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Economizer Lower Pressure Tube Bundle with Bare Tube

Views: 0     Author: Site Editor     Publish Time: 2025-06-30      Origin: Site


Economizer Lower Pressure Tube Bundle with Bare Tube


Economizer Lower Pressure Tube Bundle with Bare Tube


A lower pressure economizer tube bundle with bare tubes is a critical heat exchange component in boiler systems, designed to recover waste heat from low-temperature flue gases (typically in the tail section of boilers) to preheat feedwater. Unlike finned tubes, bare tubes (smooth, un-finned surfaces) are chosen for specific operating conditions where their unique properties align with performance and maintenance needs.


Core Design and Structure

Basic Configuration

Bare Tubes: Tubes with no external fins, relying on their inherent surface area for heat transfer. They are typically arranged in bundles (rows) to maximize contact with flue gases.


Tube Material:

Carbon steel (e.g., SA-178 Grade A): Cost-effective for low-pressure, low-corrosion environments (e.g., flue gas temperatures <250°C with low sulfur content).

Stainless steel (e.g., 304, 316): Used in corrosive conditions (e.g., high sulfur content in fuel, flue gas temperatures with acid dew point risk) to resist oxidation and acid attack.

Alloy steel (e.g., T22): For slightly higher pressure (up to 2.5 MPa) or moderate corrosion environments, balancing strength and cost.


Tube Dimensions:

Diameter: Typically 25–51 mm (1–2 inches). Smaller diameters (25–32 mm) enhance heat transfer via increased surface area per unit volume, while larger diameters (42–51 mm) reduce pressure drop for flue gases.

Wall thickness: 2–5 mm, determined by operating pressure (usually <2.5 MPa for lower pressure economizers) and corrosion/erosion allowances (0.5–1.5 mm).

Bundle Arrangement


Tube Layout:

Inline : Tubes arranged in straight rows (aligned horizontally/vertically). This minimizes pressure drop for flue gases but provides lower heat transfer efficiency due to reduced turbulence.

Staggered: Tubes offset in adjacent rows to create turbulent flow in flue gases, enhancing heat transfer (10–20% higher than inline) but increasing pressure drop.

Row Count: 2–10 rows, depending on heat recovery requirements. More rows increase heat transfer surface area but require larger space and higher pressure drop.



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