Overview
Comment: | Initial revision |
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Downloads: | Tarball | ZIP archive | SQL archive |
Timelines: | family | ancestors | descendants | both | origin/master | trunk |
Files: | files | file ages | folders |
SHA3-256: |
0428fdd508f175bc742f8abb5656cf12 |
User & Date: | gawthrop@users.sourceforge.net on 1998-03-09 10:13:27 |
Other Links: | branch diff | manifest | tags |
Context
1998-03-09
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10:19:43 | Added note about energy consevation. check-in: 2bff7c924e user: gawthrop@users.sourceforge.net tags: origin/master, trunk | |
10:13:27 | Initial revision check-in: 0428fdd508 user: gawthrop@users.sourceforge.net tags: origin/master, trunk | |
1998-03-08
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21:01:40 | Now does multiple crs check-in: 0c29b561b7 user: gawthrop@users.sourceforge.net tags: origin/master, trunk | |
Changes
Added mttroot/mtt/lib/comp/compound/Thermal/IncompressibleFlow/Pipe/Pipe_desc.tex version [81399e8826].
> > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > > | 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 | % Verbal description for system Pipe (Pipe_desc.tex) % Generated by MTT on Tue Jan 13 18:02:53 GMT 1998. % %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % %% Version control history % %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % %% $Id$ % %% $Log$ % %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% The acausal bond graph of system \textbf{Pipe} is displayed in Figure \Ref{Pipe_abg} and its label file is listed in Section \Ref{sec:Pipe_lbl}. The subsystems are listed in Section \Ref{sec:Pipe_sub}. The \textbf{Pipe} component represents one way flow of incompressible fluid though a pipe. Externally, it has true energy bonds: $P$/$\dot V$ (Pressure/volume-flow) representing hydraulic energy and $T$/$\dot S$(Temperature/Entropy-flow) representing convected thermal energy. Internally, however, the thermal part is represented by a pseudo bond graph which computes the flow of internal energy $\dot E$ from the upstream temperature $T_1$ and the volumetric flow rate $\dot V$ as: \begin{equation} \dot E = \rho c_p T_1 \dot V \end{equation} The $AF$ component makes the $FMR$ component use $T_1$ rather than $T_1-T_2$. The two \textbf{ES} components provide the conversion from true to psuedo thermal bonds and vice versa. %%% Local Variables: %%% mode: latex %%% TeX-master: t %%% End: |