FEBRUARY 2010 – UNDERSTANDING DERIVATIVE IN PID CONTROL
The third factor in PID is the least understood. Derivative action can do good things, but when used improperly, it causes headaches. You’ve probably heard the expression, “a little knowledge
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The third factor in PID is the least understood. Derivative action can do good things, but when used improperly, it causes headaches. You’ve probably heard the expression, “a little knowledge
Temperature control applications can be broken into two main categories—fully continuous and semi-continuous (or batch). An example of a fully continuous temperature controller is a shell-and-tube heat exchanger. In this
Ask technicians and engineers about manually tuning PIDs. Their responses usually fall into one of the three different groups: 1) Some who will say it’s a “dark art” and won’t
Let’s say you take your car in for an oil change. The oil you select is rated for traveling a distance of 5,000 miles. In all likelihood the
New Feature Speeds Implementations and Aligns Solution with Six Sigma March 31, 2011 – Control Station announced enhancement of its PlantESP Performance Monitoring Solution with the introduction of an innovative
November 3, 2010 – Control Station, the leader in PID control loop tuning and process control technologies, announced today that its PlantESP – an innovative PID controller performance monitoring and
Innovative Technology Simplifies Isolation, Optimization of Regulatory Controllers November 2, 2010 – Control Station, the leader in PID control loop tuning and process control technologies, today announced the launch of
Finding controller performance issues in a typical production facility is not hard, but isolating and correcting their root-cause can present real challenges. Ask around stories abound of production staff who