LMTD Correction Factor Chart, Exams of Thermodynamics

Calculate the log mean temperature difference ∆Tlm and the correction factor F, if necessary. 4.Obtain (select or calculate) the value of the ...

Typology: Exams

2022/2023

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16042014
1
LMTDCorrectionFactor
Chart
Nimish Shah
2
The LMTD method is very suitable for determining the
size of a heat exchanger to realize prescribed outlet
temperatures when the mass flow rates and the inlet
and outlet temperatures of the hot and cold fluids are
specified.
With the LMTD method, the task is to select a heat
exchanger that will meet the prescribed heat transfer
requirements.
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pf4
pf5
pf8
pf9
pfa
pfd

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LMTD Correction Factor

Chart

Nimish Shah

2

The LMTD method is very suitable for determining the

size of a heat exchanger to realize prescribed outlet temperatures when the mass flow rates and the inlet and outlet temperatures of the hot and cold fluids are specified.

With the LMTD method, the task is to select a heat

exchanger that will meet the prescribed heat transfer

requirements.

Tm an appropriate mean (average) temperature difference between the two fluids

4

TYPES OF HEAT EXCHANGERS

7

Multipass and Cross-Flow Heat Exchangers: Use of a Correction Factor

F correction factor depends on the geometry of the heat exchanger and the inlet and outlet temperatures of the hot and cold fluid streams. F for common cross-flow and shell-and-tube heat exchanger configurations is given in the figure versus two temperature ratios P and R defined as

1 and 2 inlet and outlet T and t shell- and tube-side temperatures

8

Correction factor F charts for common shell- and-tube heat exchangers.

9

Correction factor F charts for common cross-flow heat exchangers.

10

is the rate of evaporation or condensation of the fluid

h (^) fg is the enthalpy of vaporization of the fluid at the

specified temperature or pressure.

The heat capacity rate of a fluid during a phase-change

process must approach infinity since the temperature

change is practically zero.

  • Assumptions made in the derivation of the temperature

correction factor Ft, in addition to those made for LMTD:

    1. Equal heat transfer areas in each pass.
    1. A constant overall heat-transfer coefficient in each pass.
    1. The temperature of the shell-side fluid in any pass is constant

across any cross section.

    1. There is no leakage of fluid between shell passes.
  • Though these conditions will not be strictly satisfied in practical

heat exchangers, the Ft values obtained from the curves will give an estimate of the “true mean temperature difference” that is sufficiently accurate for most designs.

Lets calculate one Example….!

Calculate for the following cases, the surface area required for a heat

exchanger which is required to cool 3200 kg/h of benzene (Cp=1.

kJ/kg 0 C) from 71 0 C to 42 0 C. The cooling water (Cp =4.18 kJ/kg 0 C) at

15 0 C has a flow rate of 2200 kg/h.

  • (i) Single pass counter-flow,
  • (ii) 1-4 exchanger (one-shell pass and four-tube passes), and
  • (iii) Cross flow single pass with water mixed and benzene unmixed.

For each configuration, the overall heat transfer coefficient may be taken

as 0.28 kW/m 2 0C.

(i) Single pass counter‐flow

  • Find mass flowrate…
  • Calculate outlet temperature of cooling water…..
  • Calculate total Heat transfer/ duty Q….
  • Draw temperature profile….
  • Find ∆tm for …..
    • 32 0 C
  • Calculate Area required….
    • 5.1 m^2

Use Chart for 1 ‐ 2 pass

Use Chart for 1 ‐ 2 pass F=0.

• F = 0.

  • Calculate Area….
    • 5.66 m^2

(ii) 1 ‐ 4 exchanger (one‐shell pass and four‐

tube passes)

(iii) Cross flow exchanger (one‐ fluid mixed

other unmixed)

  • Find mass flowrate…
  • Calculate outlet temperature of

cooling water…..

  • Calculate total Heat transfer/

duty Q….

  • Draw temperature profile….
    • Same as last calculated
    • Same as last calculated
    • Same as last calculated
    • Draw it for counter flow arrangement

Use Chart for Cross flow

F = 0.

• F = 0.

  • Calculate Area….
    • 5.64 m^2

(iii) Cross flow exchanger (one‐ fluid mixed

other unmixed)