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* o! O; @2 |9 F7 S, y2 S' N; q计算结果： , U% G5 A3 L. t6 R# [
Shortcut Column 'SCD1'
7 z% ]* w$ B& x, }! g- k6 q. g& N FEEDS/ ^3 }7 S& X. v
STREAM PHASE ! l& c) j9 l: y4 @- P
------------ ------
5 y: k0 P* f/ D: Y# F4 z S12 LIQUID2 y) v# Q0 g* F4 S2 S
PRODUCTS
$ Y2 e& S: @3 J0 ? y ------------- TOTAL STREAM RATES -------------
5 c- f/ G" B( C! r8 f* d" f MOLES WEIGHT LIQUID VOL NORM VAPOR(1) NUM1 o) i- E& C1 X! O7 V
STREAM + PHASE KG-MOL/HR KG/HR M3/HR M3/HR SECTION TRAYS
; C! _3 t5 D( R6 m9 B, C, g' v: J ------------ - ---------- ---------- ---------- ---------- ------- -----
$ E" V1 _$ r) t S13 L 4.70 200.98 0.25 105.37 1 4.60
2 m/ U, t/ t* N7 L8 Y$ b+ [1 Z S14 L 95.30 1717.36 1.72 2136.03 5 V) \% H1 c2 A" J/ u; a; Z5 N- \
TOTALS 100.00 1918.35 1.97 2241.40 4.60$ M! ], v' E" K
SPECIFICATIONS
9 _. j, }. \9 E PARAMETER COMP. SPECIFICATION SPECIFIED CALCULATED
# C! X( c. W { P1 T; V TYPE NUM TYPE VALUE VALUE
. [. T2 K) \' K0 ^% l ----------------- ------- ------------- ---------- ----------2 _) q1 S$ u. T+ p
STRM S13 2 VOL PERCENT 9.600E+01 9.600E+01 0 F; e; b5 J' U
STRM S14 2 WT PERCENT 5.000E-02 5.003E-02 7 w: ~" N* {2 l5 @
SUMMARY OF UNDERWOOD CALCULATIONS7 K% E0 b7 ] m+ [2 |5 j4 d
MINIMUM REFLUX RATIO 5.82157
{% F+ t4 H1 C9 C FEED CONDITION Q 1.16050
. `+ s8 J i# q& y FENSKE MINIMUM TRAYS 4.60057 ; P. j: z3 [* f5 ]% o1 Z* X: i
OPERATING REFLUX RATIO 1.25 * R-MINIMUM
. N% R$ G+ l6 h. \* s# C$ M TOTAL FEED R/R-MIN M/M-MIN REFLUX DUTY, M*KCAL/HR 6 Q: ?5 l. L+ N* y: a; B5 S
TRAYS TRAY RATIO CONDENSER REBOILER4 q1 V, D; f D/ C2 Y5 h( y
----- ---- ------- ------- ------ ---------- ----------3 l" V' O- R9 g* ?, c+ V
11 2.75 1.125 2.419 6.549 -3.311E-01 4.662E-01 ! v6 l5 z- j. T, J9 P8 m9 B
10 2.57 1.188 2.222 6.913 -3.470E-01 4.822E-01
$ C- f" |& P8 X 10 2.42 1.250 2.066 7.277 -3.630E-01 4.981E-01 8 W$ U* s2 I; a) N5 c. b% p
9 2.30 1.312 1.939 7.641 -3.789E-01 5.141E-01 ' s, X: ^' Y" K4 X0 x: f8 R4 X; s
8 2.21 1.375 1.835 8.005 -3.949E-01 5.300E-01 |
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