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henrikt-ma committed Aug 25, 2020
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2 changes: 1 addition & 1 deletion chapters/connectors.tex
Expand Up @@ -87,7 +87,7 @@ \subsection{Inside and Outside Connectors}\label{inside-and-outside-connectors}
\begin{center}
\includegraphics{innerouterconnector}
\end{center}
\caption{Example for inside and outside connectors}
\caption{Example for inside and outside connectors.}
\end{figure}
The figure visualizes the following \lstinline!connect! equations to
the connector \lstinline!c! in the models \lstinline!m!$i$. Consider the
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6 changes: 3 additions & 3 deletions chapters/derivationofstream.tex
Expand Up @@ -44,7 +44,7 @@ \section{Reasons for avoiding the actual mixing enthalpy in connector definition
\begin{center}
\includegraphics[width=3in,height=3in]{fluidmix}
\end{center}
\caption{Exemplary connection set with three connected components and a common mixing enthalpy}
\caption{Exemplary connection set with three connected components and a common mixing enthalpy.}
\end{figure}

\section{Rationale for the formulation of inStream}\label{rationale-for-the-formulation-of-the-instream-operator}
Expand Down Expand Up @@ -140,7 +140,7 @@ \section{Rationale for the formulation of inStream}\label{rationale-for-the-form
\begin{center}
\includegraphics[width=3in,height=3in]{fluidmix3}
\end{center}
\caption{Exemplary connection set with three connected components}
\caption{Exemplary connection set with three connected components.}
\end{figure}

In the general case of a connection set with \emph{n} components,
Expand Down Expand Up @@ -191,7 +191,7 @@ \subsection{Connection of 3 stream connectors where one mass flow rate is identi
\begin{center}
\includegraphics[width=6in,height=3in]{fluidmix4}
\end{center}
\caption{Example series connection of multiple models with stream connectors }
\caption{Example series connection of multiple models with stream connectors.}
\end{figure}

For the two components with finite mass flow rates (not the sensor), the
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2 changes: 1 addition & 1 deletion chapters/operatorsandexpressions.tex
Expand Up @@ -49,7 +49,7 @@ \section{Operator Precedence and Associativity}\label{operator-precedence-and-as
or ternary. Operators with the same precedence occur at the same line of
the table:
\begin{table}[H]
\caption{Operators}
\caption{Operators.}
\begin{tabular}{|p{5cm}|p{5cm}|p{4cm}|}
\hline
\tablehead{Operator Group} & \tablehead{Operator Syntax} & \tablehead{Examples}\\ \hline
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2 changes: 1 addition & 1 deletion chapters/stream.tex
Expand Up @@ -126,7 +126,7 @@ \section{Stream Operator inStream and Connection Equations}\label{stream-operato
\begin{center}
\includegraphics[width=2.3in,height=2.08125in]{fluidsystem}
\end{center}
\caption{Examplary FluidSystem with $N$=3 and $M$=2}
\caption{Examplary \lstinline!FluidSystem! with $N = 3$ and $M = 2$.}
\end{figure}

\begin{nonnormative}
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2 changes: 1 addition & 1 deletion chapters/synchronous.tex
Expand Up @@ -18,7 +18,7 @@ \subsection{Overview}\label{overview}
\begin{center}
\includegraphics[width=7in,height=4in]{plantmodel}
\end{center}
\caption{A continuous plant and a sampled data controller connected together with sample and (zero-order) hold elements}
\caption{A continuous plant and a sampled data controller connected together with sample and (zero-order) hold elements.}
\end{figure}

\begin{itemize}
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