Monthly Archives for June 2013

Dead Band in Process Control

The range through which an input signal can be varied, upon reversal of direction, without initiating an observable change in the output signal. Dead band is the name given to a general phenomenon that can apply to any device. For … Continue reading

21. June 2013 by Jack
Categories: Control Valve | Tags: | Leave a comment

Vapor-Liquid Equilibria

What we know about vapor-liquid equilibria is mainly based on experimental data. There are of course predictive methods, but they are based on the results of measurements for the determination of the parameters they involve and the control of their … Continue reading

11. June 2013 by and
Categories: Petroleum Refinery | Tags: | Leave a comment

Membrane Separations

Membrane separation operations are still seldom used in refining today. The potential applications of the different ultrafiltration, pervaporation and gaseous permeation technologies are described in the other section. Since selectiv­ity is kinetic, a membrane separation module separates a mixture into … Continue reading

11. June 2013 by and
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Fixed Bed Adsorption Operations

In an adsorption operation the movement of the solid phase gives rise to seri­ous problems (solid phase displacement devices, mechanical resistance of the adsorbent, etc.). As a result, the adsorbent is generally implemented in a fixed bed. The adsorption-desorption operation … Continue reading

06. June 2013 by and
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Thermodynamic Equilibrium and Kinetic Factors

Table 1.1 shows that the most common separation operations are based on equilibrium selectivity, also termed thermodynamic selectivity. This selectivity is due to the fact that at thermodynamic equilibrium, the distribution of the component(s) to be separated out is different … Continue reading

06. June 2013 by and
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Membrane Separation

Separation can also be based on kinetic selectivity, i.e. on a difference in migration velocity of the relevant components. This principle is used in a membrane separation operation as represented schematically in Figure 1.5 for a binary mixture of two … Continue reading

06. June 2013 by and
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Equilibrium Based Separation

Separation operations based on equilibrium selectivity can be classified according to the separating agent that is used (matter or energy) and the nature of the phases in contact: Distillation is the most commonly used basic operation. The feed is nor­mally … Continue reading

06. June 2013 by and
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Function of Separation Operations in Refining

A crude oil is made up of a complex mixture of a very large number of compo­nents, most of which are hydrocarbons. In order to get petroleum products that meet given specifications, it is first necessary to sep­arate out the … Continue reading

06. June 2013 by and
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Differential Pressure in Distillation Tower

The tower differential pressure is the difference between the pressures at the bottom of the tower and the pressures at top of the tower. This difference in pressure is caused by the flow of vapor in the tower. Without vapor … Continue reading

05. June 2013 by and
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Temperature Control in Distillation Tower

The temperature decreases as the material move higher in the tower. The gradual decrease in temperature from the bottom of the distillation tower to the top is called the temperature gradient. The temperature gradient is measured in term of difference … Continue reading

04. June 2013 by and
Categories: Petroleum Refinery | Tags: , , , | Leave a comment

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