What to do when Your Heat Exchanger is fail?
A lack of effective cooling due to heat exchanger failure can
cause production losses and unplanned downtime. Fortunately, two common causes
of exchanger loss — mechanical failures and chemically induced corrosion — can
be prevented.
Heat exchangers are used in many critical processes to protect
other valuable manufacturing equipment, optimise energy consumption and reduce
associated operating costs. A properly selected, installed and maintained heat
exchanger can help enhance the reliability and efficiency of a fluid system.
When a heat exchanger fails, however, it can lead to costly downtime.
Speaking of Heat Exchangers, specialised boiler tubes are utilised
in the proper functioning of such exchangers. SA179tube Is one leading
Manufacturer, Supplier & Stockist Of A334 & SA334 Pipes
& Tubes.
Two common types of heat exchanger failure — both of which can
be prevented — are:
· Mechanical failures, including steam or water hammer, thermal
fatigue and freeze up.
· Chemically induced corrosion, resulting from a chemical interaction with circulating fluids.
This article will review the operational problems that can develop in a shell-and-tube type heat exchanger and describe the corrective actions that can be taken in order to prevent such problems.
Metal Erosion
Excessive fluid velocity on either the shell or tube side of the
heat exchanger can cause damaging erosion as the tubing metal wears. If
corrosion is already present, it can be accelerated. Erosion has the potential
to remove the tube material’s protective film, exposing fresh metal to further
attack.
Areas most prone to erosion are the U-bend of U-type heat
exchangers and the tube entrances of all shell-and-tube heat exchangers.
Tube-entrance areas can experience material loss when excessive, high velocity
fluid from a nozzle is divided into many smaller streams as it enters the heat
exchanger. When excessive velocity occurs at the entrance area of tubes, it
typically produces a horseshoe-shaped erosion pattern.
Several steps can be taken to minimise the risk of metal
erosion. The maximum recommended velocity in the tubes and entrance nozzle is a
function of many variables, including tube material, fluid handling and
temperature. Materials such as steel, stainless steel, and copper-nickel
withstand higher tube velocities than copper (table 1). Where practical,
staying below these velocities will help minimise metal erosion.
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