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ChemicalHeat TransfereasyFE ExamCourseworkPE / Advanced

Required Heat Exchanger Area

A heat exchanger must transfer Q=500 kWQ = 500\ \text{kW}.

The overall heat transfer coefficient is U=800 W/m2KU = 800\ \text{W/m}^2\text{K} and the log mean temperature difference is 40 K40\ \text{K}.

Find the required heat transfer area.

Given
Q500 kWHeat duty
U800 W/m^2*KOverall heat transfer coefficient
LMTD40 KLog mean temperature difference
Hint 1

The exchanger design equation relates duty, coefficient, area, and temperature driving force.

Hint 2

A = Q/(U·ΔT_lm).

Hint 3

Check units: U is in W/m²K, so Q must be in W.

Worked solution — try the problem first

The design equation for an exchanger:

Q=UAΔTlmA=QUΔTlmQ = UA\,\Delta T_{lm} \quad\Longrightarrow\quad A = \frac{Q}{U\Delta T_{lm}}

Convert the duty to watts to match UU:

Q=500 kW=500,000 WQ = 500\ \text{kW} = 500{,}000\ \text{W}

A=500,000800×40=500,00032,000=15.6 m2A = \frac{500{,}000}{800 \times 40} = \frac{500{,}000}{32{,}000} = 15.6\ \text{m}^2

A=15.6 m2\boxed{A = 15.6\ \text{m}^2}

In practice you would add margin for fouling. Over time, deposits add thermal resistance and reduce the effective UU, so exchangers are commonly oversized by 10-25%, or specified with a fouling factor built into UU.

Note the LMTD is given here. In a real design you would compute it from the four terminal temperatures, and apply a correction factor FF for shell-and-tube geometries that are neither pure counterflow nor pure parallel flow: Q=UAFΔTlmQ = UAF\Delta T_{lm}.

Concepts:Heat exchanger designOverall heat transfer coefficientLMTD

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