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For a specified fluid pair, inlet temperatures, and mass flow rates, what kind of heat exchanger will have the highest effectiveness: double-pipe parallel- flow, double-pipe counterflow, crossflow, or multipass shell-and-tube heat exchanger?

Short Answer

Expert verified
Answer: The multipass shell-and-tube heat exchanger usually has the highest effectiveness for a specified fluid pair, inlet temperatures, and mass flow rates.

Step by step solution

01

Double-Pipe Parallel-Flow Heat Exchanger

In a double-pipe parallel-flow heat exchanger, the fluids flow in the same direction along the pipes, and heat transfer occurs between the two fluids. The performance tends to be limited as the temperatures equilibrate at lower effectiveness than other exchanger designs.
02

Double-Pipe Counterflow Heat Exchanger

In a double-pipe counterflow heat exchanger, the fluids flow opposite to each other, increasing the temperature difference along the heat exchanger and enhancing heat transfer between the two fluids. This design results in higher effectiveness compared to the parallel flow.
03

Crossflow Heat Exchanger

A crossflow heat exchanger is designed in such a way that the fluid streams flow perpendicular to each other resulting in a continuous temperature difference along the flow passages. This configuration is known for its compactness, and it can achieve relatively high effectiveness.
04

Multipass Shell-and-Tube Heat Exchanger

In a multipass shell-and-tube heat exchanger, fluid flow through tubes multiple times, changing direction after each pass. This design is intended to increase heat transfer effectiveness while maintaining a more compact design. The effectiveness of these heat exchangers is usually higher than that of the other three types and can be even optimized further.
05

Comparison and Conclusion

In summary, among double-pipe parallel-flow, double-pipe counterflow, crossflow, and multipass shell-and-tube heat exchangers, the multipass shell-and-tube heat exchanger usually has the highest effectiveness for a specified fluid pair, inlet temperatures, and mass flow rates. This is due to its design capabilities to increase heat transfer effectiveness while maintaining a more compact design compared to other configurations.

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Most popular questions from this chapter

A double-pipe parallel-flow heat exchanger is used to heat cold tap water with hot water. Hot water $\left(c_{p}=4.25 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( enters the tube at \)85^{\circ} \mathrm{C}$ at a rate of \(1.4 \mathrm{~kg} / \mathrm{s}\) and leaves at \(50^{\circ} \mathrm{C}\). The heat exchanger is not well insulated, and it is estimated that 3 percent of the heat given up by the hot fluid is lost from the heat exchanger. If the overall heat transfer coefficient and the surface area of the heat exchanger are \(1150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and $4 \mathrm{~m}^{2}$, respectively, determine the rate of heat transfer to the cold water and the log mean temperature difference for this heat exchanger.

A counterflow heat exchanger is used to cool oil $\left(c_{p}=2.20 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( from \)110^{\circ} \mathrm{C}\( to \)85^{\circ} \mathrm{C}\( at a rate of \)0.75\( \)\mathrm{kg} / \mathrm{s}\( with cold water \)\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)\( that enters the heat exchanger at \)20^{\circ} \mathrm{C}$ at a rate of \(0.6 \mathrm{~kg} / \mathrm{s}\). If the overall heat transfer coefficient is \(800 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), the heat transfer area of the heat exchanger is (a) \(0.745 \mathrm{~m}^{2}\) (b) \(0.760 \mathrm{~m}^{2}\) (c) \(0.775 \mathrm{~m}^{2}\) (d) \(0.790 \mathrm{~m}^{2}\) (e) \(0.805 \mathrm{~m}^{2}\)

Oil is being cooled from \(180^{\circ} \mathrm{F}\) to \(120^{\circ} \mathrm{F}\) in a oneshell and two-tube heat exchanger with an overall heat transfer coefficient of $40 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\(. Water \)\left(c_{p c}=1.0 \mathrm{Btu} / \mathrm{lbm} \cdot{ }^{\circ} \mathrm{F}\right)\( enters at \)80^{\circ} \mathrm{F}$ and exits at \(100^{\circ} \mathrm{F}\) with a mass flow rate of $20,000 \mathrm{lbm} / \mathrm{h}\(. Determine \)(a)\( the NTU value and \)(b)$ the surface area of the heat exchanger.

A heat exchanger is used to condense steam coming off the turbine of a steam power plant by cold water from a nearby lake. The cold water $\left(c_{p}=4.18 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\right)$ enters the condenser at \(16^{\circ} \mathrm{C}\) at a rate of \(42 \mathrm{~kg} / \mathrm{s}\) and leaves at \(25^{\circ} \mathrm{C}\), while the steam condenses at $45^{\circ} \mathrm{C}$. The condenser is not insulated, and it is estimated that heat at a rate of \(8 \mathrm{~kW}\) is lost from the condenser to the surrounding air. The rate at which the steam condenses is (a) \(0.228 \mathrm{~kg} / \mathrm{s}\) (b) \(0.318 \mathrm{~kg} / \mathrm{s}\) (c) \(0.426 \mathrm{~kg} / \mathrm{s}\) (d) \(0.525 \mathrm{~kg} / \mathrm{s}\) (e) \(0.663 \mathrm{~kg} / \mathrm{s}\)

Consider a heat exchanger that has an NTU of 4 . Someone proposes to double the size of the heat exchanger and thus double the NTU to 8 in order to increase the effectiveness of the heat exchanger and thus save energy. Would you support this proposal?

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