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Redoing Coulson Vol.6 Example 12.13 via Timmerhaus Method Example 14.7
m1.5LHX m0.5WHX mm3BHX
nFlowPassages 1FlowPassagesPlates
Δ°Cm
W
21PlateConductivity2
m
4
n13
WHX
LHX
PlatesAHX
mm0.75Platethick
4000
2
mn3
BHX
WHX2
FlowPassages
FlowAreaperStrem
m0.006BHX2De
Δ°Cm
W
0.19ThermalConductivity
s
kg
27.8MassFlow
Δ°Ckg
kJ
2.84CP
sPa
3
100.34Viscosity
3
m
kg
750Density
°C40Tempout
°C95Tempin
Methanol
Δ°Cm
W
0.59ThermalConductivity
Δ°Ckg
kJ
4.2CP
sPa
3
100.8Viscosity
3
m
kg
995Density
°C40Tempout
°C25Tempin
Water
Use respective Matrix indexes
kW4342.36
4
Methanol
2
Methanol
10
Methanol
12
MethanolQHX
s
kg
68.926349
2
Water
4
Water
10
Water
QHX
WaterMassFlow
sn45
m2224
FlowAreaperStrem6
Methanol
12
Methanol
MethanolVelocity
sn37611
m3473888
FlowAreaperStrem6
Water
WaterMassFlow
WaterVelocity
Reynold's number
n17
11120000
8
Methanol
6
MethanolMethanolVelocity
De
MethanolRe
n63
43423600
8
Water
6
WaterWaterVelocity
De
WaterRe
Prandtl number5.082105
14
Methanol
8
Methanol
10
Methanol
MethanolPr
5.6949
12
Water
8
Water
10
Water
WaterPr
21 Oct 2018 08:48:09 - Page3.sm
1 / 2
Generic function of Nusselt function for Re > 100
0.4
Pr
0.64
Re
De
k
0.4Nu , , , PrReDe
k
K
2
m
W
2
5 589575757575758
16
25 n
16
25 173
2
5 2996286060606050
16
25 1112000038
Nu , , , MethanolPr
MethanolRe
De14
MethanolMethanolh
K
2
m
W
2
5 7154691653947020
16
25 n
16
25 633
2
5 40745362639427100
16
25 43423600118
Nu , , , WaterPr
WaterRe
De12
WaterWaterh
K
2
m
W
10000MethanolFouling
Fouling Heat Transfer Coefficients
K
2
m
W
6000WaterFouling
1
WaterFouling
1
Waterh
1
PlateConductivity
Platethick
MethanolFouling
1
Methanolh
1
OverallCoefficient
K55
4
Water
2
MethanolΔT1 K15
2
Water
4
MethanolΔT2
K30.786211
ln
ΔT2
ΔT1
ΔT2
ΔT1
LMTD
Based on max temperature difference i.e Methanol's1.786514
LMTD
4
Methanol
2
Methanol
NTU
Solver will try solving an essentially non-linear eq. An estimated range
of 10-300 for n will reduce solving time
92round , 0solve , , , 30010n
10
Methanol
12
Methanol
AHX
OverallCoefficient
NTUn
2
m68.25AHX92FlowPassages 91Plates
K
2
m
W
7083.947746Methanolh s
m
0.537198MethanolVelocity
K
2
m
W
23806.635689Waterh s
m
1.003952WaterVelocity
K
2
m
W
2059.518971OverallCoefficient
21 Oct 2018 08:48:09 - Page3.sm
2 / 2

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A non-Iterative way for preliminary designing Plate & Frame Exchanger

  • 1. Redoing Coulson Vol.6 Example 12.13 via Timmerhaus Method Example 14.7 m1.5LHX m0.5WHX mm3BHX nFlowPassages 1FlowPassagesPlates Δ°Cm W 21PlateConductivity2 m 4 n13 WHX LHX PlatesAHX mm0.75Platethick 4000 2 mn3 BHX WHX2 FlowPassages FlowAreaperStrem m0.006BHX2De Δ°Cm W 0.19ThermalConductivity s kg 27.8MassFlow Δ°Ckg kJ 2.84CP sPa 3 100.34Viscosity 3 m kg 750Density °C40Tempout °C95Tempin Methanol Δ°Cm W 0.59ThermalConductivity Δ°Ckg kJ 4.2CP sPa 3 100.8Viscosity 3 m kg 995Density °C40Tempout °C25Tempin Water Use respective Matrix indexes kW4342.36 4 Methanol 2 Methanol 10 Methanol 12 MethanolQHX s kg 68.926349 2 Water 4 Water 10 Water QHX WaterMassFlow sn45 m2224 FlowAreaperStrem6 Methanol 12 Methanol MethanolVelocity sn37611 m3473888 FlowAreaperStrem6 Water WaterMassFlow WaterVelocity Reynold's number n17 11120000 8 Methanol 6 MethanolMethanolVelocity De MethanolRe n63 43423600 8 Water 6 WaterWaterVelocity De WaterRe Prandtl number5.082105 14 Methanol 8 Methanol 10 Methanol MethanolPr 5.6949 12 Water 8 Water 10 Water WaterPr 21 Oct 2018 08:48:09 - Page3.sm 1 / 2
  • 2. Generic function of Nusselt function for Re > 100 0.4 Pr 0.64 Re De k 0.4Nu , , , PrReDe k K 2 m W 2 5 589575757575758 16 25 n 16 25 173 2 5 2996286060606050 16 25 1112000038 Nu , , , MethanolPr MethanolRe De14 MethanolMethanolh K 2 m W 2 5 7154691653947020 16 25 n 16 25 633 2 5 40745362639427100 16 25 43423600118 Nu , , , WaterPr WaterRe De12 WaterWaterh K 2 m W 10000MethanolFouling Fouling Heat Transfer Coefficients K 2 m W 6000WaterFouling 1 WaterFouling 1 Waterh 1 PlateConductivity Platethick MethanolFouling 1 Methanolh 1 OverallCoefficient K55 4 Water 2 MethanolΔT1 K15 2 Water 4 MethanolΔT2 K30.786211 ln ΔT2 ΔT1 ΔT2 ΔT1 LMTD Based on max temperature difference i.e Methanol's1.786514 LMTD 4 Methanol 2 Methanol NTU Solver will try solving an essentially non-linear eq. An estimated range of 10-300 for n will reduce solving time 92round , 0solve , , , 30010n 10 Methanol 12 Methanol AHX OverallCoefficient NTUn 2 m68.25AHX92FlowPassages 91Plates K 2 m W 7083.947746Methanolh s m 0.537198MethanolVelocity K 2 m W 23806.635689Waterh s m 1.003952WaterVelocity K 2 m W 2059.518971OverallCoefficient 21 Oct 2018 08:48:09 - Page3.sm 2 / 2