All Topics
Triple Effect Evaporator Design — Mass Balance, Steam Economy & BPE
Complete step-by-step TEE design guide — mass balance, boiling point elevation, heat transfer area sizing, vapour-liquid separator, and steam jet ejector. Plant-validated methods.
NPSH Explained — Available vs Required & How to Prevent Cavitation
Understand NPSHa and NPSHr, how to calculate them, and practical steps to prevent cavitation in centrifugal pumps in process plants.
Triple Effect Evaporator Design — Mass Balance, Steam Economy & BPE
Complete walkthrough of TEE design methodology including forward-feed mass balances, boiling point elevation corrections, and steam economy calculations.
Shell & Tube Heat Exchanger Sizing — LMTD Method with Worked Example
How to size a shell and tube heat exchanger using LMTD correction factor, overall heat transfer coefficient, and fouling resistances.
Distillation Column Design — McCabe-Thiele Method Step by Step
Number of theoretical stages, reflux ratio, feed tray location, and tray efficiency — all explained with a binary distillation worked example.
CSTR vs PFR — When to Use Which Reactor & How to Size Them
Comparison of continuous stirred tank and plug flow reactors, Damköhler number, space time, and volume calculations with design equations.
Industrial Pipe Sizing — Velocity, Pressure Drop & Schedule Selection
How to select pipe diameter, schedule, and material for process lines. Covers recommended velocities, Darcy-Weisbach pressure drop, and ANSI B36.10/B36.19 schedules.
Steam Jet Ejector Design — HEI Standards, Air Leakage & SSC
Design of single and multi-stage steam ejectors for vacuum systems. HEI air leakage estimation, steam specific consumption from charts, and motive steam sizing.