By Thomas A. Hughes
ISBN-10: 0876640145
ISBN-13: 9780876640142
ISBN-10: 1680155539
ISBN-13: 9781680155532
ISBN-10: 1891891901
ISBN-13: 9781891891908
ISBN-10: 2212212232
ISBN-13: 9782212212235
Excellent for lecture room use or self-study, this newly up to date best-selling booklet has supplied millions of scholars, technicians, engineers, and revenues individuals with a realistic advent to the foundations, applied sciences, and methods utilized in commercial strategy regulate. This 5th version takes an identical confirmed strategy of past versions. every one bankruptcy starts off with uncomplicated definitions and ideas that let readers to develop into good versed within the rules essential to under-stand the variables that impact approach regulate structures. New positive factors within the 5th version contain more advantageous assurance of technique keep an eye on pcs and commercial networks and a brand new bankruptcy on liquid density dimension. Sections have been additionally further on human laptop interface (HMI), instant units and networks. The ebook contains recommendations to routines that make it superior for self-study
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Extra info for Measurement and Control Basics, Fifth Edition
Example text
The PID controller is used on processes that respond slowly and have long periods. Temperature control is a common example of PID control because the heat rate may have to change rapidly when the temperature measurement begins to change. The derivative action shortens the response of the slow process to an upset. In the next chapter we discuss such important characteristics of processes as time constants and dead time. By understanding these concepts you will be better able to select the proper control action type for effective control.
If a control loop is using PI control, the possibility exists with the integral (reset) mode that the controller will continue to integrate and change the output even outside the operating range of the controller. ” For example, the heat exchanger shown in Figure 1-17 can be designed and built to heat 50 gal/min of process fluid from 70°F to 140°F. If the process flow should suddenly increase to 100 gal/min, it may be impossible to supply sufficient steam to maintain the process fluid temperature at140°F even when the control valve is wide open (100%), as shown in Figure 1-18.
Sensor output changes smoothly from the moment a change in measurement value occurs, even if the disturbance is sudden and discontinuous. It is interesting to note that the nature of the sensor time-response curve is the same for virtually all sensors, even though the sensors measure different physical variables. A typical response curve for a process sensor is shown in Figure 2-4, where the input has been changed suddenly at time equal to zero. Sensor Output (m) mf mi Time (t) t=0 Change Figure 2-4.
Measurement and Control Basics, Fifth Edition by Thomas A. Hughes
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