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Water Treating Equipment

Corrugated Plate Interceptor Design

Posted on September 4, 2009October 31, 2012

The most common form of parallel plate interceptor used in oil facilities is the corrugated plate interceptor (CPI). This is a refinement of the PPI…

Two Phase Separator Sizing

Two Phase Horizontal Separators Sizing

Posted on September 14, 2009October 30, 2012

For sizing a horizontal separator it is necessary to choose a seam-toseam  vessel length and a diameter. This choice must satisfy the conditions  for gas…

Water Treating Equipment

Hydrocyclone Separator

Posted on January 6, 2011October 28, 2012

Hydrocyclone separators, sometimes called enhanced gravity separators, use centrifugal force to remove oil droplets from oily water. As shown in Figure 7-16, static hydrocyclone separator…

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…

Pressure Drop in Piping

Bernoulli’s Theorem

Posted on September 25, 2009October 28, 2012

It is customary to express the energy contained in a fluid in terms of the potential energy contained in an equivalent height or “head” of…

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…

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…

Relief Valve Sizing

Critical Flow

Posted on September 25, 2009October 28, 2012

The flow of a compressible fluid through an orifice is limited by critical flow. Critical flow is also referred to as choked flow, sonic flow,…

Gas Processing

Tray Efficiency and Tower Height

Posted on May 27, 2013

In condensate stabilizers, trays generally have 70% equilibrium stage efficiency. That is, 1.4 actual trays are required to provide one theoretical stage. The spacing between…

Gas Processing

Selexol Process

Posted on October 1, 2020October 6, 2020

Developed by Allied Chemical Company, this process is selective toward removing sulfur compounds. Levels of CO2 can be reduced by approximately 85%. This process may…

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