u = u₀ + Kp · e
A P controller responds immediately and proportionally: doubling the control error doubles the output change.
A P controller responds immediately and proportionally: doubling the control error doubles the output change.
Select a target and calculate.
A P controller responds immediately and proportionally: doubling the control error doubles the output change.
Kp=2, e=6 and u₀=20 give u=32. With an actuator range of 0 to 100, this value is not yet saturated.
Ideal continuous P controller without output saturation, deadband, sampling or actuator dynamics; all signals must use consistent scaling.
Calculate a proportional controller output from controller gain, instantaneous control error and bias.
A P controller responds immediately and proportionally: doubling the control error doubles the output change. This calculator represents a clearly bounded technical relationship between the displayed quantities. The definition helps put inputs into the same reference state before interpreting the result.
u = u₀ + Kp · e
| Symbol / input | Meaning |
|---|---|
| Controller output u | Value sent by the controller to the actuator, such as a normalised valve opening or drive command. |
| Controller gain Kp | Controller-output change per unit of error. Kp comes from controller design or cautious tuning; an excessive value promotes oscillation. |
| Control error e | Instantaneous setpoint minus measured value on the same scale. Its sign sets controller action; verify it on the real process. |
| Bias u₀ | Controller output that holds the desired operating point at e=0. Obtain it from steady plant operation; use 0 if no bias is required. |
Controller output u: Value sent by the controller to the actuator, such as a normalised valve opening or drive command. Controller gain Kp: Controller-output change per unit of error. Kp comes from controller design or cautious tuning; an excessive value promotes oscillation. Control error e: Instantaneous setpoint minus measured value on the same scale. Its sign sets controller action; verify it on the real process. Bias u₀: Controller output that holds the desired operating point at e=0. Obtain it from steady plant operation; use 0 if no bias is required.
Select the target quantity, enter the other known values with units, then check the result against the worked example and model limits.
Kp=2, e=6 and u₀=20 give u=32. With an actuator range of 0 to 100, this value is not yet saturated.
A P controller responds immediately and proportionally: doubling the control error doubles the output change. Read the result as a model value for the selected operating point and check units, sign, order of magnitude and application boundary conditions.
Use the displayed units and convert afterwards. Prefixes such as k-, m- and µ- are common sources of mistakes.
P controller: output from control error: Such basic calculations support plausibility checks, early component selection and preparation of a complete verification.
Ideal continuous P controller without output saturation, deadband, sampling or actuator dynamics; all signals must use consistent scaling.
Common mistake: A formally correct result can still be unsuitable when load case, reference state or units do not match the application.
Compare unit and order of magnitude with a second calculation and vary inputs one at a time.
No. The calculator exposes a model; real boundary conditions require separate review.
Only when the calculator converts within the same physical quantity type.