Pipeline Surge Relief Design Considerations: Valves, Tanks, and Pumps
The Phenomenon That Can Destroy a Pipeline in Milliseconds Water hammer is one of the…
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How to select the Right Tower Tray for Fouling Services?
Distillation and fractionation columns are critical equipment in refining and petrochemical facilities. While tower operation…
PSV Sizing Guide: How to Calculate the Backpressure Correction Factor (Kb)
Pressure Safety Valves (PSVs) are the final line of defense against catastrophic overpressure events. While a PSV’s…
Critical Role of Safety Shutdown Interlocks in Equipment Protection
As process engineers, we design equipment, piping, and other plant components to operate within the…
Tank Inbreathing, Outbreathing & Venting Requirements in API 2000
Introduction Proper venting of atmospheric and low-pressure storage tanks is critical to prevent tank damage…
Understand the Basis to Select Proper Storage Tank Type
When storage tanks are mentioned, most people think about typical fixed storage tanks. However, things…
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P&ID Considerations
P&ID Preparation details and Common Practices.
Heat Exchanger Sizing
Best practices for sizing a shell & tube exchanger using HTRI.
Vessel & Separator Sizing
Sizing 2 phase and 3 phase separators based on surge time and separation criteria.
Pump Hydraulics
Understand pump operation and perform pump sizing.
Pipe Sizing
Understand how to choose the proper line size for various services and the criteria used for that.
PSV and Relief
Understand PSV opening scenarios and relief systems.
Compressor Operation
What is in compressors for process engineers.
Control Valve Hydraulics
Understand control valve operation and perform control valve sizing.
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