Heat Exchanger Principles and Designs
Classified in Physics
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Fundamental Heat Exchanger Concepts
Key Formulas in Heat Transfer
- Heat Exchanged (q): q = m · Cp · ΔT (Heat absorbed or released by a fluid)
- Heat Transfer Rate (Q): Q = U · A · ΔT (Overall heat transfer rate through an exchanger)
- Energy Balance for Heat Exchangers: Mc · Cpc · (ΔTc) = Mf · Cpf · (ΔTf) (Heat gained by cold fluid equals heat lost by hot fluid)
- Other Formulas (Context Dependent): ct = w1 + w2 · PC1 · CP2
Definition of a Heat Exchanger
A heat exchanger is a device designed to efficiently transfer heat from one fluid to another. Common examples include:
- Condenser: Transfers heat from a hot fluid to a colder one, causing the hot fluid to condense (e.g., steam to water).
- Evaporator: Transfers heat to a cold fluid, causing it to evaporate (e.g., refrigerant to vapor).
Heat Exchanger Flow Configurations
- Parallel Flow: Both internal and external fluids flow in the same direction.
Countercurrent Flow: Fluids flow in opposite directions. This configuration is generally more efficient, allowing for a greater temperature change in the fluids.
- Cross Flow: One fluid flows perpendicular to the other. This configuration is typically used when there is no phase change.
- Single Pass / Multi-Pass:
- Single Pass: Heat is exchanged only once as fluids flow through the exchanger.
- Multi-Pass: Fluids exchange heat multiple times by flowing through several sections or passes within the exchanger.
Specialized Heat Exchanger Types
- Regenerative Heat Exchanger: A process where heat is transferred to a heat storage medium (regenerator) during one part of a cycle, and then transferred back from the medium to another fluid during a different part of the cycle.
- Rotary Regenerator: A type of regenerative heat exchanger where a warm fluid passes through a rotating matrix, followed by a cold fluid, alternating with minimal mixing between the two fluid streams.
- Direct Contact Heat Exchangers: Devices where fluids directly contact each other for heat transfer (e.g., condenser trays).
Common Tubular Heat Exchanger Designs
Double Pipe Heat Exchangers
Consist of two concentric pipes. The inner tube carries the cold fluid, absorbing heat, while the outer annulus carries the warm fluid, losing heat. They offer good performance but are limited in capacity.
Spiral Tube Heat Exchangers
Feature an internal spiral design. These often require high fluid pressure due to significant pressure drop.
Shell and Tube Heat Exchangers
Designed for high pressures and clean industrial fluids. A shell contains a bundle of fixed tubes. Common configurations include 1-2 pass and 2-4 pass designs (referring to TEMA designations).
Shell and Tube Naming Convention (TEMA Type Example)
Components often referenced in naming include:
- Shell internal diameter
- Tube length
- Front head type
- Shell type
- Rear head type
Plate Heat Exchangers
Composed of multiple thin, corrugated plates pressed tightly together. Hot fluid passes through one channel, and cold fluid through an adjacent one, without mixing. They are suitable for cooling/heating fibrous products or for applications like milk pasteurization.
Free-Flow Plate Heat Exchangers
A variant designed for viscous fluids or those with particles, characterized by no metallic contact between plates. Specific examples might refer to dimensions like D=2 and L=5.
Spiral Heat Exchangers
Consist of two concentric spirals welded together, forming two channels for fluid flow and heat transfer. Advantages include self-cleaning capabilities, easy access for maintenance, and a compact design.
Graphite Heat Exchangers
Fluids circulate through holes within a compact block of graphite, offering excellent corrosion resistance.
Plate vs. Shell and Tube Heat Exchangers: A Comparison
Feature | Plate Heat Exchangers | Shell and Tube Heat Exchangers |
---|---|---|
Fouling Resistance | Less prone to fouling due to high turbulence and absence of dead zones. | Can be more prone to fouling in certain areas. |
Flexibility & Cleaning | Flexible design, easy to clean and adjust. | Less flexible, cleaning can be more complex. |
Compactness | Very compact design. | Generally larger footprint for similar capacity. |
Operating Limits | Limited by temperature (typically up to 300°C) and pressure (around 20 Atm) due to gaskets. | Can operate at much higher temperatures and pressures. |
Leak Risk | Higher risk of external leaks due to multiple gaskets. Safety valves are crucial. | Lower risk of external leaks, but internal leaks can be harder to detect. |