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of sections Eff-c = 1.0 Eff-C = 0.9 Eff-C = 0.8 Eff-C Temperature (C) Total no

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z(n) z(n)

y(n) x(n)

yp(n-1) x(n-1) z(n+1)

x(n+1) y(n+1)

yp(n) x(n)

z(1) z(1)

y(1) x(1)

yp(0) x(0)

z(2) z(2)

y(2) x(2)

yp(1) x(1)

y(n+1)

x(n+1)

z(n+1)

z(0) x(0)

z(3) yp(2) x(2)

L2 V2

Lh L1

zf

z(n+1)

L1 Lh

L2

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20 30 40 50 60 70 80

60 70 80 90

Temperature (C)

Total no. of sections

Eff-c = 1.0 Eff-C = 0.9 Eff-C = 0.8 Eff-C = 0.7

30 40 50 60 70 80 90

60 70 80 90

Temperature (C)

Total no. of sections

Eff-C = 1.0 Eff-C = 0.9 Eff-C = 0.8 Eff-C = 0.7

(11)

30 35 40 45 50 55 60 65 70

0 1 2 3 4 5 6

NTS of a CY packing

Total no. of sections

Eff-C = 1.0 Eff-C = 0.9 Eff-C = 0.8 Eff-C = 0.7

Liquid

Distributer Sulzer

Packing

Liquid

Collector

Catalyst Bed

참조

관련 문서

[r]

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화학량론적 계산:

Current (A) Ambient temperature (°C) Peak temperature (°C) additional requirements-. 20 55 60 Ambient temperature +55°C during 24 hours with peaks