Two Networked Watertank Systems

Two water tanks are connected by pipes, where water flows from one tank to another (adpated from [1]). The water level $x_i$ of tank $i = 0,1$ is controlled by its pump. There are two pump modes: $\textsf{On}$ and $\textsf{Off}$. Each pump changes its mode according to the water level of its tank and the other water tank. The continuous dynamics of $x_i$ is defined as follows: \begin{equation*} \dot{x}_i = \begin{cases} q_i + a \sqrt{2g} (\sqrt{x_{i - 1}} - \sqrt{x_i}) & \textsf{(On)} \\
a \sqrt{2g} (\sqrt{x_{i - 1}} - \sqrt{x_i}) & \textsf{(Off)} \end{cases}
\label{water} \end{equation*} where $a$ and $q_i$ depend on the width of the pipe and the pump’s power, and $g$ is the standard gravity constant. Figure [1] shows a hybrid automaton $H_1$ of one water tank (the other component is similar).

model

Figure 1: A hybrid automaton of one water tank controller $H_1$

For simplicity, we consider the following dynamics to obtain linear flow conditions.

\begin{equation*} \dot{x}_0 = \begin{cases} 0.9 & \textsf{(On)}\\
-0.8 & \textsf{(Off)} \end{cases}
%% \quad\quad\quad %% \dot{x}_1 = \begin{cases} 1 & \textsf{(On)}\\
-0.6 & \textsf{(Off)} \end{cases}
\end{equation*}

Table [1] shows the STL properties.

Label STL formula Description
$\textsf{f1}$ $\square_{[1,3]} ((x_0 \leq 7) \mathbf{R}_{[1,10]} (x_1 \leq 3))$ For time interval $[1,3]$, $x_1$ is less than or equal to $3$, until $x_0$ is less than or equal to $7$ for time interval $[1,10]$.
$\textsf{f2}$ $(\lozenge_{[1,10]} (x_1 < 5.5)) \mathbf{U}_{[2,5]} (x_0 \geq 5)$ Within time interval $[1, 10]$, $x_1$ is less than $5.5$, until $x_0$ is greater than or equal to $5$ in time interval $[2, 5]$.
$\textsf{f3}$ $(\lozenge_{[4,10]} (x_0 \geq 4 \rightarrow \square_{[2, 5]} x_1 \leq 2)$ For some time point in interval $[4, 10]$, if $x_0$ is greater than or equal to $4$ then $x_1$ is always less than or equal to $2$ during time interval $[2,5]$.

Table 1: STL properties for watertank


An STLmc Input Model

We use the STLmc language to describe the watertank model (water.model) as follows:

bool a;     bool b;
[0, 10] x1; [0, 10] x2;
{ mode: a = false; b = false;
  inv:  x1 >= 1; x2 >= 1;
  flow: d/dt[x1] = -0.8;
        d/dt[x2] = -0.6;
  jump: x1 <= 2 => (and a' (not b') 
                        (x1' = x1) (x2' = x2));
        x2 <= 3 => (and (not a') b' 
                        (x1' = x1) (x2' = x2));
        x1 <= 2 => (and a' b' (x1' = x1) 
                        (x2' = x2));
        x2 <= 3 => (and a' b' (x1' = x1) 
                        (x2' = x2));
}
{ mode: a = false; b = true;
  inv:  x1 >= 1; x2 <= 9;
  flow: d/dt[x1] = -0.8;
        d/dt[x2] = 1;
  jump: x2 >= 6 => (and (not a') (not b') 
                        (x1' = x1) (x2' = x2));
        x1 <= 2 => (and a' b' (x1' = x1) 
                        (x2' = x2));
        x2 >= 6 => (and a' (not b') 
                        (x1' = x1) (x2' = x2));
        x1 <= 2 => (and a' (not b') 
                        (x1' = x1) (x2' = x2));
}
{ mode: a = true; b = false;
  inv:  x1 <= 8; x2 >= 1;
  flow: d/dt[x1] = 0.9;
        d/dt[x2] = -0.6;
  jump: x1 >= 5 => (and (not a') (not b') 
                        (x1' = x1) (x2' = x2));
        x2 <= 3 => (and a' b' (x1' = x1) 
                        (x2' = x2));
        x1 >= 5 => (and (not a') (b') (x1' = x1) 
                        (x2' = x2));
        x2 <= 3 => (and (not a') b' (x1' = x1) 
                        (x2' = x2));
}
{ mode: a = true; b = true;
  inv:  x1 <= 9; x2 <= 9;
  flow: d/dt[x1] = 0.9;
        d/dt[x2] = 1;
  jump: x1 >= 5 => (and (not a') b' (x1' = x1) 
                        (x2' = x2));
        x2 >= 6 => (and a' (not b') (x1' = x1) 
                        (x2' = x2));
        x1 >= 5 => (and (not a') (not b') (x1' = x1) 
                        (x2' = x2));
        x2 >= 6 => (and (not a') (not b') (x1' = x1) 
                        (x2' = x2));
}

init: not(a); 4.4 <= x1; x1 <= 4.5; 
      not(b); 5.9 <= x2; x2 <= 6;

proposition:

# bound: 20, timebound: 20, solver: yices
goal:
  [f1]: [][1, 3]((x1 <= 7) R[1, 10] (x2 <= 3));  # threshold: 2.5
  [f2]: (<>[1, 10) x2 < 5.5) U[2, 5] (x1 >= 5);  # threshold: 0.1
  [f3]: <>[4, 10] (x1 >= 4 -> [][2, 5] x2 <= 2); # threshold: 0.01

Run

For the input model, we use a time bound $\tau = 20$ and a discrete bound $N = 20$ as input parameters. Because the model has linear dynamics, we use $\textsf{yices}$ for an underlying solver with the default algorithm $\textsf{1-step}$. For the formulas $\textsf{f1}$, $\textsf{f2}$, and $\textsf{f3}$, we choose thresholds $\epsilon_1 = 2.5$, $\epsilon_2 = 0.1$, and $\epsilon_3 = 0.01$, respectively.

The formulas $\textsf{f1}$ and $\textsf{f3}$ are safe, while the following command found a counterexample of the STL formula $\textsf{f2}: (\lozenge_{[1,10)} (x_1 < 5.5)) \mathbf{U}_{[2,5]} (x_0 \geq 5)$ at bound $4$ with respect to $\epsilon_2=0.1$ in $5$ seconds using yices.

./stlmc ./water.model -bound 20 -time-bound 20 -threshold 0.1 \
        -goal f2 -solver yices -visualize
Label $\epsilon$ $| \Psi |$ Time Result $k$ Alg.
$\textsf{f1}$ $2.5$ $18.8$ $26.2$ $\top$ - $\textsf{1-step}$
$\textsf{f2}$ $0.1$ $1.9$ $4.22$ $\bot$ $4$ $\textsf{1-step}$
$\textsf{f3}$ $0.01$ $11.2$ $20.2$ $\top$ - $\textsf{1-step}$

Table 2: Verification results of the STL properties for watertank


Visualization

Figure 2: Visualization of a counterexample (a horizontal dotted line denotes $\epsilon = 0.1$)

Figure [2] shows the visualization graphs generated for $\textsf{f2} = (\lozenge_{[1, 10)} (x_1 < 5.5)) \mathbf{U}_{[2, 5]} x_0 \geq 5$ with the subformulas: \begin{align*} \textsf{f2}_{\textsf{1}} = \lozenge_{[1,10)} (x_1 < 5.5) \qquad \textsf{f2}_{\textsf{2}} = x_0 \geq 5 \qquad \textsf{f2}_{\textsf{3}} = x_1 < 5.5 \end{align*}

The robustness degree of $\textsf{f2}$ is less than $\epsilon$ at time $0$, since the robustness degrees of $\textsf{f2}_{\textsf{2}}$ goes below $\epsilon$ in the interval $[2, 5]$.


Reference

[1]. Raisch J., Klein E., Meder C., Itigin A., O’Young S. (1999) Approximating Automata and Discrete Control for Continuous Systems — Two Examples from Process Control. In: Antsaklis P., Lemmon M., Kohn W., Nerode A., Sastry S. (eds) Hybrid Systems V. HS 1997. Lecture Notes in Computer Science, vol 1567. Springer, Berlin, Heidelberg. https://doi.org/10.1007/3-540-49163-5_16