Finned Tube Heat Exchanger
Helical, L-foot or extruded fin geometries match the gas-side film coefficient — used in air coolers, economizers and waste-heat recovery.

Helical, L-foot or extruded fin geometries match the gas-side film coefficient — used in air coolers, economizers and waste-heat recovery.
- Air coolers
- Economizers
- Flue-gas heat recovery
- · Plate / tube material
- · Design pressure & temperature
- · Connection type and size
- · Code and certification
Finned Tube Heat Exchanger Overview
Short answer
A finned tube heat exchanger adds extended surface to the gas side of tubes for air-to-liquid or gas-to-liquid heat transfer. It is used in air coolers, economizers, HVAC coils and suitable exhaust-gas waste-heat recovery duties when gas-side heat transfer controls the required area. As a finned tube heat exchanger manufacturer, Shanghai Jiangxing selects the tube circuit, fin geometry, pitch, materials and casing from the confirmed fluids, temperatures, fouling risk, pressure-drop allowance and cleaning method.
A finned tube heat exchanger places fins on the gas-facing side of a tube circuit to increase available surface where air or process gas has the lower film coefficient. The liquid, refrigerant or condensing medium normally flows inside the tubes, while ambient air, flue gas or process gas passes across the fins.
Air-cooled heat exchangers reject process heat without a cooling-water circuit; economizers recover heat from boiler or engine exhaust; HVAC coils heat, cool or dehumidify air; and gas-to-liquid units recover or reject heat between a process gas and a tube-side fluid. The same construction is not automatically suitable for every gas stream.
Fin pitch, fin geometry, tube arrangement and cleaning access are selected together. Cleaner gas can accept closer spacing, while dust, fibres, sticky deposits or condensate may require wider passages, a plain-tube section or another construction. Attachment method and materials must also suit the confirmed gas composition, temperatures and environmental exposure.
For exhaust-gas heat recovery, gas composition, dew point, dust loading and allowable gas-side pressure drop are primary design inputs. If deposits can bridge the fins or corrosive condensate can form at the fin root, maintainability and corrosion risk take priority over compact surface density.
Operating Conditions
| Tube-side design pressure | Project-specific; confirmed from the tube material, wall thickness, headers and applicable design requirements |
| Design temperature | Project-specific; confirmed from the tube alloy, fin attachment, gas composition and operating conditions |
| Gas-side velocity | Selected against the allowable pressure drop, fouling behaviour and acoustic requirements |
| Construction | Air-cooled bundles, finned-tube coils, economizer panels |
Materials of Construction
| Tubes | Carbon steel, stainless, copper, copper-nickel, titanium |
| Fins | Aluminum (1050/1100), carbon steel, stainless, copper |
| Fin attachment | Wrap-on tension, L-foot, embedded G-fin, extruded bi-metallic, welded serrated |
| Casing | Carbon steel painted, galvanized, or stainless for corrosive ambient |
Choose this when / Do not choose this when
A quick suitability check before you commit to a construction.
Choose this construction when
- One side is ambient air or process gas and the gas-side film controls the required area
- The duty is an air cooler, economizer, HVAC coil or exhaust-gas heat recovery service
- Cooling-water use should be avoided and ambient conditions support air cooling
- Gas composition, dust loading, dew point and pressure-drop allowance are available for selection
Do not choose this construction when
- The gas carries sticky, fibrous or heavy particulate that would bridge the fin passages
- Condensation below the acid dew point cannot be prevented or accommodated by the selected materials
- The available gas-side pressure drop is too low for a practical finned bundle
- The duty is liquid-to-liquid, where extended gas-side surface adds no selection benefit
Selection Parameters
Information our engineering team uses to size and quote this unit.
- Gas composition, dust loading and dew point
- Tube-side fluid, pressure, temperature and duty
- Ambient design temperature and altitude
- Allowable footprint and noise level
- Required materials (carbon, stainless, bi-metallic) based on gas chemistry and temperature
RFQ Data Checklist
Send the items below with your inquiry for the fastest accurate quotation.
- Gas analysis (composition, dust loading, sulphur content, dew point, mass flow)
- Gas inlet temperature and required gas outlet temperature
- Allowable gas-side pressure drop and available draft or fan power
- Tube-side fluid and full process data
- Inlet/outlet temperatures and required duty
- Site ambient conditions and altitude
- Footprint, duct interface, noise and power constraints
- Expected fouling, planned cleaning method and access
- Materials and fin geometry preferences
Procurement and selection dimensions
The dimensions that decide the configuration, and what each one changes in the quotation.
Sets duty, corrosion risk and the safe outlet-temperature target
Sets fin pitch and whether a finned or plain-tube section is appropriate
Sets tube circuit, rows and heat transfer area
Sets attachment method, pitch and maintainability; confirmed per project
Sets air volume, fan duty and bundle arrangement for air-cooled service
Sets tube, fin and casing materials after engineering review
Finned Tube Heat Exchanger Industry Applications
Recovers sensible heat from flue gas into feedwater or another tube-side fluid. Fin spacing, materials and cleaning access are selected from gas composition, dust and dew point.
Rejects heat from oil, water or another process fluid to ambient air where cooling-water use is limited or undesirable. Ambient conditions, fan duty and noise constraints are selection inputs.
Transfers suitable engine, turbine or process-exhaust heat to a liquid circuit. The gas analysis, pressure-drop allowance, condensate risk and maintenance plan determine whether fins are appropriate.
Transfers heat between an air stream and a tube-side water, glycol or refrigerant circuit. Coil geometry is selected from duty, air conditions, condensate handling and available space.
Finned Tube vs Plain-Tube Gas Heat Exchanger
Extended surface is valuable when the gas-side film limits heat transfer, but it must remain cleanable. A plain-tube section can be the safer choice for dirty, sticky or condensing gas streams.
| Finned Tube | Plain Tube | |
|---|---|---|
| Best-fit gas | Clean to moderately dusty air or process gas | Dirty, sticky, fibrous or condensing gas where deposits must be removed |
| Surface area | Extended gas-side surface in a compact bundle | Lower surface density; usually needs a larger bundle |
| Pressure drop | Fin pitch and rows must fit the available gas-side allowance | More open passage can reduce blockage risk |
| Cleaning | Requires access matched to fin pitch and deposit type | More direct access to the tube surface |
| Selection basis | Gas analysis, dew point, dust loading and duty | Fouling severity and cleaning access can outweigh compactness |
Frequently Asked Questions
Related industries
Other products
Related Guides
Sourcing, verification and next steps
Every unit is engineered to the confirmed duty, materials and inspection scope of the order. Design codes, test certificates and third-party inspection are quoted as options and confirmed per project rather than assumed. See our heat exchanger manufacturing and OEM capability, the quality control and inspection workflow, and the heat exchanger cost guide for what drives price. For a first-pass thermal check, use the heat exchanger sizing calculator, then send your process data for a quotation.
Need a Heat Exchanger for Your Project?
Send your working conditions, drawing or datasheet. Blair will review your request and help confirm the next step.