By William Y. Svrcek, Donald P. Mahoney, Brent R. Young
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Additional resources for A Real-Time Approach to Process Control, 3rd Edition
Square root extractors for obstruction-type meters 6. Quantity or total flowmeters, such as (a) Positive displacement (b) Sliding vane (c) Bellows type (d) Nutating disc (e) Rotating piston (f) Turbine type 7. Magnetic flowmeters 8. Vortex meters 9. Mass flowmeters, such as (a) Coriolis effect flowmeters (b) Thermal dispersion flowmeters Selection of a flowmeter is based on obtaining the optimum measuring accuracy at the minimum price. It should be noted that flowmeters may use up a substantial amount of energy, especially when used in low pressure vapour service.
S. P. (1994) Improve distillation column control design. CEP, March, 75–83. F. (1991) An industrial perspective on dynamic flowsheet simulation, in Proceedings of CPCIV (eds Y. H. Ray), AIChE, New York, pp. 181– 208. D. (1992) Object-oriented simulation, Chapter 5, in Practical Distillation Control (ed. L. Luyben), Van Nostrand Reinhold. L. (2002) Plantwide Dynamic Simulators in Chemical Processing and Control, Marcel Dekker, Inc. 2 Process Control Hardware Fundamentals In order to analyse a control system, the individual components that make up the system must be understood.
Sonic methods 5. Radar methods 6. Nuclear methods 7. Weight methods 22 A Real-Time Approach to Process Control It is extremely important that vessels are well protected from an overflow condition. An overflowing vessel may have severe safety consequences, impacting nearby employees, the environment and the surrounding community. Some vessels require low-level protection to operate safely. Ideally, each vessel should have a visual indication for the operator, an alarm point and a transmitted level indicator .
A Real-Time Approach to Process Control, 3rd Edition by William Y. Svrcek, Donald P. Mahoney, Brent R. Young