Parameter Unit Value
J·g−1 ·K−1 4.183 Obtained from literature Perry and Green (2007) [7 ]
J·g−1 ·K−1 2.9281 Obtained from literature Perry and Green (2007) [7 ] Blow down tank
m3 30 Designed
m3 60 Calculated from (6 )
Pa
Calculated from (1 )
kg·s−1 346 Calculated from (2 )
Pa
Obtained from literature Fauske (1988) [1 ], Leung (1986) [2 ]
Pa
PaCalculated from (7 )
/ 0.24 Calculated from (34 )
kg·s−1 82 Calculated from (35 )
m
Designed MAWP Pa
Designed Safety relief valve DN m
0.65 Designed
Pa
Designed Vent area
J·kg−1 846 Calculated from (6)
kg·m−2 ·s−1 2124 Calculated from (2 )
m2 0.326 Calculated from (3 )
m 0.65 Calculated from (5) Calculated data horizontal heat exchanger
mm 5000 Designed
=
W·m−2 ·K−1
Obtained from literature Perry and Green (2007) [7 ]
W·m−1 ·K−1 16.2 Obtained from literature Perry and Green (2007) [7 ]
W 585711 Calculated from (8 )
W 366125 Calculated from (8 )
°C 80 Calculated from (8 ) LMTD
°C 76.16 Calculated from (9 )
/ 6.83 Obtained from literature Richardson et al. (2009) [10 ]
/ 0.0594 Obtained from literature Richardson et al. (2009) [10 ]
/ 0.96 Obtained from literature Richardson et al. (2009) [10 ]
°C 73.11 Calculated from (10 )
m2 54 Calculated from (11 )
/ 85 Calculated from (13 ) Pipe dimensions for horizontal heat exchanger
mm 50.8 BWG 16 Perry and Green (2007) [7 ], INOX, AISI316
mm 46.732 Wall thickness mm 2.034
mm 63.5 Calculated from (14 )
mm 689.1 Calculated from (15 ) BDC mm 93 Obtained from diagrams Richardson et al. (2009) [10 ]
mm 782 Calculated from (16 )
mm 313 Calculated from (17 )
m2 0.04895 Calculated from (18 )
kg·s−1 ·m−2 1986 Calculated from (19 )
mm 36.07 Calculated from (20 )
/ 65127 Calculated from (21 )
/ 7.48 Calculated from (22 )
/ 323 Calculated from (23 )
W·m−2 ·K−1 5490 Calculated from (23 ) and (25 )
mm 875 Calculated from (26 )
Pa 53800 Calculated from (25 )
/ 85 Calculated from (27 )
kg·m−2 ·s−1 7971 Calculated from (28 )
m·s−1 2596 Calculated from (29 ) Retube / 30390 Calculated from (21 ) Prtube / 0.575 Calculated from (22 )
W·m−2 ·K−1 0.044 Calculated from (30 )
W·m−2 ·K−1 0.022 Calculated from (32 )
W·m−2 ·K−1 1957 Calculated from (31 )
Pa 91500 Calculated from (33 ) Calculated data vertical heat exchanger Recycle h−1 22.22 Calculated from (40 ) Total heat vertical kW 23553 Calculated from (36 ) Heat per recycle kW 145.4 Calculated from (38 )
°C 80 Calculated from (8 )
m2 5 Calculated from (11 )
°C 40 Calculated from (8 )
°C 15 Calculated from (8 )
°C 24 Calculated from (8 ) Pipe dimensions for vertical heat exchanger
mm 2500 Designed
mm 50.8
BWG 16 Perry and Green (2007) [7 ]
mm 46.732 Wall thickness mm 2.034
mm 63.5 Calculated from (14 )
mm 286.7 Calculated from (15 ) BDC mm 88 Obtained from diagrams Richardson et al. (2009) [10 ]
mm 388 Calculated from (16 )
mm 155.2 Calculated from (17 )
m2 0.012043 Calculated from (18 )
kg·s−1 ·m−2 8072 Calculated from (19 )
mm 36.07 Calculated from (20 ) Reshell / 264718 Calculated from (21 ) Prshell / 7.48 Calculated from (22 ) Nushell / 2547 Calculated from (23 )
W·m−2 ·K−1 43435 Calculated from (23 ) and (24 )
mm 437.5 Calculated from (26 )
Pa 82000 Calculated from (25 )
/ 13 Calculated from (27 )
kg·m−2 ·s−1 6196 Calculated from (28 )
m·s−1 2018 Calculated from (29 )
/ 23545 Calculated from (21 )
/ 0.575 Calculated from (22 )
Pa 128000 Calculated from (33 )
W·m−2 ·K−1 0.036 Calculated from (30 )
W·m−2 ·K−1 0.01867 Calculated from (32 )
W·m−2 ·K−1 5617 Calculated from (31 ) LMTD
°C 38.44 Calculated from (9 )
/ 4.44 Obtained from literature Richardson et al. (2009) [10 ]
/ 0.1385 Obtained from literature Richardson et al. (2009) [10 ]
/ 0.96 Obtained from literature Richardson et al. (2009) [10 ]
°C 36.7 Calculated from (10 )
m2 5 Calculated from (11 )
/ 13 Calculated from (13 ) Absorber and scrubber Scrubber
kg·s−1 42.21 Calculated from reaction stoichiometry Recycle h−1 22.22 Calculated from (40 )
m3 4.5 Calculated from (40 )
m
Designed MAWP Pa
Designed Absorber
/ 0.023 Calculated ratio
/ 1.8 Obtained from correlations proposed in literature Seader et al. (2010) [11 ]
kg·m−2 ·s−1 49 Calculated from obtained factor
m2 1.68 Calculated from (41 )
m 1.46 Calculated from (42 )
m 0.3048 Obtained from literature Seader et al. (2010) [11 ] No foaming factor
/ 1 Obtained from literature Seader et al. (2010) [11 ]
/ 12 Obtained from literature Seader et al. (2010) [11 ] IMTP packing mm 88.9 Obtained from literature Seader et al. (2010) [11 ]
/ 1.66 Obtained from literature Seader et al. (2010) [11 ] HETP m 1.83 Obtained from literature Seader et al. (2010) [11 ]
m 3 Obtained from literature Seader et al. (2010) [11 ]
12 Obtained from literature Seader et al. (2010) [11 ]
m3 /h
m2
59.9 Obtained from literature Seader et al. (2010) [11 ]
m
Designed MAWP Pa
Designed Neutralization reaction in absorber and in scrubber
kJ·mol−1 22.32 Calculated from literature data Perry and Green (2007) [7 ]
kW 7.1 Calculated from (37 ) Centrifugal pump
m3 ·h−1 100 Calculated from reaction stochiometry
Pa 400000 Designed Ventilator fan design
Pa 500 Calculated from (43 )
m3
h−1 72000 Calculated from (44 ) and (45 )
m
s−1 230 Calculated from (47 )
RPM 2920 Calculated from (44 ) and (45 )
kW 34 Calculated from (46 )
mm 1460 Calculated from (44 ) and (45 ) Chimney design
mm 6000 Obtained from literature diagrams Bleier (1987) [12 ]
mm 500 Obtained from literature diagrams Bleier (1987) [12 ] Pipe sizing Pipes from blow down tank via horizontal heat exchanger to absorber DNpipes Blow down tank-horizontal heat exchanger mm 400 Calculated from (48 ) Horizontal heat exchanger-absorber mm 400 Calculated from (48 ) Pipes from scrubber via pump and vertical heat exchanger to absorber DNpipes Pipes from scrubber via pump mm 125 Calculated from literature data Fauske (1986), Richardson et al. (2009) [3 ] Cooling water pipes DNpipes Main cooling water pipes mm 300 Calculated from literature data Fauske (1986), Richardson et al. (2009) [3 ] Cooling water pipes after crossing mm 200 Calculated from literature data Fauske (1986), Richardson et al. (2009) [3 ]
