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Pressure Relief

Process Relief Requirements

Posted on September 25, 2009

The ASME code requires every pressure vessel that can be blocked In to have a relief valve to alleviate pressure build up due to thermal…

Hydrates

Hydrate Formation Temperature or Pressure Determination

Posted on September 15, 2009October 28, 2012

Knowledge of the temperature and pressure of a gas stream at the wellhead is important for determining whether hydrate formation can be expected when the…

Gas Processing

Structured Packing

Posted on May 27, 2013May 27, 2013

A bed of structured packing consists of a bed support upon which elements of structured packing are placed. Beds of structured packing typically have lower…

Fluid Properties

Specific Gravity and Density

Posted on September 16, 2009October 29, 2012

Specific gravity of a liquid is the ratio of the density of the liquid at 60°F to the density of pure water. API gravity is…

LTX Units and Line Heaters

LTX Units Heat Duty

Posted on September 15, 2009October 28, 2012

To calculate the heat duty it must be remembered that the pressure drop through the choke is instantaneous. That is, no heat is absorbed or…

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…

Potential Operating Problem

Sand Problems

Posted on September 2, 2009

Sand can be very troublesome in separators by causing cutout of valve trim, plugging of separator internals, and accumulation in the bottom of the separator.…

Crude Oil Treating System

Horizontal Treaters Separator

Posted on September 2, 2009October 30, 2012

For most multi-well situations horizontal treaters are normally required. Figure 6-10 shows a typical design of a horizontal treater. Flow enters the front section of…

Crude Oil Treating System

Forming Emulsions Process

Posted on August 23, 2009October 31, 2012

For an emulsion to exist there must be two mutually immiscible liquids, an emulsifying agent, and sufficient agitation to disperse the discontinuous phase into the…

Mechanical Design of Pressure Vessels

Separator Pressure Vessels Temperature Design

Posted on September 23, 2009

The maximum and minimum design temperatures for a vessel will determine the maximum allowable stress value permitted for the material to be used in the…

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