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计算结果：
# L. a+ X! j* JShortcut Column 'SCD1'
6 a/ m3 H4 O8 X: g: x FEEDS
$ Z5 Q% J3 _- c: Q) g2 ^ STREAM PHASE
, n; H/ k6 s! [' q! j1 z; w6 R ------------ ------ * v% {$ S# P) o! O4 Y6 [) \
S12 LIQUID" i$ Y8 [! L4 E2 S/ o( R& d6 r
PRODUCTS " W, B0 |) D% U
------------- TOTAL STREAM RATES -------------1 @0 |& u& j7 h. P, j+ r/ D
MOLES WEIGHT LIQUID VOL NORM VAPOR(1) NUM
. m* \' e6 b0 J5 j* f STREAM + PHASE KG-MOL/HR KG/HR M3/HR M3/HR SECTION TRAYS 1 C; ~8 v8 f2 a. S" Y
------------ - ---------- ---------- ---------- ---------- ------- -----
. _2 {3 K1 G7 _ S13 L 4.70 200.98 0.25 105.37 1 4.60# ?7 X; Y5 Z# z$ v2 V
S14 L 95.30 1717.36 1.72 2136.03 + s3 a6 x$ b& r
TOTALS 100.00 1918.35 1.97 2241.40 4.60. V S# m2 D* c
SPECIFICATIONS
+ @4 ^$ J9 h' _3 } PARAMETER COMP. SPECIFICATION SPECIFIED CALCULATED
5 i2 w' H- ?" Y5 f" W: Q) c1 n. R2 B% i! U TYPE NUM TYPE VALUE VALUE & Z2 R$ x8 X3 n. B$ _, U$ o
----------------- ------- ------------- ---------- ----------
l8 N# A+ Z9 }1 f STRM S13 2 VOL PERCENT 9.600E+01 9.600E+01 2 m' L1 b ~7 Y" D; |* t1 Q' L
STRM S14 2 WT PERCENT 5.000E-02 5.003E-02
/ B( ~2 M# Y- \( [& t SUMMARY OF UNDERWOOD CALCULATIONS6 ~1 [( q) Z5 \ N8 O
MINIMUM REFLUX RATIO 5.82157
8 z+ e* A1 K, h* a7 X6 c FEED CONDITION Q 1.16050 # v5 @/ e6 U" W+ K
FENSKE MINIMUM TRAYS 4.60057 % p6 L1 l& {. O$ g/ V
OPERATING REFLUX RATIO 1.25 * R-MINIMUM 9 B! Z5 Z7 Z% t+ w- `1 M9 }) J6 C
TOTAL FEED R/R-MIN M/M-MIN REFLUX DUTY, M*KCAL/HR
# Q5 [( \2 _) C8 W5 j# P TRAYS TRAY RATIO CONDENSER REBOILER
; Q7 d" E3 T2 o ----- ---- ------- ------- ------ ---------- ----------( ?% ?4 K: i% C
11 2.75 1.125 2.419 6.549 -3.311E-01 4.662E-01 * c7 ^) J+ v; h, ?: @% y4 N
10 2.57 1.188 2.222 6.913 -3.470E-01 4.822E-01 2 Z8 r& |( X2 ?9 S- h$ @0 y
10 2.42 1.250 2.066 7.277 -3.630E-01 4.981E-01
" g L& ~3 a2 m$ V" c. { 9 2.30 1.312 1.939 7.641 -3.789E-01 5.141E-01 0 S& N/ u) J, v2 s5 F
8 2.21 1.375 1.835 8.005 -3.949E-01 5.300E-01 |
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3179
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