Training Heat Exchangers — LMTD Method Heat Exchanger Types and the Energy Balance
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Heat Exchanger Types and the Energy Balance

24 min Heat Exchangers — LMTD Method

Heat Exchanger Types and the Energy Balance

Heat exchangers transfer thermal energy between two fluids. They appear in HVAC systems, power plants, chemical processes, engines, and refrigeration. The fundamental design equation links heat duty, area, and temperature difference.

Common Heat Exchanger Types

Double-pipe (concentric tube): One fluid inside, one in the annulus. Simplest type. Parallel-flow or counter-flow.
Shell-and-tube: Tubes bundled inside a shell. Baffles direct shell-side flow. 1, 2, or 4 tube passes.
Cross-flow: Fluids flow perpendicular. Common in finned-tube radiators, HVAC coils.
Plate (compact): Stacked corrugated plates. High area-to-volume ratio.

Energy Balance

At steady state, heat lost by the hot fluid equals heat gained by the cold fluid (no losses):

$$\dot{Q} = \dot{m}_h c_{p,h}(T_{h,\text{in}} - T_{h,\text{out}}) = \dot{m}_c c_{p,c}(T_{c,\text{out}} - T_{c,\text{in}})$$

We often define the capacity rate: $C = \dot{m}c_p$ (W/K), so $\dot{Q} = C_h \Delta T_h = C_c \Delta T_c$.

Overall Heat Transfer Coefficient

$$\frac{1}{UA} = \frac{1}{h_i A_i} + R''_{f,i}\frac{1}{A_i} + \frac{\ln(D_o/D_i)}{2\pi k L} + R''_{f,o}\frac{1}{A_o} + \frac{1}{h_o A_o}$$

For thin-walled tubes ($A_i \approx A_o$): $\frac{1}{U} = \frac{1}{h_i} + R''_f + \frac{1}{h_o}$

Typical $U$ values (W/(m²·K)): Water-to-water: 850–1700 • Steam-to-water: 1000–6000 • Gas-to-gas: 10–40

Example 1 — Energy Balance

Hot water ($\dot{m} = 2$ kg/s, $c_p = 4180$) cools from 90°C to 60°C. Cold water ($\dot{m} = 3$ kg/s, $c_p = 4180$) enters at 20°C. Find $\dot{Q}$ and $T_{c,\text{out}}$.

$\dot{Q} = 2 \times 4180 \times (90 - 60) = 250{,}800$ W = 250.8 kW

$T_{c,\text{out}} = 20 + \frac{250{,}800}{3 \times 4180} = 20 + 20 = 40$°C

Example 2 — Overall U

Inner convection $h_i = 3000$ W/(m²·K), outer $h_o = 500$. No fouling, thin wall. Find $U$.

$\frac{1}{U} = \frac{1}{3000} + \frac{1}{500} = 0.000333 + 0.002 = 0.002333$

$U = 429$ W/(m²·K)

The outer (lower) coefficient dominates — this is common when one fluid is gas and the other is liquid.

Example 3 — Capacity Rates

Oil ($\dot{m} = 1.5$ kg/s, $c_p = 2100$) is cooled by water ($\dot{m} = 2$ kg/s, $c_p = 4180$). Which is $C_{\min}$?

$C_h = 1.5 \times 2100 = 3150$ W/K (oil)

$C_c = 2 \times 4180 = 8360$ W/K (water)

$C_{\min} = 3150$ W/K (oil side). The fluid with $C_{\min}$ experiences the larger temperature change.

Practice Problems

1. Steam condenses at 100°C, heating water from 15°C to 55°C at $\dot{m}_c = 4$ kg/s. Find $\dot{Q}$.
2. $h_i = 8000$, $h_o = 200$, no fouling. Find $U$. Which side controls?
3. Hot gas: $\dot{m} = 0.5$ kg/s, $c_p = 1050$. Cold air: $\dot{m} = 0.8$ kg/s, $c_p = 1005$. Which is $C_{\min}$?
4. $\dot{Q} = 100$ kW, $C_h = 5000$ W/K. Find the hot-side temperature drop.
5. What does a large $U$ value indicate about a heat exchanger?
6. $h_i = h_o = 1000$. Find $U$ (no fouling, thin wall).
Show Answer Key

1. $\dot{Q} = 4 \times 4180 \times 40 = 668{,}800$ W = 668.8 kW

2. $1/U = 1/8000 + 1/200 = 0.005125$. $U = 195$ W/(m²·K). Outer side controls.

3. $C_h = 525$ W/K, $C_c = 804$ W/K. $C_{\min} = 525$ (hot gas).

4. $\Delta T = 100{,}000/5000 = 20$°C

5. High $U$ means efficient heat transfer — typically liquid-to-liquid or phase change.

6. $U = 500$ W/(m²·K)