Add documentation in rst for PID

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Mario Hüttel 2021-07-15 00:21:14 +02:00
parent 8a9bd0df6e
commit 0bf587b8bb

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@ -26,6 +26,48 @@ reflow oven's solid state relais output is saturated by software to a limit of 0
In addition to the above features, the derivate term contains an additional first order low pass filter in order to prevent coupling of high frequency noise amplified by the derivate term. In addition to the above features, the derivate term contains an additional first order low pass filter in order to prevent coupling of high frequency noise amplified by the derivate term.
The low pass filter is charcterized by its time constant :math:`k_{d\tau}`. The low pass filter is charcterized by its time constant :math:`k_{d\tau}`.
Time Continuous Transfer Function
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
The time continous transfer function of the PID controller is
.. math:: H_c(s) = \frac{Y_c(s)}{X_c(s)} = k_p + \frac{k_i}{s} + \frac{k_ds}{1+sk_{d\tau}}
Time Discrete Transfer Function
~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~
The time descrete transfer function which is implemented in the code is derived by converting the time continuous transfer function
with the bilinear transformation:
.. math:: s = \frac{2}{T_s}\cdot \frac{z-1}{z+1}
The frequency warping of the bilinear transform can be considered negligible because the PID controller is targetted for low frequency temperature signal data with a maximum far below the nyquist freqency.
In this area, the mapping of the continuous frequencies to the time descrete can be considered linear.
The time discrete transfer function after inserting the bilinear transform is:
.. math:: H_d(z) = H_c(s)\bigg|_{s=\frac{2}{T_s}\cdot \frac{z-1}{z+1}} = k_p + \frac{k_i T_s (z+1)}{2(z-1)} + \frac{\frac{2}{T_s}k_d(z-1)}{\left(1+\frac{2k_{d\tau}}{T_s}\right)z+\left(1-\frac{2k_{d\tau}}{T_s}\right)}.
Converted to an implementable form:
.. math:: H_d(z) = k_p + \frac{k_iT_s(1+ z^{-1})}{2(1-z^{-1})} + \frac{\frac{2}{T_s}k_d(1-z^{-1})}{(1+2k_{d\tau}T_s^{-1})+(1-2k_{d\tau}T_s^{-1})z^{-1}}
This function can be splitted in the three individual parts of the PID controller:
.. math:: H_{d1}(z) = k_p
.. math:: H_{d2}(z) = \frac{k_iT_s(1+ z^{-1})}{2(1-z^{-1})}
.. math:: H_{d3}(z) = \frac{\frac{2}{T_s}k_d(1-z^{-1})}{(1+2k_{d\tau}T_s^{-1})+(1-2k_{d\tau}T_s^{-1})z^{-1}}
The individual time domain difference equations :math:`y_i[n] = \mathcal{Z}^{-1}\left\lbrace H_{di} * X(z)\right\rbrace` that are implemented in software are:
.. math:: y_1[n] = k_p x[n]
.. math:: y_2[n] = \underbrace{\frac{k_iT_s}{2}}_{k_{i_t}} \left( x[n] + x[n-1]\right) + y_2[n-1]
.. math:: y_3[n] = \underbrace{\frac{2k_{d}}{2k_{d\tau} + T_s}}_{k_{d_t}}\left( x[n] - x[n-1] \right) + \underbrace{\frac{2k_{d\tau} - T_s}{2k_{d\tau} + T_s}}_{\overline{k_{d_t}}} y_3[n-1]
The final output value is the sum of all three terms:
.. math:: y[n] = \sum_{i=1}^{3} y_i[n]
.. _pid_code_api: .. _pid_code_api: