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[0001] This application is a division of application Ser. No. 09/455,475, filed Dec. 6, 1999, which is hereby incorporated herein by reference.
[0002] The invention relates generally to an apparatus and method for controlling the operation of a centrifugal chiller refrigeration system. More particularly, the chiller control system of the present invention operates a centrifugal chiller which possesses both a magnetic bearing centrifugal compressor and an adjustable speed motor drive. Additionally, the present invention discloses the necessary components and control logic for use with the chiller control system.
[0003] A centrifugal chiller typically consists of the following components: one or more evaporators, compressors, condensers and expansion devices. In a chiller, the compressor acts as a vapor pump, where raising the pressure of the refrigerant from the evaporating pressure to the condensing pressure provides an active means of absorbing heat from a lower temperature environment and rejecting that heat to a higher temperature environment. As an active machine, the chiller requires an apparatus to control its operation.
[0004] In general terms, a centrifugal compressor for a chiller typically consists of the following components: inlet guide vanes, one or more impellers within a housing surrounded by one or more diffusers with collectors driven by some mechanical shaft means, such as for example, an electric motor. The mechanical shaft means is supported by one or more bearings of the rolling element, journal, or magnetic bearing type which accommodate both radial and axial loads. In variable speed electric chillers, the centrifugal compressor is supplied with electrical power through an adjustable speed motor drive which alters the frequency and/or voltage of the power to the motor to modulate the speed of the compressor.
[0005] The chiller control system for a centrifugal chiller typically performs one or more of the following functions: adjust inlet guide vane position and/or compressor speed to match the cooling capacity with the cooling load, monitor chiller operating conditions for unsafe operation and take appropriate action when encountered, display chiller operating conditions for user interpretation, and/or operate the chiller in response to a predefined schedule.
[0006] Chiller control systems of the microprocessor type typically consist of one or more of the following devices, a microprocessor which runs a control algorithm, sensors which acquire operating data from one or more points on the chiller, display devices for communicating information on chiller operating conditions and various devices for the input of information to the chiller control system. While these chiller control systems have performed adequately for centrifugal chillers consisting of compressors with rolling element bearings and/or journal bearings, they are inadequate for chillers with magnetic bearing centrifugal compressors.
[0007] Rolling element bearings are generally passive devices and, during normal operation, operate without the requirement of active control. The chiller control system does not typically provide active control of the rolling element bearings where, in this context, active implies continual adjustment of some bearing feature. Chiller control systems for centrifugal chillers which use rolling element bearings in the compressor may monitor the bearing temperature, at periodic intervals, as an indication of whether the machine is operating properly. An elevated temperature is used as an indication of a potential mechanical problem with the bearings. If the measured bearing temperature exceeds a predefined setpoint, the chiller control system may be programmed to stop the machine and alert the user.
[0008] In magnetic bearing centrifugal compressors, the compressor rotor is suspended on a magnetic field generated in the magnetic bearings. For definitional purposes, “magnetic bearings” are electromagnetic devices used for suspending a rotating body in a magnetic field without mechanical contact. The bearings can be further classified as active, indicating that some type of active control system is necessary to ensure stable levitation of the rotating body.
[0009] Distinct from other compressor types, a magnetic bearing centrifugal compressor uses magnetic bearings as the primary means for supporting the rotor structure. There is a clearance gap between the rotating and stationary components of the bearing that is measurable and controllable. For the magnetic bearings to operate properly, electrical power and proper operation of the magnetic bearing control electronics are required.
[0010] As described previously, existing chiller control systems for centrifugal chillers do not work adequately for centrifugal chillers with active magnetic bearing centrifugal compressors. The necessary control strategies are not provided by the controllers known in the art.
[0011] Specifically, these chiller control systems do not monitor the magnetic bearings for stable levitation which is required in order to prevent damage to the magnetic bearing centrifugal compressor. Existing chiller control systems may allow the compressor to turn at high speeds while the magnetic bearings are not stably levitated. When this occurs, the rotor does not spin about a fixed axis. Rather, the rotor spins on an axis contained within a small cylinder defined by the clearances between the compressor rotor assembly and the stationary compressor housing. The unconfined rotation of the compressor rotor assembly may generate large forces (due to the kinetic energy stored in the rotor at high speeds), and may thereby damage the magnetic bearings, the compressor rotor assembly, and compressor impeller, as well as the attached stationary compressor housing. In the event of a loss of active control of the compressor rotor, the rotor may contact the auxiliary bearings within the compressor.
[0012] Due to the disadvantages associated with chiller control systems known in the prior art for centrifugal chillers which have magnetic bearing centrifugal compressors, it should therefore be appreciated that there is a need for a chiller control system for a magnetic bearing centrifugal chiller.
[0013] In view of the foregoing, it is an object of the present invention to provide a chiller control system apparatus and method for controlling a centrifugal chiller which possesses a magnetic bearing centrifugal compressor and an adjustable frequency motor drive.
[0014] The function of a chiller control system is to operate a centrifugal chiller in such a manner as to meet the cooling load requirements. The chiller control system continuously monitors the cooling load and other chiller variables, and adjusts the operation of the chiller to match the cooling load. In sophisticated chiller control systems, in addition to matching cooling load, the control system seeks to operate the compressor in a manner that maximizes operating efficiency to reduce overall electrical power consumption.
[0015] While maximizing overall centrifugal chiller operating efficiency, the chiller control system must operate the magnetic bearing centrifugal compressor safely by avoiding compressor surge. Surge occurs when there are sudden reversals in the direction of fluid flow through the compressor impeller as the pressure difference across the impeller becomes too large. (Since additional static pressure rise occurs in the compressor diffuser as the fluid is decelerated, the pressure near the diffuser entrance may exceed the pressure at the impeller exit.)
[0016] When the impeller exit pressure drops below diffuser pressure, the fluid flow direction reverses and flows back into the compressor impeller, resulting in significantly increased stresses and a substantially increased vibration of the compressor rotor. The flow reversal causes the pressure at the impeller exit and within the diffuser to drop. When the pressure drops below the surge point, the flow again reverses direction and flows into the diffuser. A compressor operates in a surging condition when these sudden flow reversals are occurring. The flow reversals during surge damage the chiller equipment.
[0017] Prior experimental studies have shown that the maximum operating efficiency of a centrifugal compressor is close to the surge boundary. To minimize energy consumption, the impeller should not impart more energy to the fluid than necessary to meet the temperature lift requirements for the vapor compression refrigeration cycle. Any additional energy imparted to the refrigerant flow above the required amount is wasted. Maximum efficiency occurs near the surge boundary. Hence, to maximize the efficiency of a centrifugal chiller, the compressor should be operated at the lowest speed possible that is just great enough to avoid a surge condition. The location of the surge point is a function of the aerodynamic design of the centrifugal compressor.
[0018] During centrifugal compressor development, detailed measurements of the pressure rise versus flow rate behavior of the compressor at various operating speeds, inlet guide vane angle settings and diffuser vane angle settings are typically conducted. These measurements determine a surge line for the compressor, a plot of the points (flow coefficient, head coefficient) on the compressor operating map (where the non-dimensional head coefficient lies along the y-axis and the non-dimensional flow coefficient lies along the x-axis) where the surge condition is encountered. The compressor avoids a surging condition when its current operating state (defined by the calculated flow coefficient and head coefficient) lies below and to the right of the surge line on the compressor operating map. The operating envelope for the compressor is the complete set of points (flow coefficient, head coefficient) for which some combination of inlet guide vane angle, diffuser vane angle, and compressor speed will allow operation in a non-surge condition. This operating map for the compressor can be stored in the memory of the control system as a set of equations which define the surge line or as a set of points which form an array of stable operating states.
[0019] A surge condition can be detected by the chiller control system by changes in chiller performance. When the compressor is surging, the torque on the rotor oscillates (from positive to negative) which causes noticeable changes in the electrical current supplied to the motor element.
[0020] A surge condition can also be detected by the chiller control system by changes in the magnetic bearing operating conditions. When the compressor is surging, the rotor oscillates which causes noticeable changes in bearing position, stabilizing current, force and temperature.
[0021] The compressor head coefficient-flow coefficient operating map determines the safe operating condition (flow coefficient, head coefficient) for a particular cooling load and pressure lift requirement. The compressor head-flow operating map can be adjusted or modified, should changes occur over time in either the impeller surface finish, the diffuser vane condition or the impeller to shroud clearance.
[0022] The typical chiller control system adjusts the compressor speed, inlet guide vane position, and diffuser vane position to meet the pressure ratio requirements and the cooling load requirements while operating as efficiently as possible. Prior experimental research studies have shown that a coordinated adjustment of the inlet guide vanes and diffuser vanes can increase the operating efficiency of a centrifugal compressor impeller from 2 to 6 percent. Wallman et al., “Improvements in Performance Characteristics of Single-Stage and Multistage Centrifugal Compressors by Simultaneous Adjustments of Inlet Guide Vanes and Diffuser Vanes.” Transactions of the ASME Journal of Turbomachinery, January 1987, Vol. 109, pgs. 41-47.
[0023] It is an object of the present invention to provide a chiller control system for centrifugal chillers which possess magnetic bearing centrifugal compressors.
[0024] It is another object of the present invention to provide a chiller control system for centrifugal chillers which possess adjustable speed motor drives.
[0025] It is yet another object of the present invention to prevent operation of the chiller in the event of a problem with the magnetic bearings, thereby preventing damage to the chiller compressor(s).
[0026] It is another object of the present invention to prevent operation of the magnetic bearings in the event of a problem with the centrifugal chiller electrical power supply, thereby prolonging magnetic bearing operating life.
[0027] Another object of the present invention is to provide a measurement of the electrical power consumption of the centrifugal chiller during operation, thereby eliminating the need for an external electrical power measurement device.
[0028] It is even another object of the present invention to provide a measurement of the centrifugal compressor operating speed.
[0029] It is yet another object of the present invention to provide a method of storing centrifugal chiller operating data over long periods of time to allow the assembly of energy usage studies.
[0030] It is still a further object of the present invention to provide an improved user interface for displaying operational parameters of the centrifugal chiller.
[0031] Yet another object of the present invention is to provide a chiller control system algorithm which controls the operation of inlet guide vane position, diffuser vane position, magnetic bearing position, and motor speed in order to maximize the chiller operating efficiency.
[0032] It is another object of the present invention to provide a method for measuring bearing forces, vibrations and imbalances in order to indicate the machine's condition, and predict problems and schedule maintenance.
[0033] These and other objectives and advantages are achieved by the chiller control system apparatus and method according to the invention. A centrifugal chiller, for which the preferred embodiment of the invention is applicable, consists of an evaporator, a magnetic bearing centrifugal compressor, a condenser, and an expansion device. The magnetic bearing centrifugal compressor increases the pressure of the refrigerant vapor from the saturation pressure of the refrigerant in the evaporator to the saturation pressure of the refrigerant in the condenser. A typical embodiment of the magnetic bearing centrifugal compressor, such as that described in co-pending patent application Ser. No. 08/908,035, filed Aug. 11, 1997, the specification of which is herein expressly incorporated by reference, contains a compressor rotor supported on both sides of the electric motor element by radial magnetic bearings of the type well known to those skilled in the art. Axial magnetic bearings located outside of each radial magnetic bearing absorb thrust loads. A microprocessor magnetic bearing control unit (MBU) provides active control of the magnetic bearings to maintain the compressor rotor in a stable levitated position at all operating speeds. The magnetic bearing centrifugal compressor is driven by an electric motor whose speed is controlled by a microprocessor adjustable speed motor drive (ASD).
[0034] In a preferred embodiment, the chiller control system apparatus consists of a microprocessor chiller controller (CC), an adjustable speed motor drive (ASD), and a magnetic bearing control unit (MB). The chiller controller (CC) acquires, processes, records and analyzes operating data from the centrifugal chiller sensors. The chiller controller (CC) possesses both analog and digital input and output capabilities for data acquisition and control. Additionally, the chiller controller (CC) uses a touchscreen display for data input and output communication. The chiller controller (CC) runs a chiller control system algorithm (described later) that processes input sensor data and sends control signals to various other components of the chiller control system described herein.
[0035] The chiller controller (CC) communicates with the magnetic bearing control unit (MBU) through digital input and output signal lines and serial communications links. Through these lines, the CC provides commands to levitate and delevitate the magnetic bearings, monitors the operating status of the magnetic bearings, reads any alarm or warning conditions and accesses diagnostic and tuning functions. The chiller controller (CC) communicates with the adjustable speed motor drive (ASD) through both digital and analog input and output signals lines. Through these lines, the CC provides commands to stop and start the centrifugal chiller, signals the desired motor speed, monitors operating data, reads any alarm and/or warning conditions and accesses other control functions. It is through the analog input signal line of the ASD that the CC communicates the desired compressor operating speed to the ASD. The ASD then uses its internal microprocessor and PID algorithm to match actual compressor speed to the desired setpoint speed.
[0036] As critical components of the chiller control system, the MBU and the ASD are connected by pairs of incoming and outgoing signal lines. Through these lines, alarm and/or warning conditions are communicated instantly whenever they occur to the other component, thus allowing the microprocessor of the other component to take the appropriate action.
[0037] The CC actuates the inlet guide vanes through inlet guide vane position and feedback signals. The CC actuates the diffuser vanes through diffuser vane position and feedback signals. The position of the inlet guide vanes, the diffuser vanes, and the compressor operating speed are coordinated by a complex chiller control system algorithm that responds to input data from a variety of sensor signals which monitor operating conditions within the chiller. The chiller control system algorithm provides all monitoring, controlling and communicating functions.
[0038] The chiller control system algorithm according to the invention serves to operate the centrifugal compressor at the lowest speed possible with the inlet guide vanes and the diffuser vanes adjusted at an angle to maximize efficiency. Here, the chiller control system algorithm contains several loops that adjust the three main control parameters (inlet guide vane position, diffuser vane position, and compressor speed).
[0039] Other objects, advantages and novel features of the present invention will become apparent from the following detailed description of the invention when considered in conjunction with the accompanying drawings, wherein:
[0040]
[0041]
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[0044]
[0045]
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[0050]
[0051]
[0052] A schematic diagram of the chiller control system apparatus is shown in
[0053] The chiller control system requires input data from several sources on which it makes judgements about its performance. Here, the chiller control system monitors the data at regularly scheduled intervals. Cooling load requirements are determined from the measured inlet and outlet water temperatures and the calculated water flow rate (based on the measured pressure drop within the evaporator heat exchanger). The compressor head rise is calculated from measured pressures at the inlet and exit of the compressor. Because of the computational capabilities of the control system, with knowledge of the refrigerant equations of state, the thermodynamic properties of the refrigerant can be calculated. From measurements of the temperatures and pressures at the inlet and exit of the compressor, the complete thermodynamic properties of the refrigerant, including enthalpy, entropy, and specific volume can be determined.
[0054] The compressor capacity for this control system is estimated from measurements of the water flow rate and measurements of the inlet and outlet chilled water temperatures in the evaporator. The flow rate through the evaporator is determined from measurements of the differential water pressure taken in the inlet and outlet chilled water lines. The measured pressure drop is correlated with the flow rate through the evaporator in its original clean condition. A curve showing the flow rate versus measured pressure drop for the evaporator is stored in the control system memory. The cooling capacity is calculated from the water flow rate, water specific heat, and the measured temperature difference from the inlet to the outlet of the evaporator.
[0055] The magnetic bearing control unit, MBU
[0056] The adjustable speed motor drive, ASD
[0057] The chiller controller, the microprocessor computer CC
[0058] The chiller control system apparatus contains signal conditioning electronics for the sensors. The signal conditioning electronics provide instrument grade power for the various sensors located throughout the centrifugal chiller. The signal conditioning electronics convert the high voltage signals from the magnetic bearing control unit (MBU)
[0059] Subroutines for determination of the refrigerant enthalpy, entropy, and specific volume as a function of measured pressure and temperature allow calculation of the isentropic efficiency of the compression process. The total real electrical power consumption is measured by the ASD
[0060] Control systems, known in the prior art, typically use liquid crystal display LCD screens to display operating parameters and use keypads to input and output information. The control system apparatus of the present invention uses a touchscreen display, of the type known in the art, as the interface between the user and the chiller control system. A touchscreen display presents true graphics capabilities which allows the presentation of a larger quantity of information to the user than the that which is capable of being presented with smaller displays. The additional information simplifies the user's task of assessing chiller operating conditions. Both text based and graphics based information can be displayed simultaneously.
[0061] The chiller control system algorithm software has been configured to be menu and button driven, thereby preventing inadvertent changes to the chiller operating status by pressing the wrong panel switches.
[0062] Using a hard disk drive storage device, of the type well known in the art, provides the CC
[0063] The chiller controller CC
[0064] The speed of the electric motor is controlled by an ASD
[0065] The ASD
[0066] The ASD
[0067] The ASD varies the voltage and/or frequency of the outgoing electrical power to maintain the electric motor at a desired operating speed under load conditions or to track a desired acceleration/deceleration curve. The ASD microprocessor controller uses an internal PID algorithm with user programmable parameters to match the actual electric motor speed with a desired electric motor speed reference signal. Feedback of the actual motor speed to the ASD controller comes from a speed sensor which is mounted in the electric motor. The chiller controller determines the desired compressor speed for the centrifugal chiller based on the particular thermal conditions encountered during operation. The chiller controller communicates the desired compressor speed to the controller through an analog output signal line.
[0068] The ASD microprocessor controller records the supply voltage and line current, calculates real power and total energy consumption, calculates actual compressor speed from the feedback signal, monitors the total operating hours and records other important operating statistics during operation. The information is updated and stored in the available controller memory at regular intervals. The chiller controller retrieves the information through the RS-485 serial communications link and uses it to estimate the chiller kW/ton efficiency. The communications protocol to retrieve the information is programmed into the chiller control system algorithm.
[0069] Operation of the ASD controller and its response to input signals is directed through several groups of parameters stored in memory. These parameters can be accessed either locally at the ASD control panel, or remotely through the RS-485 serial communications link. For this application, the ASD control panel is disabled so that the preprogrammed parameters cannot be changed. The preprogrammed parameters are set for use with the chiller control system algorithm. For servicing and diagnostic purposes, the CC
[0070] The CC
[0071] The magnetic bearing control unit MBU
[0072] The magnetic bearing control unit
[0073] The CC
[0074] During the levitation sequence, digital outputs of the MBU
[0075] The LCOMP output indicates that the levitation sequence has been started. The CC
[0076]
[0077] The ENABLE/QSTOP D
[0078] The START/STOP line D
[0079] The READY/REMOTE line
[0080] The microprocessor chiller controller runs a computer algorithm that performs the sequence of actions necessary to start and stop the chiller, monitor the current operating condition, record operating data and run a graphical user interface to display conditions to the user. A software program contains the graphical user interface (GUI) which communicates with the user and allows the user to monitor operating data when the chiller is running. Its algorithm acquires the operating data, checks for alarms and warnings, calculates the chiller cooling capacity, determines the parameters for position of the inlet guide vanes to match measured capacity with desired capacity and updates the operating history log. The program provides PID control of the compressor speed, inlet guide vane angle, and diffuser vane angle.
[0081] Shown in
[0082] The operating state variables define the current operating state of the centrifugal compressor from measured temperatures, pressures and/or flow rates within the chiller. These variables include the non-dimensional pressure coefficient (PC) defined for a centrifugal compressor as,
[0083] and a non-dimensional efficiency coefficient (EC) which represents the isentropic efficiency defined for a centrifugal compressor as
[0084] The operating state variables include a surge subroutine, denoted by S( ), that calculates a surge pressure coefficient (PCs) and a surge flow coefficient (FCs) that lie on the surge line at points near the actual current operating pressure coefficient (PC) and flow coefficient (FC). These non-dimensional coefficients are compared to a compressor operating map, a plot of pressure coefficient versus flow coefficient behavior (described earlier) generated from experimental test data. The surge line on the compressor operating map is represented by a best fit equation.
[0085] For the chiller control system apparatus according to the invention, the oscillations in the electrical current are used to indicate surge. By periodically sampling the electrical current, a standard deviation of the sampled measurements can be determined quickly. When the standard deviation exceeds a predetermined value, the compressor is understood to be operating in a surge condition. The larger the standard deviation of the sampled data, the larger the variation of the electrical current around some mean value.
[0086] The plant variables define the desired, actual and acceptable operating conditions for the chiller. The centrifugal chiller control system works to maintain the measured chiller leaving evaporator water temperature (LWTm) within a small temperature band (LWTb) centered around a preprogrammed setpoint temperature (LWTs) which is dependent on the requirements of the attached the building air conditioning system or process cooling system. The leaving water temperature error (LWTe) is the difference between the measured leaving water temperature and the leaving water temperature setpoint. The changes in building or process cooling load are reflected in changes in the chiller entering evaporator water temperature. When the entering evaporator water temperature increases (increased cooling load), the chiller must increase its cooling capacity in order to cool the incoming water to the desired leaving evaporator water temperature. Conversely, when the entering evaporator water temperature decreases (decreased cooling load), the chiller must decrease its cooling capacity in order to avoid cooling the incoming water below the desired leaving evaporator water temperature. The control system always works to maintain the measured leaving water temperature (LWTm) in the error band (LWTb) around the leaving water temperature setpoint (LWTs).
[0087] The chiller control system algorithm may work to minimize either the calculated isentropic efficiency of the compression process or the measured real mechanical efficiency (kW/ton) of the compressor. The chiller control system adjusts the control variables in order to match the output with the plant variable. The iteration counters are used to keep track of the number of iterations through various subroutines within the chiller control system. These iteration counters act as built in delays, allowing the chiller to reach a steady state condition before additional adjustments are made in order to bring the plant variables to the desired point. The speed adjustment background counter (BN) is used to determine the number of iterations through various subroutine components before an attempt to reduce speed to improve operating efficiency is attempted. The diffuser adjustment background counter is used to determine the number of iterations through various subroutine components before an attempt to change diffuser vane angle to improve operating efficiency is attempted.
[0088] The operating flags indicate current conditions within the chiller control system based on decisions made by the chiller control system algorithm. The RANGE flag indicates whether the measured leaving water temperature is within the desired error band around the leaving water temperature setpoint. The RUN flag indicates whether the chiller compressors are running. The ALARM flag indicates whether an alarm condition was encountered in any part of the chiller system including the chiller sensors, the magnetic bearing control unit, or the adjustable speed motor drive. The SURGE flag indicates that a compressor surge condition was encountered. The detection of surge may be determined from standard deviations of the measured electrical currents in the motor windings, or from monitoring bearing conditions. The speed reduction flag (NoNDEC) is used to signal that no other reductions in compressor speed are allowed in order for the chiller to reach steady state condition and to prevent surge. The IDAD and NAD mode flags are used to indicate the subroutines to provide primary control to the centrifugal chiller.
[0089] The miscellaneous variables (for example, gain factors) are used to approximately relate the changes in one control variable with an equivalent change in another critical control variable. The IGV/N gain factor (GIGV-N) converts an adjustment of in let guide vane position to an equivalent adjustment of the compressor speed. The IGV/DIF gain factor (GIGV-DIF) converts an adjustment of inlet guide vane position into an equivalent adjustment of the diffuser vane position.
[0090]
[0091] In step
[0092] If the chiller is running and within range the chiller remains on. If the chiller is running and the leaving water temperature error, measured in step
[0093] The chiller control system levitates the magnetic bearings and accelerates the compressor speed to the design speed (N
[0094] On the first iteration through the main chiller control system loop, the angle adjustment flag (IDAD) is initialized to true in step
[0095] In general terms, capacity control for the chiller is accomplished by varying the compressor speed, inlet guide vane position, and diffuser vane position simultaneously. In step
[0096] In step
[0097] Following the estimate of the inlet guide vane adjustment made by the PID controller in step
[0098] In the angle adjustment mode (IDAD) subroutine, a flowchart of which is shown in
[0099] In step
[0100] In step
[0101] In step
[0102] In step
[0103] In step
[0104] If the leaving water temperature range counter exceeds 20 and the speed reduction flag has been set to false, then the chiller control system reduces the compressor speed by approximately 2% in step
[0105] If the leaving evaporator water temperature is within range, RANGE has been set to true, the chiller control system assesses the current state of the speed reduction flag in step
[0106] If the speed reduction flag has been set to true, the chiller control system checks the current state of the diffuser vane adjustment background counter in step
[0107] The compressor speed adjustment background counter determines the frequency of attempts by the chiller control system to reduce compressor speed without causing a compressor surge or without allowing the measured leaving evaporator water temperature to leave the desired leaving evaporator water temperature range. Typically the adjustments in compressor speed occur on a less frequent basis than adjustments in diffuser vane angle and inlet guide vane angle.
[0108] On exit of the IDAD mode subroutine at step
[0109] In the NAD mode subroutine, execution starts at step
[0110] In step
[0111] In step
[0112] In step
[0113] In step
[0114] In step
[0115] In step
[0116] The NAD mode subroutine transfers control back to the main chiller control system loop in step
[0117] After achieving steady state, successive attempts are made to increase efficiency by reducing the compressor speed and hence reducing motor power consumption. The optimum operating point occurs where the speed has been reduced to the minimum speed that will produce the required pressure difference across the impeller for a given cooling load. Reduction of speed below this point will cause unsteady surge conditions that must be avoided. Real dynamic surge conditions and a surge boundary curve may be plotted on a non-dimensional compressor map of pressure coefficient versus flow coefficient. If the surge boundary curve is sufficiently distant from the real surge conditions, the compressor may be safely operated at points outside the boundary curve. A surge condition is detected by measuring the standard deviation of the motor current. If the controller detects surge conditions, the speed is immediately increased by a set increment.
[0118] Upon completion of a chiller startup routine, the compressor is initialized to run at maximum speed and maximum inlet guide vane opening. Similarly, upon completion of a high lift heat pump startup routine, the compressor is initialized to run at maximum speed and maximum inlet guide vane opening for the particular operating temperature lift. The main controller measures chiller system parameters, calculates the deviation of the leaving water temperature about a user-defined setpoint, calculates a non-dimensional pressure coefficient error based on the enthalpy difference across the compressor, impeller diameter and compressor speed. Additionally, the main controller predicts a new inlet guide vane position using a PID algorithm and directs the capacity control mode as either inlet guide vane (IGV) mode or speed (N) mode. The initial operating mode is set to IGV control. FIGS.
[0119] IGV mode operation updates the inlet guide vane position to reduce the deviation of the LWT from the setpoint below a predetermined criterion, thereby achieving steady state. While maintaining a steady state through inlet guide vane control, successive attempts are made to increase efficiency by reducing the compressor's speed. The decrease in speed is proportional to the difference between the pressure coefficient of the operating point and the surge boundary condition pressure coefficient at the operating point flow coefficient. A reduction in compressor speed must be offset by an increase in the inlet guide vane opening. The compressor speed will not be reduced under steady state conditions if any of the following occur: the inlet guide vanes are greater than 70% fully opened, a surge condition recently occurred, or the compressor is operating near the surge boundary curve so that a further reduction of the compressor's speed could send it into a surge condition. Transfer from IDAD mode to N mode can only occur if, based on the difference between the LWT and setpoint, the PID algorithm requests that the inlet guide vanes be fully open for a predetermined number of consecutive algorithm loops.
[0120] NAD mode operation initially increases the speed of the compressor to match the increase in the cooling load detected by a change in LWT. Subsequent speed reductions may also occur. All speed changes in this mode are proportional to the change in the inlet guide vane position requested by the PID controller.
[0121] Transfer from NAD mode to IDAD mode will occur if: a surge condition is detected, the speed is modulated below 50% of the maximum compressor speed, or the compressor speed is modulated below 98% of the maximum speed following conditions where the chiller could not meet the cooling load demands.
[0122] The magnetic bearing centrifugal compressor, because it uses an ASD to control motor speed, has the advantage of using a second control method to meet the aggregate cooling load that across the line started centrifugal compressors do not. When the temperature lift and flow rate requirements for meeting the cooling load are such that, even with both inlet guide vanes and a variable geometry diffuser the compressor cannot avoid operating in a surge condition, a second control strategy can be employed.
[0123] In this control strategy, the compressor is cycled, using a variable duty cycle that is determined by the compressor control system, between two different operating points that do not lie within the surge operating condition. The manner of operation is very similar to the operation of home air conditioners which cycle on and off to maintain the room temperature within a fixed temperature deadband around a preset temperature point.
[0124] Essentially, when the temperature rises above the upper limit of the temperature deadband around the desired leaving water temperature, the compressor operates in the high speed condition where the cooling capacity exceeds that required to meet the instantaneous cooling load. As a result, the leaving water temperature begins to drop and continues to drop until it reaches the lower limit of the temperature deadband around the desired leaving water temperature setpoint. At this point, the compressor speed is reduced to the low speed condition where the cooling capacity drops nearly to zero. In this condition, the condensing temperature of the refrigerant drops below the temperature of the external thermal control system. Only the sensible portion of the heat that is above the temperature of the external thermal control system can be rejected.
[0125] FIGS.
[0126] The existence of a MBU
[0127] The foregoing disclosure has been set forth merely to illustrate the invention and is not intended to be limiting. Since modifications of the disclosed embodiments incorporating the spirit and substance of the invention may occur to persons skilled in the art, the invention should be construed to include everything within the scope of the appended claims and equivalents thereof.