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Condensate & Feedwater U-Tube Heat Exchangers

Boiler House Heat Recovery

Condensate returning from process users carries substantial heat and is already treated, which makes recovering both the water and its energy the single best economic move available in most steam plants. You avoid the make-up water cost, the treatment chemical cost and the fuel to reheat it, all at once.

Feedwater preheating raises boiler efficiency directly. Every degree added before the boiler is a degree the boiler does not have to add. High-pressure feedwater heaters in power generation are among the most demanding U-tube applications built, and they are classic DEU territory: a D-type front head closure for tube-side pressure beyond what a bolted bonnet holds economically, behind a bundle with no rear pressure joint at all.

Blowdown recovery is the item most often omitted. Continuous blowdown carries heat away by design, and it does so continuously. A small exchanger recovering that heat into make-up water typically pays back in months. The reason it gets left out is not economics; it is that nobody put it on the drawing.

Flash steam is part of the design, not an afterthought. Hot condensate and blowdown released to a lower pressure flash into steam. Ignoring that produces an exchanger sized for a liquid stream that is partly vapor in practice. The usual arrangement is a flash vessel recovering low-pressure steam first, with the remaining liquid passing through the heat exchanger, and sizing the exchanger for the liquid that actually reaches it is what makes the numbers work.

Oxygen control matters as much as heat recovery. Recovered condensate that picks up air on its way back becomes a corrosion problem in the boiler rather than an asset. Closed recovery systems, properly vented deaeration and attention to where the return line can draw air are all part of doing this properly.

Thermal cycling is constant. Boiler house exchangers follow plant steam demand, which means they cycle for their whole service life. A U-tube bundle absorbs that without an expansion joint, which is a large part of why the geometry dominates the application.

Related pages: steam-to-water heating, DEU high-pressure exchangers, high-pressure U-tube construction and clean steam generation.



condensate and feedwater u-tube heat exchanger diagram showing flash vessel, feedwater heater and blowdown recovery

Hot condensate and blowdown flash when released to lower pressure. Recover the low-pressure steam first, then size the exchanger for the liquid that actually reaches it.

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high pressure u-tube heat exchanger with heavy forged channel and thick tubesheet
High Pressure:
Fewest Sealed Joints
  • No rear head joint
  • Heavy tubesheet
  • Hydro tested
carbon steel industrial u-tube heat exchanger with saddle supports and davit arm
Industrial:
ASME Code Stamped
  • TEMA R, B or C
  • Carbon steel to alloy
  • Shells to 48 inches
custom engineered u-tube heat exchanger built to specified process conditions
Custom Build:
Rated To Your Duty
  • Any alloy or code
  • Applied nozzle loads
  • Accessories designed in

Condensate & Feedwater

Common FAQs

Because it is hot and already treated. Recovering it saves the heat, the make-up water and the chemical treatment for that volume simultaneously. In most steam plants it is the highest-return heat recovery available and the first thing worth doing.

An exchanger that raises boiler feedwater temperature before it enters the boiler, using steam or recovered heat. Higher feedwater temperature means less fuel to reach steam conditions. High-pressure versions in power plants are among the most demanding U-tube applications built.

On any boiler with continuous blowdown, usually yes, with payback often measured in months. The heat is being discarded by design, the exchanger is small, and the recovered energy goes straight into make-up water. It is omitted more often through oversight than through economics.

Because hot condensate released to lower pressure partly becomes vapor. An exchanger sized as though the whole stream were liquid will be wrong. The usual arrangement recovers low-pressure flash steam in a vessel first and sizes the exchanger for the remaining liquid.

Two reasons. These exchangers cycle continuously with plant steam demand, and a U-bundle absorbs that without an expansion joint. And on high-pressure feedwater duty the absence of a rear pressure-boundary joint is a real cost and reliability advantage.

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