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LTX Units and Line Heaters

LTX Unit Condensate Stabilizer

Posted on May 27, 2013

It should be clear from the description of LTX units that the lower pressure separator in an LTX unit is a simple form of cold-feed…

Pressure Relief

Relief Valve Installation

Posted on September 25, 2009

Each relief valve should be equipped with inlet piping no smaller than the valve inlet flange size, and inlet piping should be as short as…

Mechanical Design of Pressure Vessels

Separator Vessels Pressure Design

Posted on September 23, 2009October 30, 2012

The design pressure for a vessel is called its “Maximum Allowable Working Pressure” (MAWP). In conversation this is sometimes referred to simply as the vessel’s…

Relief Valve Sizing

Two-Phase Flow Standard Sizes

Posted on September 25, 2009October 28, 2012

Two-Phase Flow There are no precise formulas for calculating orifice area for twophase flow. The common convention is to calculate the area required for the…

Treater Vessels Sizing

Treaters Separator Design Procedure

Posted on September 15, 2009

In specifying the size of a treater, it is necessary to determine theĀ  diameter (d), length or height of the coalescing section (Leff or h),…

Gas Processing

Gas Processing Plant Condensate Stabilizer

Posted on May 27, 2013

A gas-processing plant, is designed to recover ethane, propane, butane, and other natural gas liquids from the gas stream. A condensate stabilizer also recovers some…

Treater Vessels Sizing

Treater Separator Settling Equations

Posted on September 15, 2009October 30, 2012

The specific gravity difference between the dispersed water droplets and the oil should result in the water “sinking” to the bottom of the treatment vessel.…

Two Phase Separator Equipment

Vortex Breakers Types

Posted on September 2, 2009October 28, 2012

It is normally a good idea to include a simple vortex breaker as shown in Figure 4-9 to keep a vortex from developing when the…

Relief Valve Sizing

Liquids Flow Rate

Posted on September 25, 2009October 28, 2012

Conventional Valve, Balanced-Bellows Valve, or Pilot-Operated Valve The corresponding equations for liquid flow are the following: Note that a preliminary orifice size must be determined…

Fractions from atmospheric and vacuum distillation

Straight Run Kerosene

Posted on September 26, 2009

This fraction is usually the first side stream of a conventional atmospheric distillation unit. It may be cut to meet a burning oil specification or…

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Categories

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  • Relief Valve Sizing
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