|
CND12 Condenser data summary |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Calculation reference : |
|
CONDCHMPA |
|
|
|
|
|
|
|
Calculation object : |
|
Updating for presentation and costs |
|
|
|
|
|
|
|
If condenser for vacuum duty : |
|
Standard example C & H |
|
|
|
|
|
|
|
Calculation date and time : |
|
11-Aug-03 |
|
10:13:37 |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Gas/vapour composition: |
|
|
|
kg/h |
|
Mol. Wt. |
|
|
|
Non condensables |
|
Nitrogen |
|
1,270.000 |
|
28.016 |
|
|
|
Condensing vapour |
|
Water vapour |
|
4,131.389 |
|
18.016 |
|
|
|
|
|
|
|
|
|
|
|
|
|
Condenser physical parameters: |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Sections: |
9 |
|
Exchanger tube |
|
Arrangement: |
|
Triangular |
|
|
Number: |
88 |
|
Shell/tubesheet material |
|
(-) |
|
C/MS |
|
|
Tube clearance: |
6.350 |
|
Tube |
|
Material |
|
C/MS |
|
|
Tube passes: |
1 |
|
Baffle |
|
% cut |
|
45 |
|
|
Number: |
30 |
|
Nozzle diameter, mm |
|
Inlet: |
|
350.00 |
|
|
Outlet: |
150 |
|
|
|
|
|
|
|
|
|
|
|
Calc. diameter of tube bundle |
|
mm |
|
262.63 |
|
|
|
|
|
Inside shell diameter - used |
|
mm |
|
605.63 |
|
|
|
|
|
Shell bundle clearance allowance |
|
mm |
|
343.00 |
|
|
|
|
|
Baffle spacing |
|
mm |
|
421.00 |
|
|
|
|
|
Outside tube diameter |
|
mm |
|
19.05 |
|
|
|
|
|
Tube wall thickness |
|
mm |
|
1.651 |
|
|
|
|
|
Total length of tubes - calculated |
|
m |
|
13.116 |
|
|
Available m: |
12.63 |
|
Thickness of tube sheet |
|
mm |
|
35.000 |
|
|
|
|
|
Outside condensing surface - calculated |
|
m^2 |
|
65.762 |
|
|
Available m^2: |
66.52 |
|
Min. shell section area for flow |
|
m^2 |
|
0.102 |
|
|
|
|
|
Equivalent tube diameter |
|
mm |
|
18.542 |
|
|
|
|
|
|
|
|
|
|
|
|
|
|
|
Pressure losses: |
|
|
|
|
|
|
|
|
|
Condenser total pressure loss |
|
mbar |
|
43.529 |
|
|
|
|
|
Shell side pressure loss |
|
mbar |
|
39.847 |
|
|
|
|
|
Nozzle pressure loss, mbar |
|
inlet |
|
2.233 |
|
|
outlet: |
1.45 |
|
|
|
|
|
|
|
|
|
|
|
Condenser conditions: |
|
|
|
|
|
|
|
|
|
Inlet vapour/gas mass flow rate |
|
kg/m^2.h |
|
52,961.19 |
|
|
|
|
|
Pressure at condenser inlet |
|
mbar |
|
1,013.00 |
|
|
|
|
|
Gas/vapour inlet temperature |
|
oC |
|
95.02 |
|
|
|
|
|
Gas/vapour outlet temperature |
|
oC |
|
40.00 |
|
|
|
|
|
CW temp. at inlet to condenser |
|
oC |
|
25.00 |
|
|
|
|
|
CW temp. at outlet from condenser |
|
oC |
|
60.00 |
|
|
|
|
|
Av. temperature of condensate at exit |
|
oC |
|
50.00 |
|
|
|
|
|
Cooling water requirement |
|
m^3/h |
|
70.495 |
|
|
|
|
|
Total heat rejected |
|
kW/h |
|
2,838.704 |
|
kJ/h |
10,219,333.22 |
|
|
Average thermal loading calc area |
|
kW/h.m^2 |
|
43.166 |
|
Actual |
42.68 |
|
|
Thermal conductivity of tube wall |
|
W/m.K |
|
112.645 |
|
|
|
|
|
Thermal resistance of tube wall |
|
m^2.K/W |
|
0.0000147 |
|
W/m^2.K |
68,228.35 |
|
|
Fouling factor - condensing side |
|
m^2.K/W |
|
0.0001239 |
|
W/m^2.K |
8,071.03 |
|
|
Fouling factor - CW side |
|
m^2.K/W |
|
0.0001239 |
|
W/m^2.K |
8,071.03 |
|
|
Cooling water resistance |
|
m^2.K/W |
|
0.0001942 |
|
W/m^2.K |
5,149.76 |
|
|
Condensate film resistance |
|
m^2.K/W |
|
0.0000881 |
|
W/m^2.K |
11,352.00 |
|
|
Sum of 'constant' resistances |
|
m^2.K/W |
|
0.0005507 |
|
W/m^2.K |
1,815.96 |
|
|
CW velocity |
|
m/s |
|
1.200 |
|
|
|
|
|
CW Reynolds Number |
|
(-) |
|
30,051.66 |
|
|
|
|
|
CW mass flow rate |
|
kg/m^2.h |
|
4,282,254.85 |
|
|
|
|
|
NC gas mole fraction - entry |
|
(-) |
|
0.1650 |
|
outlet |
0.93 |
|
|
Vapour/gas ReN at condenser - entry |
|
(-) |
|
17,538.40 |
|
outlet |
3,668.91 |
|
|
Sensible heat transfer coeff.- entry |
|
W/m^2.K |
|
150.72 |
|
outlet |
51.10 |
|
|
Molar mass transfer coeff. - entry |
|
kmol/h.m^2.bar |
|
82.77 |
|
outlet |
5.92 |
|
|
Overall heat transfer coeff. - entry |
|
W/m^2.K |
|
642.36 |
|
outlet |
225.25 |
|
|
NC gas heat transfer coeff. - entry |
|
W/m^2.K |
|
993.96 |
|
outlet |
257.14 |
|
|
|
|
|
|
|
|
|
|
|
|
Practical LMTD |
|
oC |
|
42.966 |
|
|
|
|
|
HTC based on calculated surface |
|
W/m^2.K |
|
1,004.666 |
|
|
|
|
|
Actual HTC based on actual surface |
|
W/m^2.K |
|
993.271 |
|
|
|
|
|
Factor available from HTC difference |
|
m^2.K/W |
|
0.0000114 |
|
|
W/m^2.K |
87,570.99 |
|
|
|
|
|
|
|
|
|
|
|
Condenser and condensation costs: |
|
|
|
Purchase cost |
|
|
Installed cost |
|
|
|
|
|
|
Jan 1999 |
|
|
Jan-99 |
|
|
|
|
|
|
£ |
|
|
£ |
|
|
Condenser supply source : |
|
|
|
Specialist |
|
|
|
|
|
Selected CW pump |
|
|
|
Pump in steel casing and CI impeller |
|
|
|
|
|
Cost of condenser - Method : |
A |
£ |
|
9,513.09 |
|
|
20,680.63 |
|
|
Cost of CW pump |
|
£ |
|
9,847.52 |
|
|
19,695.05 |
|
|
Total capital costs |
|
£ |
|
19,360.61 |
|
|
40,375.68 |
|
|
|
|
|
|
|
|
|
|
|
|
Condenser operating costs: (Page 8) |
|
|
|
|
|
|
|
|
|
Total utility costs (TUC) |
|
£/a |
|
88,092.07 |
|
|
|
|
|
Total annual cost (TAC) |
|
£/a |
|
95,713.54 |
|
|
103,967.63 |
|
|
Total maintenance cost (TMC) |
|
£/a |
|
4,431.47 |
|
|
|
|
|
Total (ownership) costs (TVC) |
|
£/a |
|
100,145.00 |
|
|
|
|
|
Annual TVC for pumping kg/h suction gas |
|
£ |
|
18.541 |
|
|
|
|
|
Total cost for condensing kg of vapour |
|
£ |
|
0.00328 |
|
|
|
|
|
Total cost of removing a kg of from the system |
£ |
|
0.00247 |
|
|
0.00 |
|