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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…

Two Phase Oil and Gas Separation

Vertical Two Phase Separator Basic Design

Posted on August 17, 2009October 29, 2012

Figure 4-2 is a schematic of a vertical separator. In this configuration the inlet flow enters the vessel through the side. As in the horizontal…

Basic Configuration

Lease Automatic Custudy Transfer

Posted on August 21, 2009October 29, 2012

In large facilities oil is typically sold through a LACT unit, which is designed to meet API Standards and whatever additional measuring and sampling standards…

Oil and Water Separation

Vessel Internal Design

Posted on September 2, 2009

Two common internals not discussed are coalescing plates and sand jets. It is possible to use various plate or pipe coalescer designs to aid in…

Condensate Stabilization

Partial Pressure

Posted on September 16, 2009October 29, 2012

The fraction of any one component that flashes to gas at any stage in a process is a function of the temperature, pressure, and composition…

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…

LTX Units and Line Heaters

Fire Tube Sizing

Posted on September 16, 2009October 28, 2012

The area of the fire tube is normally calculated based on a heat flux rate of 10,000 Btu/hr-ft2. The fire-tube length can be determined from:…

Pressure Relief

Relief Valve Vent Scrubber

Posted on September 25, 2009

A vent scrubber is a two-phase separator designed to remove the liquid from the relieving fluids before the gas is flared or vented. The liquid…

Two Phase Separator Theory

Two Phase Separator Re-entrainment

Posted on September 14, 2009

Re-entrainment is a phenomenon caused by high gas velocity at the gas-liquid interface of a separator. Momentum transfer from the gas to the liquid causes…

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…

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