate controller 127a which outputs a blowoff valve opening degree command value on the basis of an inlet flow rate target value. The upstream-side anti-surge control unit 54b includes the pressure indicator 126 which outputs an input post-merger outlet pressure determination value as it is, a function generator 118b which outputs an inlet flow rate target value, a flow rate indicator 125b which outputs an input inlet flow rate determination value as it is, and a flow rate controller 127b which outputs a blowoff valve opening degree command value on the basis of an inlet flow rate target value.
Also, although the pressure indicator 126 is common between the upstream-side anti-surge control unit 54a and the upstream-side anti-surge control unit 54b, the present invention is not limited thereto.
The outlet pressure control unit 55 includes a pressure controller 129 which outputs an operation value for setting the input outlet pressure determination value to a setting value and a function generator 119 which outputs a blowoff valve opening degree command value.
The downstream-side anti-surge control unit 56 includes a function generator 120 which outputs an outlet flow rate target value and a flow rate controller 128 which outputs a blowoff valve opening degree command value on the basis of the outlet flow rate target value.
Also, the IGV opening degree command value correction unit 52a includes a performance difference correction coefficient generation unit 124, an inlet flow rate target value generation unit 122, and a function generator 121a. The IGV opening degree command value correction unit 52b includes the performance difference correction coefficient generation unit 124, the inlet flow rate target value generation unit 122, and a function generator 121b.
The performance difference correction coefficient generation unit 124 and the inlet flow rate target value generation unit 122 are common between the IGV opening degree command value correction unit 52a and the IGV opening degree command value correction unit 52b. The performance difference correction coefficient generation unit 124 generates and outputs a performance difference correction coefficient for correcting a performance difference between the two first-stage compressor bodies 101a and 101b. The performance difference correction coefficient and the inlet flow rate determination values in the first-stage compressor bodies 101a and 101b are input to the inlet flow rate target value generation unit 122 and inlet flow rate target values are generated for the first-stage compressor bodies 101a and 101b.
The inlet flow rate target values are input to the corresponding function generators 121a and 121b. The function generator 121a is provided in correspondence with a command value selection unit 113a. The function generator 121b is provided in correspondence with a command value selection unit 113b.
The inlet flow rate target value and the inlet flow rate determination value output from the corresponding flow rate indicator 125a are input to the function generator 121a. The inlet flow rate target value and the inlet flow rate determination value output from the corresponding flow rate indicator 125b are input to the function generator 121b. Function generators 121 (121a and 121b) generate and output IGV opening degree command correction values in proportion to a difference between the inlet flow rate target value and the inlet flow rate determination value. Here the function generators 121 (121a and 121b) may consider the integration of the difference between the inlet flow rate target value and the inlet flow rate determination value and generate and output the IGV opening degree command correction value.
The control unit 30a inputs an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114a from the flow rate indicator 125a, an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114b from the flow rate indicator 125b, and an output flow rate determination value of the outlet flow rate determination unit 115. The control unit 30a determines whether a malfunction is present in the multi-stage compressor system 1a on the basis of the inlet flow rate determination values and the output flow rate determination value.
Next, operations of the control unit 30a and the notification unit 40 provided in the compressor control device 200a according to the second embodiment will be described.
The control unit 30a inputs the inlet flow rate determination value corresponding to the inlet flow rate determination unit 114a from the flow rate indicator 125a, the inlet flow rate determination value corresponding to the inlet flow rate determination unit 114b from the flow rate indicator 125b, and an output flow rate determination value of the outlet flow rate determination unit 115. The control unit 30a designates the inlet flow rate determination value input from the flow rate indicator 125a as FI11. The control unit 30a designates the inlet flow rate determination value input from the flow rate indicator 125b as FI12. The control unit 30a designates the output flow rate determination value input from the outlet flow rate determination unit 115 as FC3. The control unit 30a determines whether an absolute value of (FI11+FI12−FC3) is greater than or equal to a predetermined reference value. This reference value is a value determined in consideration of a flow rate response delay or a gas leakage amount of a normal operation time, a drain flow rate in a compressor intercooler, or the like.
The control unit 30a determines that the multi-stage compressor system 1a is normal when the absolute value of (FI11+FI12−FC3) is less than the predetermined reference value.
Also, when the absolute value of (FI11+FI12−FC3) is greater than or equal to the predetermined reference value, the control unit 30a determines that a malfunction is occurring in the multi-stage compressor system 1a. In this case, the control unit 30a notifies the user that some malfunction is likely occurring in the multi-stage compressor system 1a via the notification unit 40. For example, the notification unit 40 is a display, a speaker, a vibration device, or the like. The notification unit 40 may display “Please confirm whether the measuring device is normal.” or “Gas is likely leaking.” or provide a notification by sound. Also, the notification unit 40 may cause the malfunction of the multi-stage compressor system 1a to be known by vibration.
Also, the control unit 30a may stop flow rate deviation correction when it is determined that a malfunction has likely occurred in the multi-stage compressor system 1a. Also, the control unit 30a may control the blowoff valve 108 to be opened to a fixed degree of opening in order to prevent a surge operation. In addition, the control unit 30a may stop the system.
As described above, in the multi-stage compressor system 1a, the control unit 30a compares the flow rates of gases taken in by the first-stage compressor bodies 101a and 101b, which are measured by the inlet flow rate determination units 114a and 114b (the first sensor), with the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115 (the second sensor). When the flow rates of gases taken in by the first-stage compressor bodies 101, which are measured by the inlet flow rate determination units 114a and 114b, are different from the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115, the control unit 30a determines that there is a possibility of a malfunction of the determination unit or gas leakage in the multi-stage compressor system 1a. The control unit 30a notifies the user of a possibility of some occurring malfunction in the multi-stage compressor system 1a via the notification unit 40.
Thus, the multi-stage compressor system 1a can detect a malfunction in the multi-stage compressor system 1a without making the measuring instrument redundant.
The multi-stage compressor system according to the third embodiment 1b includes a multi-stage compressor 10a and a compressor control device 200b (a control device).
The multi-stage compressor system 1b according to the third embodiment is a system in which inlet pressure determination units 134 (134a and 134b), inlet temperature determination units 135 (135a and 135b), pressure indicators 136a, 136b, and 136c, and temperature indicators 137 (137a, 137b, and 137c), an outlet pressure determination unit 138, an outlet temperature determination unit 139, and a flow rate indicator 140 are added to the multi-stage compressor system 1a according to the second embodiment.
Here, a difference of the multi-stage compressor system 1b according to the third embodiment from the multi-stage compressor system 1a according to the second embodiment will be described.
The inlet pressure determination unit 134a generates an inlet pressure determination value by determining the pressure of the gas flowing into the first-stage compressor body 101a. The pressure indicator 136a outputs an inlet pressure determination value input from the inlet pressure determination unit 134a to the flow rate indicator 125a.
The inlet temperature determination unit 135a generates an inlet temperature determination value by determining the temperature of a gas flowing into the first-stage compressor body 101a. The temperature indicator 137a outputs the inlet temperature determination value input from the inlet temperature determination unit 135a to the flow rate indicator 125a.
The flow rate indicator 125a corrects a flow rate determination value on the basis of the input inlet pressure determination value and the input inlet temperature determination value.
The inlet pressure determination unit 134b generates an inlet pressure determination value by determining the pressure of a gas flowing into the first-stage compressor body 101b. The pressure indicator 136b outputs the inlet pressure determination value input from the inlet pressure determination unit 134b to the flow rate indicator 125b.
The inlet temperature determination unit 135b generates an inlet temperature determination value by determining the temperature of a gas flowing into the first-stage compressor body 101b. The temperature indicator 137b outputs the inlet temperature determination value input from the inlet temperature determination unit 135b to the flow rate indicator 125b.
The flow rate indicator 125b corrects a flow rate determination value on the basis of the input inlet pressure determination value and the input inlet temperature determination value.
The outlet pressure determination unit 138 generates an outlet pressure determination value by determining the pressure of a gas flowing out of the last-stage compressor body 102. The pressure indicator 136c outputs an outlet pressure determination value output from the outlet pressure determination unit 138 to the flow rate indicator 140.
The outlet temperature determination unit 139 generates an outlet temperature determination value by determining the temperature of the gas flowing out of the last-stage compressor body 102. The temperature indicator 137c outputs the outlet temperature determination value output from the outlet temperature determination unit 139 to the flow rate indicator 140.
The flow rate indicator 140 corrects a flow rate determination value on the basis of the input outlet pressure determination value and the input outlet temperature determination value.
The control unit 30b inputs an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114a from the flow rate indicator 125a, an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114b from the flow rate indicator 125b, and an outlet flow rate determination value from the flow rate indicator 140. The control unit 30b designates the inlet flow rate determination value input from the flow rate indicator 125a as FI11c. The control unit 30b designates the inlet flow rate determination value input from the flow rate indicator 125b as FI12c. The control unit 30b designates the output flow rate determination value input from the flow rate indicator 140 as FC3c. The control unit 30b determines whether an absolute value of (FI11c+FI12c−FC3c) is greater than or equal to a predetermined reference value. This reference value is a value determined in consideration of a flow rate response delay or a gas leakage amount of a normal operation time, a drain flow rate in a compressor intercooler, or the like.
The control unit 30b determines that the multi-stage compressor system 1b is normal when the absolute value of (FI11c+FI12c−FC3c) is less than the predetermined reference value.
Also, when the absolute value of (FI11c+FI12c−FC3c) is greater than or equal to the predetermined reference value, the control unit 30b determines that a malfunction is occurring in the multi-stage compressor system 1b. In this case, the control unit 30b notifies the user that some malfunction is likely occurring in the multi-stage compressor system 1b via the notification unit 40. For example, the notification unit 40 is a display, a speaker, a vibration device, or the like. The notification unit 40 may display “Please confirm whether the measuring device is normal.” or “Gas is likely leaking.” or provide a notification by sound. Also, the notification unit 40 may cause the malfunction of the multi-stage compressor system 1b to be known by vibration.
Also, the control unit 30b may stop flow rate deviation correction when it is determined that a malfunction is likely occurring in the multi-stage compressor system 1b. Also, the control unit 30b may control the blowoff valve 108 to be opened to a fixed degree of opening in order to prevent a surge operation. In addition, the control unit 30b may stop the system.
As described above, in the multi-stage compressor system 1b, the control unit 30b compares the flow rates of gases taken in by the first-stage compressor bodies 101a and 101b, which are measured by the inlet flow rate determination units 114a and 114b (the first sensor), with the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115 (the second sensor). When the flow rates of gases taken in by the first-stage compressor bodies 101, which are measured by the inlet flow rate determination units 114a and 114b, are different from the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115, the control unit 30b determines that there is a possibility of a malfunction of the determination unit or gas leakage in the multi-stage compressor system 1b. The control unit 30b notifies the user of a possibility of some occurring malfunction in the multi-stage compressor system 1b via the notification unit 40.
Thus, the multi-stage compressor system 1b can detect a malfunction in the multi-stage compressor system 1b without making the measuring instrument redundant.
Also, as described above, in the multi-stage compressor system 1b, the control unit 30b determines that there is a possibility of a malfunction of the determination unit or gas leakage in the multi-stage compressor system 1b using a corrected gas flow rate on the basis of a measurement value of a pressure or a temperature in addition to the control unit 30a in the multi-stage compressor system 1a.
Thereby, the control unit 30b can make a more accurate determination.
Also, when the pressure and temperature are measured as in the above-described example, it is desirable to measure a pressure upstream and measure a temperature downstream. This is because the turbulence of a gas flow due to the temperature measurement instrument is likely to affect measurement of the pressure when the temperature measurement instrument is located upstream and a pressure is measured downstream.
Also, although a flow rate is corrected on the basis of results of measuring a pressure and a temperature in the above-described example, the present invention is not limited thereto. A molecular weight of a gas may be measured and the flow rate may be corrected on the basis of the molecular weight. Thereby, it is possible to perform correction considering an influence by a gas other than the air and the control unit 30b can make a more accurate determination.
The multi-stage compressor system 1c according to the fourth embodiment includes a multi-stage compressor 10a and a compressor control device 200c.
The multi-stage compressor system 1c according to the fourth embodiment is a system in which drain flow rate meters 141 (141a and 141b) and drain valves 142 (142a and 142b) are added to the multi-stage compressor system 1a according to the second embodiment.
Here, a difference of the multi-stage compressor system 1c according to the fourth embodiment from the multi-stage compressor system 1a according to the second embodiment will be described.
The drain flow rates during cooling by the coolers 109a and 109b are measured from the drain flow rate meters 141 (141a and 141b) or the flow rate is estimated on the basis of degrees of opening of the drain valves 142 (142a and 142b).
For example, correspondence relationships between drain flow rates and degrees of opening of the valves are pre-acquired by experiments and the like and recorded in a storage unit. The drain flow rate is estimated on the basis of the correspondence relationships.
The control unit 30c inputs an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114a from the flow rate indicator 125a, an inlet flow rate determination value corresponding to the inlet flow rate determination unit 114b from the flow rate indicator 125b, and an outlet flow rate determination value of the outlet flow rate determination unit 115. The control unit 30c designates the inlet flow rate determination value input from the flow rate indicator 125a as FI11. The control unit 30c designates the inlet flow rate determination value input from the flow rate indicator 125b as FI12. The control unit 30c designates the output flow rate determination value input from the outlet flow rate determination unit 115 as FC3. The control unit 30c designates a drain flow rate sum input from the drain flow rate meter 141 or the drain valve 142 as ΣFL. The control unit 30c determines whether an absolute value of (FI11+FI12−FC3−ΣFL) is greater than or equal to a predetermined reference value. This reference value is a value determined in consideration of a flow rate response delay or a gas leakage amount of a normal operation time.
The control unit 30c determines that the multi-stage compressor system 1c is normal when the absolute value of (FI11+FI12−FC3−ΣFL) is less than the predetermined reference value.
Also, when the absolute value of (FI11+FI12−FC3−ΣFL) is greater than or equal to the predetermined reference value, the control unit 30c determines that a malfunction is occurring in the multi-stage compressor system 1c. In this case, the control unit 30c notifies the user that some malfunction is likely occurring in the multi-stage compressor system 1c via the notification unit 40. For example, the notification unit 40 is a display, a speaker, a vibration device, or the like. The notification unit 40 may display “Please confirm whether the measuring device is normal.” or “Gas is likely leaking.” or provide a notification by sound. Also, the notification unit 40 may cause the malfunction of the multi-stage compressor system 1c to be known by vibration.
Also, the control unit 30c may stop flow rate deviation correction when it is determined that a malfunction is likely occurring in the multi-stage compressor system 1c. Also, the control unit 30c may control the blowoff valve 108 to be opened to a fixed degree of opening in order to prevent a surge operation. In addition, the control unit 30c may stop the system.
Also, the drain flow rate may be estimated from relationships between input gas conditions (a temperature, a pressure, a humidity, etc.) and operation conditions (a temperature and a pressure).
As described above, in the multi-stage compressor system 1c, the control unit 30c compares the flow rates of gases taken in by the first-stage compressor bodies 101a and 101b, which are measured by the inlet flow rate determination units 114a and 114b (the first sensor), with the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115 (the second sensor). When the flow rates of gases taken in by the first-stage compressor bodies 101, which are measured by the inlet flow rate determination units 114a and 114b, are different from the flow rate of a gas discharged by the last-stage compressor body 102, which is measured by the outlet flow rate determination unit 115, the control unit 30c determines that there is a possibility of a malfunction of the determination unit or gas leakage in the multi-stage compressor system 1c. The control unit 30c notifies the user of a possibility of some occurring malfunction in the multi-stage compressor system 1c via the notification unit 40.
Thereby, the multi-stage compressor system 1c can detect a malfunction in the multi-stage compressor system 1c without making the measuring instrument redundant.
Also, when the pressure and temperature are measured as in the above-described example, it is desirable to measure a pressure upstream and measure a temperature downstream. This is because the turbulence of a gas flow due to the temperature measurement instrument is likely to affect measurement of the pressure when the temperature measurement instrument is located upstream and a pressure is measured downstream.
Also, although a flow rate is corrected on the basis of results of measuring a pressure and a temperature in the above-described example, the present invention is not limited thereto. A molecular weight of a gas may be measured and the flow rate may be corrected on the basis of the molecular weight. Thereby, it is possible to perform correction considering an influence by a gas other than the air and the control unit 30c can make a more accurate determination.
Also, as described above, in the multi-stage compressor system 1c, the control unit 30c determines that there is a possibility of a malfunction of the determination unit or gas leakage in the multi-stage compressor system 1c using a drain flow rate in addition to the control unit 30a in the multi-stage compressor system 1a.
Thereby, the control unit 30c can make a more accurate determination.
Also, although an example shown in the above-described embodiment is an example in which the gas flow rate of the last-stage compressor body 102 is measured, the present invention is not limited thereto. The control unit may compare measurement values in compressor bodies of arbitrary different stages. In this case, the possibility of a malfunction of a measuring instrument used in measurement and the possibility of gas leakage between compressor bodies of two different stages are determined.
Also, an embodiment of the present invention has been described, but the above-described multi-stage compressor system 1 internally includes a computer system. Each process described above may be stored in a computer-readable recording medium in the form of a program. The above-described process is performed by the computer reading and executing the program. Here, the computer-readable recording medium may be a magnetic disk, a magneto-optical disc, a compact disc read-only memory (CD-ROM), a digital versatile disc-read only memory (DVD-ROM), a semiconductor memory, or the like. In addition, the computer program may be distributed to the computer through a communication line, and the computer receiving the distributed program may execute the program.
Also, the above-described program may be a program for implementing some of the above-described functions. Further, the above-described program may be a program, i.e., a so-called differential file (differential program), capable of implementing the above-described function in combination with a program already recorded on the computer system.
Although some embodiments of the present invention have been described, these embodiments have been proposed as examples and are not intended to limit the range of the invention. These embodiments can be executed in various other modes. Various omissions, replacements, and changes can be made in a range not departing from the scope of the invention.
According to the multi-stage compression system, the control device, the malfunction determination method, and the program described above, it is possible to detect a malfunction in a multi-stage compressor system without making a measuring instrument redundant.
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| PCT/JP2015/067896 | 6/22/2015 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2016/002565 | 1/7/2016 | WO | A |
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