lecture10_heatexchangers

26
1 (1) Heat Exchanger Types (2) Heat Exchanger Analysis Methods Overall Heat Transfer Coefficient fouling, enhanced surfaces LMTD Method Effectiveness-NTU Method Outline

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Page 1: Lecture10_HeatExchangers

1

(1) Heat Exchanger Types(2) Heat Exchanger Analysis

MethodsOverall Heat Transfer Coefficient

fouling, enhanced surfacesLMTD Method Effectiveness-NTU Method

Outline

Page 2: Lecture10_HeatExchangers

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HX Classifications

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HX Classifications

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Concentric tube (double piped)Heat Exchanger Types

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Concentric tube (double piped) One pipe is placed concentrically within

the diameter of a larger pipe Parallel flow versus counter flow

Heat Exchanger Types

Fluid AFluid B

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Shell and TubeHeat Exchanger Types

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Compact Heat Exchangers

Heat Exchanger Types

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Cross Flow finned versus unfinned mixed versus unmixed

Heat Exchanger Types

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Heat Exchanger Types

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Heat Exchanger Types

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Heat Exchanger Analysis

Overall Heat Transfer Coefficient LMTD Effectiveness-NTU

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Overall Heat Transfer Coefficient

hoho

hfw

co

cf

co hAAR

RA

RhAUA )(

1)()()(

11 ,,

The overall coefficient is used to analyze heat ex-changers. It contains the effect of hot and cold side convection, conduction as well as fouling and fins.

factor fouling fR

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Enhanced Surfaces

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Log-Mean Temperature DifferenceTo relate the total heat transfer rate to inlet and outlet fluid temperatures. Apply energy balance:

Page 15: Lecture10_HeatExchangers

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Log-Mean Temperature DifferenceWe can also relate the total heat transfer rate to the temperature difference between the hot and cold fluids.

LM

ch

TUAQTTTlet

.

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The log mean temperature difference depends on the heat exchanger configuration

Th,in

Th,out

Th,in

Tc,in

Th,out

Tc,in

Tc,out

Tc,out

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LMTD Parallel-Flow HX

ocohch

icihch

LMLM

TTTTT

TTTTT

TTTTTTUAQ

,,2,2,2

,,1,1,1

)12

12

:Flow Parallelfor Where

/ln(

Page 18: Lecture10_HeatExchangers

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LMTD Counter-Flow HX

icohch

ocihch

LMLM

TTTTT

TTTTT

TTTT

TTUAQ

,,2,2,2

,,1,1,1

)12

12

:FlowCounter for Where

/ln(

Tlm,CF > Tlm,PF FOR SAME U: ACF < APF

Page 19: Lecture10_HeatExchangers

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LMTD- Multi-Pass and Cross-Flow

CFLMLMLM TFTTUAQ , Apply a correction factor to obtain LMTD

t: Tube Side

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LMTD MethodSizing a Heat Exchanger: Calculate Q and the unknown outlet

temperature. Calculate DTlm and obtain the correction

factor (F) if necessary Calculate the overall heat transfer

coefficient. Determine A.The LMTD method is not as easy to use for

performance analysis….

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The Effectiveness-NTU Method Define Qmax

for Cc < Ch Qmax = Cc(Th,i - Tc,i)for Ch < Cc Qmax = Ch(Th,i - Tc,i)

or Qmax = Cmin(Th,i - Tc,i)

Q = Cmin(Th,i - Tc,i)

)()(

)()(

,,min

,,

,,min

,,

max icih

icocc

icih

ohihh

TTCTTC

TTCTTC

qq

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The Effectiveness-NTU Method

For any heat exchanger: f(NTU,Cmin/Cmax)

NTU (number of transfer units) designates the nondimensional heat transfer size of the heat exchanger:

minCUANTU

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The Effectiveness-NTU Method

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The Effectiveness-NTU Method

PERFORMANCE ANALYSIS Calculate the capacity ratio Cr = Cmin/Cmax and

NTU = UA/Cmin from input data Determine the effectiveness from the

appropriate charts or -NTU equations for the given heat exchanger and specified flow arrangement.

When is known, calculate the total heat transfer rate

Calculate the outlet temperature.

Page 25: Lecture10_HeatExchangers

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The Effectiveness-NTU MethodSIZING ANALYSIS When the outlet and inlet temperatures are

known, calculate Calculate the capacity ratio Cr = Cmin/Cmax Calculate the overall heat transfer coefficient,

U When and C and the flow arrangement are

known, determine NTU from the -NTU equations.

When NTU is known, calculate the total heat transfer surface area.

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The Homework