In Figure A, a traditional controller is shown measuring the temperature inside the tank and manipulating the steam valve opening to add more or less heat as inflowing water disturbs the tank . Learn how cascade control works to improve quality and performance in temperature control applications. For example: changing cooling water flow rate to . The output function can be configured for ? The primary loop controls the main .
The secondary controller , FC, measures .
The choice of which to use depends on the disturbances that affect the effluent temperature.
If the main disturbance is variations in the steam supply pressure, due possibly to variable steam demands of other process units, then controlling the steam flow with the. Thus, the secondary flow control loop is essentially the manipulated variable for the primary temperature controller. The net feedback effect is the same. The use of cascade control offers considerable performance improvements in . The extra layer of control does not degrade the response to xd1′, because the process is usually much slower than the controller.
The Single Loop Jacketed Stirred Reactor As shown in the process graphic below (click for large view), the reactor exit stream temperature is controlled by adjusting the . The benefit of using the cascade configuration is that any disturbances within the inner (fast) loop, can be corrected (by PID2), without waiting for it to show up in the temperature loop (PID1), so that better (tighter and faster) temperature control can be achieved.
Cascade can be carried to more nested levels. Integral action in Master is to be. Inhibited when OP limit reached in Slave. Batch Reactor Temperature Control . Description of the simulated systems.
This paper examines how difficult control tasks are enhanced by introducing secondary measurements, creating control cascades.
Temperature is much used as secondary measurement because of cheap implementation and quick and accurate response. This makes the primary temperature control linear with respect to . Furnace temperature is primarily regulated by the gas flow control. The furnace control system has larger capacity lags and suite for cascade PID control.
However, traditional parameters tuning method of controller can only meet either of the target tracking and disturbance rejection.
In this paper, using off-line PID parameter . Abstract: In the centralized heating, ventilating and air-conditioning (HVAC) system, air handling units (AHU) are traditionally controlled by single loop proportional-integral-derivative (PID) controllers. The control structure is simple, but the performance is usually not satisfactory. The root causes are nonlinearity in the jacket loop from selecting inappropriate control valves and excessive dead zones in the split range. If the heaters get to hot, the liquid will degrade.
This vat uses three zones of heaters supplying heat energy to one main zone of the process, the vat.
Temperature sensor location for cascade control schemes in tubular reactors is still an open research problem. Several studies have pointed out that most temperature sensitive zones along the length of the reactor are suitable to this end. VRC 6Boiler Management Control.
This weather-compensating flow temperature control offers timed programs to manage heating and hot water systems.
No comments:
Post a Comment
Note: only a member of this blog may post a comment.