... direct-synthesis controllers The basic idea is to specify the desired response of the system to a particular type of disturbance and then, knowing the model of the process, back-calculate the controller ... PI controller Use r/ values of 0.5 and minutes 15.3 Make Nyquist plots for the processof Problem 15.1 and find the value of gain that gives the following specifications: l l l Gain margin of ... Calculate the controller gain that gives a closedloop damping coefficient of 0.3 CIJA~~EK IS: Stability Analysis of Sampled-Data Systems 537 15.8 A process controlled by a proportional digital controller...
... continuous analog control Computer control offers a number of advantages that outweigh its theoretical dynamic disadvantages: cost; ease of configuring and tuning control loops; ease of maintenance; ... It is defined below A sequence of impulses z.$, comes out of the impulse sampler on the input of the process Each of these impulses produces a response from the .process Consider the kth impulse ... of powers of z-t, the coefficients in front of all the terms give the values of fCllr,,, The infinite series is obtained by merely dividing the numerator of F,,, by the denominator of Fczj Z(c)...
... grounded in the essence of chemical processcontrol will be capable of understanding the features of model predictive control should the need arise The basic idea of MPC is to use a process model (either ... number of zeros and the number of poles of Fts, in the right half of the s plane If the process is openloop stable, none of the transfer functions in &ts, has any poles in the right half of the ... we can tune each controller independently As we will soon see, the dynamics and stability of this multivariable closedloop process depend on the settings of all controllers Controller structures...
... RESPONSE OF FEEDBACK CONTROLLERS Before we give some examples of the design of feedback controllers in the frequency domain, it would be wise to show what the common P, PI, and PID controllers ... 11.13 Bode plots of controllers 11.3.1 Proportional Controller (P) The transfer function of a P controller is G cCs) = KC Substituting s = iw gives Gc(iw) = Kc (11.37) A proportional controller merely ... Proportional-Integral Controller (PI) The transfer function of a PI controller is ~‘IIAIWK I I: F;requency-I>otllaitl Analysis of Closedloop Systems G(i,,) = Kc 397 (11.38) The Bode plot of this combination of...
... important property of complex numbers The magnitude of the product of two complex numbers is the product of their magnitudes The argument of the product of two complex numbers is the sum of their arguments ... the size of the reactor increases The flow rate of cooling water also increases rapidly as reactor size increases The ratio of K,,, to Kmi”, which is a measure of the controllability of the system, ... used a model of the process to calculate the controller settings, but the structure of the model has not been explicitly involved in the controller design There are several alternative controller...
... (N - M) of 1, and the asymptotes go off at 180” Example 8.7 shows that the asymptotes go off at 60” since the order of the system is third * B Use of hIATLAB software The commercial software ... by a factor of over the firepower of the Klingon vessels, which all have the same firepower The firepower of the rest of Kirk’s fleet is on a par with that of the Klingons But these officers have ... advantages of Laplace transforms The techniques involve finding the transfer function of the openloop process, specifying the desired performance of the closedloop system (process plus controller),...
... controllability factor can be some measure of the “goodness” ofcontrol (integral of the squared error), the cost of the control effort, or the value of some controllability measure (such as the plant ... steady-state effects of recycles 6.2 EFFECT OF RECYCLE ON TIME CONSTANTS One of the most important effects of recycle is to slow down the response ,of the process, i.e., increase the process time constant ... The annual profit for each plant is calculated by taking the value of the onspecification products and subtracting the cost of reprocessing off-specification material, the cost of raw materials,...
... performance of a control system These structures include ratio control, cascade control, and override control 4.1 RATIO CONTROL As the name implies, ratio control involves keeping constant the ratio of ... type of nonlinear control can bc achieved by using nonlinear transformations of the controlled variables For example, in chemical reactor control the rate of reaction can be controlled instead of ... of adaptive control strategies in processcontrol 4.6 VALVE POSITION (OPTIMIZING) CONTROL Shinskey [Chem Erg Prog 72(5):73, 1976; Chem Eng Prog 74(5):43, 19781 proposed the use of a type of control...
... briefly at some of the control hardware that is currently used in processcontrol systems: transmitters, control valves, controllers, etc Then we discuss the performance of conventional controllers ... Analog and Digital Controllers The part of the control loop with which we spend most of our time in this book is the controller The job of the controller is to compare the process signal from ... controversial subjects in processcontrol The sizing ofcontrol valves is a good example of the engineering trade-off that must be made in designing a plant Consider the process sketched in Fig...
... Levels ofProcessControl 1.4.1 ProcessControl Laws / 1.4.2 Languages qf ProcessControl / 1.4.3 Levels ofProcessControl 1.5 Conclusion P A R T 20 22 24 I Time Domain Dynamics and Control ... knowledge not only of these traditional areas but also of the fundamentalsofprocesscontrol For those of us who have been part of this period of development, the attainment of parity with the ... LANGUAGES, AND LEVELS OFPROCESSCONTROL 1.4.1 ProcessControl Laws Several fundamental laws have been developed in the processcontrol field as a result of many years of experience Some of these may...
... technique, the statistical design of the controlcharts and the TBE controlcharts Chapter reviews the current research trend of TBE controlcharts and the multivariate controlcharts technique In Chapter ... traditional controlcharts have encountered a lot of difficulties In order to overcome difficulties of conventional controlcharts in detecting process shifts in high-quality processes, a new kind ofcontrol ... effective controlcharts for multivariate TBE data and study the optimal statistical design issue of the proposed controlcharts Chapters provides an introduction of the principle of the control charts...
... Flow diagram of proposed framework 111 Figure 6.9: ACF ofprocess variable (y) in example 123 Figure 6.10: BI ofprocess variable (y) in example 124 Figure 6.11: Surrogate data plot ofprocess variable ... ends of gas concentration section Today, the operation of the FCC unit has become advanced, encompassing the use of automatic process controllers to control the key variables This is because control ... plants and (9) Mineral Processing etc However, regardless of the application, the purpose ofprocesscontrol is still the same and its objective is to ensure that the process is kept within certain...
... 14.4 Implementation ofControl Loops 14.4.1 ON/OFF action pneumatic controller 14.4.2 ON/OFF action electrical controller 14.4.3 PID action pneumatic controller 14.4.4 PID action control circuits ... 1.2 ProcessControl In order to produce a product with consistently high quality, tight processcontrol is necessary A simple-to-understand example ofprocesscontrol would be the supply of water ... understanding of instrumentation and processcontrol Instrumentation and processcontrol involve a wide range of technologies and sciences, and they are used in an unprecedented number of applications...
... the fabrication Supervisory Control Run-by-Run Control Real-Time Control Run-by-Run Control Real-Time Control Run-by-Run Control Real-Time ControlProcess A Process B Process C wafer movement wafer ... topics are the subject of Chapters and 10 These topics include run-by-run controlof unit processes and supervisory controlofprocess sequences, as well as the diagnosis ofprocess and equipment ... and utilization of information occurs at another level of abstraction, which consists of various control loops Finally, the organization of the process belongs to yet another level of abstraction,...
... Page of Tuning of a PID controller using Ziegler-Nichols Method LAB Objective: 1) To demonstrate the use of PID controller using LabVIEW 2) Finding the values of KP and TI and TD ... there are several PID controller modules We shall use the Academic PID controller The difference between different PID controllers is shown below: Page of Program: Page of Page of Conclusion: 1) ... and described in this note The PID controller encapsulates three of the most important controller structures in a single package The parallel form of a PID controller has transfer function: (...
... 61285 (1994) Industrial -process control Safety of analyzer houses 61297 (1995) Industrial -process control systems Classification of adaptive controllers for the purpose of evaluation 61298-1 ... pneumatic signal for processcontrol systems Expression of performance of air quality infra-red analyzers 60534: Industrial -process control valves 60534-1 (1987) Part 1: Control valve terminology ... industrial -process measurement and control equipment in oxygen service Industrial -process measurement and control Terms and definitions Binary direct voltage signals for process measurement and control...
... IEC:2000 –5– INDUSTRIAL -PROCESS CONTROL VALVES – Part 6-2: Mounting details for attachment of positioners to control valves – Positioner mounting on rotary actuators Scope This part of IEC 60534 is intended ... INTERNATIONAL ELECTROTECHNICAL COMMISSION –––––––––––– INDUSTRIAL -PROCESS CONTROL VALVES – Part 6-2: Mounting details for attachment of positioners to control valves – Positioner mounting on rotary actuators ... to be in conformity with one of its standards 6) Attention is drawn to the possibility that some of the elements of this International Standard may be the subject of patent rights The IEC shall...
... actual quantity & type of yarn twist have to be maintain ProcessControlof Sizing Section Output Variable of Sizing Output Quantity Required Quantity ProcessControl Count of sized yarn 10 To maintain ... algorithm (sequence of finite instruction ) for controlling the output of a specific production process Quality is formed during production process So, if a production process is not controlled, the ... reduced by controlling the yarn tension during sizing ProcessControlof Drawing-in & trying Section Output Variable of Drawing in & trying Output Quantity Required Quantity ProcessControl Cross...
... actual quantity & type of yarn twist have to be maintain ProcessControlof Sizing Section Output Variable of Sizing Output Quantity Required Quantity ProcessControl Count of sized yarn 10 To maintain ... sized yarn Density of sized beam ( yarn / inch ) 73 75 Density of sized beam can be maintained by controlling the ProcessControlof Drawing-in & trying Section Output Variable of Drawing in & trying ... achieved PROCESSCONTROLProcesscontrol is performed by six steps : Step-1: Draw process flow chart showing real change in products geometry Step-2 : Segregate or highlight the part of the flow...
... components of all control systems are Sensor/transmitter Also often called the primary and secondary elements Controller The “brain” of the control system Final control element Often a control valve ... 1-6 1-7 A ProcessControl System Important Terms and the Objective of Automatic ProcessControl Regulatory and Servo Control Transmission Signals, Control Systems, and Other Terms Control Strategies ... Sampled-Data Controllers 329 7-2.5 Summary of Controller Tuning 330 Tuning Controllers for Integrating Processes 331 7-3.1 Model of Liquid Level Control System 331 7-3.2 Proportional Level Controller...