Cracking in petroleum refineries

A J MAKWANA
0
It is an endothermic reaction.Disassociation of high molecular wt. Hydrocarbons into smaller fragments through agency of heat with or without catalyst is called cracking.

 To converts the heavy residue to lighter distillate.

 To decreases the boiling point, pour point and Viscosity.

 To increases the octane number.

 To increases the unsaturation and aromatization.


Effect of temperature and pressure on cracking:

 Pressure retards cracking reactions. But in practice a positive pressure of 10 to 15 Kgs/cm2is used to minimize coke formation. Recycling increases refractory nature of stocks and hence recycling should not exceed 2 to 3 times of fresh stock for economic operation.

 Increase in cracking time and temperature increases the lighter fraction and decreases the fuel oil yield.

 Pressure has negligible effect on velocity of reaction. At high pr. gas / gasoline ratio is less

 Increases in pressure also increase the coke production.

 For high pressure more resistance time is required which results in formation of more hydrocarbons.

 With higher pressures gas to gasoline ratio becomes less.Thermal cracking:

 Disassociation of high molecular wt. Hydrocarbons into smaller fragments through agency of heat alone is called Thermal cracking.

 It is an endothermic and gas phase reaction and here all feed stock vaporized.

 Thermal cracking is currently used to "upgrade" very heavy fractions to produce light fractions or distillates, burner fuel and/or petroleum coke.

 In this process long chain hydrocarbons broken to smaller fragment one is 

saturated and other is unsaturated and also formation of coke and hydrogen.

 Process variable: feed stock property, temperature, pressure and resistance

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