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When Heat Becomes the Enemy Sulphidation, Creep, and the Shutdown Crack in Refinery High-Temperature Exchangers
In the first two parts of this series, corrosion was driven by chemistry and by flow. In the refinery hot-exchanger, a third agent takes command — temperature itself. Above a few hundred degrees, steel stops being a passive bystander to its environment and begins to react with it: sulphur attacks it, hydrogen invades it, and under sustained load it slowly deforms and tears. And in a final irony, the most dangerous crack of all appears not while the exchanger is running hot, b

Paresh Haribhakti
5 hours ago6 min read


Heat Exchanger Failure Analysis: Why Condensers Corrode at the Inlet, Air Zone, and During Idle Periods
In Part 1 of this series I argued that a heat exchanger failure is rarely proportional to the size of the leaking tube. Nowhere is that truer than in the condenser. A condenser does not fail because the whole bundle is bad — it fails because a few tubes, in three very specific situations, see conditions the rest never do. Across the condenser investigations my teams have closed, the same three culprits recur: the inlet end that erodes, the air-removal zone that grooves, and t

Paresh Haribhakti
Jun 237 min read


When Chemistry Eats Steel
A Metallurgist’s Guide to Heat Exchanger Failures in the Chemical & Petrochemical Industry In more than four decades of looking down a microscope at why industrial equipment fails, I have come to regard the heat exchanger as the most under-appreciated component in any process plant. It rarely makes the front page when a unit trips. It carries neither the glamour of a reactor nor the visibility of a compressor. And yet, across the 500-plus heat exchanger investigations my team

Paresh Haribhakti
Jun 97 min read
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