Marina Krotofil
D1 - Marina Krotofil - Hacking Chemical Plants for Competition and Extortion
D1 - Marina Krotofil - Hacking Chemical Plants for Competition and Extortion
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Process interdependencies<br />
%mol<br />
0.0752<br />
0.075<br />
0.0748<br />
0.0746<br />
O2 in Reactor Feed<br />
0.0744<br />
0 2 4 6 8<br />
Hours<br />
%mol<br />
C2H6 in Gas Recycle<br />
0.258<br />
0.256<br />
0.254<br />
0.252<br />
0.25<br />
0.248<br />
0.246<br />
0 1 2 3 4 5 6 7 8<br />
Hours<br />
158<br />
Heater Exit Temperature<br />
156<br />
154<br />
97.2<br />
FEHE Cold Exit Temperature<br />
C<br />
152<br />
97.15<br />
150<br />
148<br />
146<br />
0 1 2 3 4 5 6 7 8<br />
Hours<br />
C<br />
97.1<br />
97.05<br />
97<br />
0.85<br />
Organic Flow Rate<br />
96.95<br />
0 2 4 6 8<br />
Hours<br />
Kmol/min<br />
0.84<br />
0.83<br />
160<br />
159.8<br />
Reactro Exit Temperature<br />
0.82<br />
0.81<br />
0 1 2 3 4 5 6 7 8<br />
Hours<br />
159.6<br />
C<br />
159.4<br />
159.2<br />
159<br />
0 1 2 3 4 5 6 7 8<br />
Hours<br />
0.503<br />
HAc Tank Level<br />
0.502<br />
%<br />
0.501<br />
0.5<br />
0 1 2 3 4 5 6 7 8<br />
Hours
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