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October 13, 2026

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heat exchanger maintenance

Fouling deposits inside a shell and tube heat exchanger
PPI October 6, 2026 0

Fouling in Heat Exchangers – Why Design Assumptions Fail in Practice

A shell-and-tube heat exchanger may leave the factory in perfect condition, delivering the exact heat duty predicted during design. Yet, over time, many exchangers gradually lose efficiency, consume more energy,…

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Maintenance-friendly shell and tube heat exchanger design
PPI September 27, 2026 0

Designing for Maintenance Begins Before the Exchanger Is Built

A shell-and-tube heat exchanger spends most of its life in operation, but its true maintainability is determined long before it is commissioned. Decisions made during the design stage—such as exchanger…

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Comparison of TEMA front head types A, B, and C in shell and tube heat exchangers showing construction and maintenance access
PPI July 16, 2026 0

TEMA Front Head Types (A, B, C) Explained

The Front Head Determines How the Process Fluid Enters, Leaves, and Can Be Maintained When engineers first learn about TEMA classifications, they usually notice designations such as: Most people immediately…

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Comparison showing fouling deposits vs corrosion metal damage inside heat exchanger tubes
PPI April 12, 2026 0

Fouling vs Corrosion – Why They Are Often Confused – Two Different Problems That Produce Similar Symptoms

In operating plants, performance loss in heat exchangers is frequently described with a single word: “corrosion.” In many cases, the real cause is fouling. The confusion between fouling and corrosion…

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Recent Posts

  • How Exchanger Fouling Silently Reduces Duty & Increases Cost
  • Why Designers Add Fouling Margin in Exchangers
  • Fouling Factor in Heat Exchanger Design – What It Really Represents
  • Fouling in Heat Exchangers – Why Design Assumptions Fail in Practice
  • What Process Engineers Should Check Before Approving a Heat Exchanger Vendor Drawing

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