ChemEngPro
Results-driven process engineer with many years in designing, commissioning, and operating pilot plants and R&D scale-up technologies. Provided engineering services to projects in the petrochemical, clean-tech, pulp and paper, and plastics industries. Skilled in performing simulations and designing equipment, creating P&IDs, PFDs, cause and effect matrices, control narratives, mass and energy balances, and conducting hydraulic and ASPEN modeling analysis.
Passionate about teaching chemical engineering and bridging the gap between Academia and real life through solving real-life case studies with students.
What’s on a P&ID? Pipes vs Tubes, Equipment, Instruments & Signals Explained
P&ID Anatomy Explained | How to Read & Understand Piping and Instrumentation Diagrams
Pump Performance Curves Explained | Efficiency, NPSHr & Power Curves
Pump Curves & Operating Point Explained | Centrifugal vs Positive Displacement
Pump Data Sheets Explained: Overview Guide + Free Templates
Code vs Standard: What’s the Difference? (ASME/API Explained for Engineers)
Pressure Relief Valves vs Burst Discs | Reclosing vs Non-Reclosing Devices Explained
What Makes an Ideal Safety Relief Valve? Objectives, Design Traits & API/ASME Requirements
Safety Valve vs Relief Valve vs Safety Relief Valve — API Definitions Explained Simply
Why Pressure Relief Valves Are Mandatory — What Most Engineers Overlook
Friction Head Loss Explained | Darcy Equation & Resistance Coefficient for Piping Systems
Compressible vs Incompressible Fluids | Why It Matters in Pump and Piping Design
Cavitation and Flashing in Valves
Installed Valve Characteristic Curve
Pump hydraulic horse power, brake horse power, motor power and efficiency
Orifice Plate Design
Flow Coefficient (Cv) Explained: How to Size Valves & Convert Cv to Resistance Coefficient (K)
Bernoulli Equation Explained Simply: Total Fluid Energy in Piping Systems