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Pressure Drop in Piping

Darcy’s Equation

Posted on September 25, 2009October 28, 2012

This equation, which is also sometimes called the Weisbach equation or the Darcy-Weisbach equation, states that the friction head loss between two points in a…

Pressure Relief

Pressure Relief Valves

Posted on September 25, 2009

The most important safety devices in a production facility are the pressure relief valves, which ensure that pipes, valves, fittings, and pressure vessels can never…

Gas Processing

Gas Stripping Service

Posted on May 27, 2013

For stripping service, as in a glycol or amine contactor , bubble cap trays are the most common. In recent years, there has been a…

Shell and Tube Exchangers

Heat Exchanger Types

Posted on September 14, 2009October 29, 2012

There are many different arrangements of the shells, tubes and baffles in heat exchangers. Figure 3-6 is a list of TEMA standard classifications for heat…

Water Treating Equipment

Settling Tanks and Skimmer Vessels

Posted on September 4, 2009October 31, 2012

The simplest form of primary treating equipment is a settling (skim) tank or vessel. These items are normally designed to provide long residence times during…

Heat Exchangers

Fired Heater Design

Posted on September 15, 2009October 29, 2012

Direct-fired combustion equipment is that in which the flame and/or products of combustion are used to achieve the desired result by radiation and convection. Common…

Basic Configuration

Water Treatment Process

Posted on August 21, 2009October 31, 2012

Water Treatment describes choosing a process for this subsystem, including vessel and open drains. Figure 2-13 shows an enlargement of the watertreating system for the…

Heat Transfer Theory

Oil Sensible Heat Duty

Posted on September 13, 2009October 29, 2012

The sensible heat duty for the oil phase is: where Q0 = oil flow rate, bpd SG = oil specific gravity C0 = oil specific…

Fractions from atmospheric and vacuum distillation

Refinery Gas and LPGs

Posted on September 26, 2009October 28, 2012

In many refineries most of theC4’s and lighter are removed from the atmospheric column overhead distillate in the first column of the light end unit.…

LTX Units and Line Heaters

LTX Wall Thickness Sizing

Posted on September 16, 2009October 28, 2012

Before choosing a wall thickness it is necessary to choose a pressure rating for the coil. Typically, the high-pressure coil (L1) is rated for the…

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Recent Posts

  • Filtration Techniques for Preventing Clogs in Low-Flow Coriolis MFCs
  • Understanding Bernoulli’s Equation with Friction in Process Engineering
  • Head Bernoulli Equation in Process Engineering
  • Separating Oil, Water, and Gas with Weir System Separators
  • Cyclone Separator Capacity

Categories

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  • Oil and Water Separation
  • Potential Operating Problem
  • Pressure Drop in Piping
  • Pressure Relief
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  • Relief Valve Sizing
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  • Three Phase Separator Sizing
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  • Two Phase Oil and Gas Separation
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  • Two Phase Separator Sizing
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  • Type Of Devices
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  • Water Treating Theory
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