Monday 18 December 2017

CASCADE CONTROL

Cascade Control 
Cascade control is a multiple loop control configuration, like the override control which involves more than one measurement and one manipulation. In the cascade configuration, there are two control loops to manipulate one process variable.
The outer loop that measures the controlled variable is the major one and its controller uses the set point given by the operator. The outer loop is also called as primary or master loop. The inner loop measures an intermediate process variable (usually a major disturbance) and uses the output of primary controller as its set point. The inner loop can also be known as secondary or slave loop. The secondary loop helps in the effective control of primary process variable.
Block Diagram of Cascade control
Block Diagram of Cascade control
How cascade control makes the difference?
Feedback Control (Left) and Cascade Control (Right) of Process Fluid Outlet Temperature
Consider a temperature control problem in a furnace. The furnace is used to heat the process fluid stream and the outlet temperature of fluid stream is to be controlled. In feedback control, the outlet temperature is measured and the flow rate of fuel gas is adjusted accordingly. The fuel gas flow rate keeps the outlet temperature at desired value. The fuel gas flow rate gets affected directly by any disturbances in fuel gas header pressure or control valve problems like hysteresis.
The disturbances can be nullified by cascading the temperature controller to a flow controller (fuel gas inlet). The temperature control is the primary control and its controller output is the set point for flow controller. The flow control will be the secondary control and corrects the disturbances that affect the fuel gas flow rate before it affects the outlet temperature.

Key rules for cascade control
  1. The cascade control has an advantage of disturbance rejection. The secondary controller corrects the variations occurring in secondary variable before it affects the primary variable.
  2. The secondary loop response must be at least three times faster than that of primary loop.
  3. Secondary variable has to be chosen in such a way that the process dynamics (time lags) are split equally. If most of the process dynamics comes under secondary loop, then the addition of cascade control leads to the instability of primary loop.
  4. The most common secondary variables are valve position control, flow control and temperature control (in chemical reactions).
  5. The common mode of secondary control is proportional controller. The proportional and integral control mode is also used at times. Integral control is said to slow down the secondary loop response. Moreover, in cascade control we have primary controller to eliminate the offset of proportional controller. Derivative action is not used in secondary control.
  6. In the process of tuning, the secondary loop is first tuned and then the primary loop.
Example for Cascade control
Speed control of a DC motor
Cascade control in speed control of a DC motor
Cascade control in speed control of a DC motor

The speed control of the DC motor is done controlling the armature voltage by a thyristor unit. The thyristor adjusts the armature voltage which gets reflected upon armature current and speed of DC motor. The armature current is the secondary variable because it has lots of chances to go high and low during start-up, shut down and loading the DC motor. To limit the maximum and minimum value of current, saturation is applied to the current set point. The secondary control loop takes care of these changes and helps in primary controller to control speed.

2 comments:

  1. Very good and useful blog.it's a request ,please post more blogs regarding instrumnentation and control

    ReplyDelete
  2. Thank you. Sure i would post more. Keep following.

    ReplyDelete

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