Production of Polysilicon using a Modified Siemens Process
Production of Polysilicon using a Modified Siemens Process
Production of Polysilicon using a Modified Siemens Process
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
CHEMCAD 6.0.1 Page 22<br />
Job Name: Systems Final Project Impurities Date: 05/12/2011 Time: 02:29:15<br />
DISTILLATION PROFILE<br />
Unit type : SCDS Unit name: Eqp # 6<br />
* Net Flows *<br />
Temp Pres Liquid Vapor Feeds Product Duties<br />
Stg K bar kmol/h kmol/h kmol/h kmol/h kW<br />
1 196.5 1.00 188.27 9.41 -1392<br />
2 284.6 1.00 158.86 197.68<br />
3 315.3 1.00 172.65 168.27<br />
4 320.9 1.00 171.44 182.06<br />
5 324.2 1.00 170.70 180.85<br />
6 326.2 1.00 170.43 180.11<br />
7 327.2 1.00 170.34 179.85<br />
8 327.7 1.00 170.30 179.75<br />
9 328.0 1.00 170.29 179.72<br />
10 328.1 1.00 126.47 179.70 15.58<br />
11 329.5 1.00 127.10 120.30<br />
12 329.7 1.00 127.11 120.93<br />
13 329.7 1.00 127.11 120.94<br />
14 329.8 1.00 127.10 120.94<br />
15 329.8 1.00 127.10 120.93<br />
16 329.8 1.00 127.10 120.93<br />
17 329.8 1.00 127.10 120.93<br />
18 329.8 1.00 127.10 120.93<br />
19 329.8 1.00 127.10 120.93<br />
20 329.8 1.00 120.93 6.17 936.9<br />
Mole Reflux ratio 20.000<br />
Total liquid entering stage 10 at 327.978 K, 170.289 kmol/h.