Page 287 - Materials Chemistry, Second Edition

L1644_C06.fm Page 258 Monday, October 20, 2003 12:06 PM

TABLE 6.12
Scenario 1: Steam Production with Refining and Electricity Production
(Spanish Mix, 1995)
Mixture (kg emission/t C 3 H 8 ) Separation (kg emission/t C 3 H 8 )

Steam Electricity Venting

504.49 619.94 151.59 —
CO 2
2.14 5.67 0.87 —
SO 2
COD 0.055 0.0041 0.00046 —
VOC 2.73 8.51 0.77 0.00422

TABLE 6.13
Scenario 2: Steam Production with Refining and Electricity Production
(Norwegian Matrix, 1995)

Mixture (kg emission/t C 3 H 8 ) Separation (kg emission/t C 3 H 8 )
Steam Electricity Venting

504.49 619.94 110.23 —
CO 2
2.14 5.67 0.00108 —
SO 2
COD 0.055 0.0041 0.00000173 —
VOC 2.73 8.51 0.00084 0.00422

TABLE 6.14
Scenario 3: Steam Production with Refining and Electricity Production
(Natural Gas Combustion)

Mixture (kg emission/t C 3 H 8 ) Separation (kg emission/t C 3 H 8 )
Steam Electricity Venting

504.49 619.94 573.29 —
CO 2
2.14 5.67 0.0137 —
SO 2
COD 0.055 0.0041 0.00035 —
VOC 2.73 8.51 0.185 0.00422

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