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September 11, 2026

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Thermal Design

Pressure drop versus heat transfer trade-off in a shell-and-tube heat exchanger
PPI September 3, 2026 0

Pressure Drop vs Heat Transfer – The Real Design Trade-Off

Every heat exchanger designer faces the same engineering challenge: improving heat transfer almost always increases pressure drop, while reducing pressure drop usually weakens heat transfer. The objective is not to…

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Effect of baffles on shell-side pressure drop in a shell-and-tube heat exchanger
PPI August 30, 2026 0

Effect of Baffles on Shell-Side Pressure Drop

Baffles are among the most important internal components of a shell-and-tube heat exchanger. They improve shell-side heat transfer by directing fluid across the tube bundle, but they also create additional…

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Common thermal design misjudgements that affect heat exchanger performance
PPI August 20, 2026 0

Common Thermal Design Misjudgements in Heat Exchangers

Most heat exchanger thermal design problems do not arise because engineers cannot perform the calculations. They arise because perfectly correct calculations are applied with incorrect assumptions, unrealistic expectations, or incomplete…

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Heat exchanger thermal design margin balancing operating flexibility and lifecycle cost
PPI August 18, 2026 0

Design Margin in Heat Exchanger Thermal Calculations

A design margin is not extra safety built into a heat exchanger for the sake of caution. It is a carefully considered allowance that helps the exchanger continue meeting process…

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Heat exchanger thermal design failure due to fouling and changing plant conditions
PPI August 16, 2026 0

Why Exchanger Thermal Designs Fail in Operating Plants

A heat exchanger can satisfy every thermal calculation during design and still fail to achieve the required performance after commissioning. The reason is usually not a mistake in the equations—it…

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Overall heat transfer coefficient U in shell and tube heat exchanger thermal design
PPI August 13, 2026 0

How Engineers Use U in Heat Exchanger Design (Not Textbook U)

The Overall Heat Transfer Coefficient (U) is one of the most important parameters in heat exchanger design, yet experienced engineers rarely treat it as a fixed value from a handbook.…

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LMTD correction factor Ft for shell and tube heat exchanger thermal design
PPI August 11, 2026 0

Heat Exchanger Correction Factor (F) – Why It Exists in Exchanger Design

Real heat exchangers rarely operate under ideal counterflow conditions. The correction factor exists because practical exchanger flow arrangements behave differently from the textbook assumptions used in LMTD calculations. Why Isn’t…

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LMTD temperature driving force in shell and tube heat exchanger thermal design
PPI August 9, 2026 0

Why Temperature Difference Drives Heat Transfer

Heat Always Needs a Driving Force Heat naturally flows from a higher temperature to a lower temperature. Without a temperature difference: The larger the temperature difference, the easier it becomes…

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Heat exchanger duty calculation using flow rate specific heat and temperature difference in industrial thermal design
PPI August 6, 2026 0

Heat Exchanger Duty Calculation – Practical Assumptions

Every Heat Duty Calculation Begins with Equations but Ends with Engineering Judgment One of the first calculations every process engineer learns is the heat exchanger duty equation: Q = m…

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Engineering workflow showing heat exchanger thermal design from process datasheet to operating plant
PPI August 4, 2026 0

Heat Exchanger Thermal Design in Practice – From Datasheet to Reality

Why a Thermally Correct Heat Exchanger on Paper May Still Underperform in a Real Plant Heat exchanger thermal design is often viewed as a calculation exercise. An engineer receives a…

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Recent Posts

  • Field Symptoms of Excess Pressure Drop in Heat Exchangers
  • Pressure Drop Challenges During Plant Revamp
  • Hydraulic Design Errors Engineers Make in Heat Exchanger Design
  • Pressure Drop vs Heat Transfer – The Real Design Trade-Off
  • Velocity Limits in Heat Exchangers – Erosion vs Performance

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