Production of Polysilicon using a Modified Siemens Process
Production of Polysilicon using a Modified Siemens Process
Production of Polysilicon using a Modified Siemens Process
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CHEMCAD 6.0.1 Page 25<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 # 19<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 />
1 307.2 1.00 1.24 12.43 -98.62<br />
2 309.8 1.00 1.22 13.67<br />
3 310.2 1.00 1.22 13.65<br />
4 310.3 1.00 1.21 13.64<br />
5 310.3 1.00 1.21 13.64<br />
6 310.3 1.00 1.21 13.64<br />
7 310.3 1.00 1.21 13.64<br />
8 310.3 1.00 1.21 13.64<br />
9 310.3 1.00 1.21 13.64<br />
10 310.3 1.00 13.51 13.64 12.55<br />
11 314.5 1.00 13.23 13.38<br />
12 319.3 1.00 13.02 13.10<br />
13 323.6 1.00 12.92 12.90<br />
14 326.5 1.00 12.88 12.79<br />
15 328.1 1.00 12.87 12.76<br />
16 329.0 1.00 12.86 12.74<br />
17 329.4 1.00 12.86 12.74<br />
18 329.6 1.00 12.86 12.74<br />
19 329.7 1.00 12.82 12.74<br />
20 330.7 1.00 12.69 0.13 98.66<br />
Mole Reflux ratio 0.100<br />
Total liquid entering stage 10 at 307.586 K, 13.767 kmol/h.