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Fauskes method including disengagement

This method extends Fauske s method14,51 (see A5.3.2) to cases in which the system is not inherently foamy and so vapour/ liquid disengagement will occur before the reactor js empty. [Pg.167]

The method is for vapour pressure systems and the conditions of applicability are as given in A5.3.1, with the addition of (a) and (b) below  [Pg.167]

In order to use the sizing method, the reactor, void fraction, aD, at which total vapour/ liquid disengagement is expected at the maximum accumulated pressure, must first be evaluated. This may be done by level swell calculation (see Annex 3) or by small-scale experiment with the same vapour superficial velocity as will occur at plant-scale (see Annex 2). Equation (A5.7)can then be used to find the relief area  [Pg.168]

A value of the correction factor, for vent line friction, F, required by equation (A5.7) can be obtained from Table A5.1. [Pg.168]

5 Worked example of Fauske s method with disengagement [Pg.168]


See other pages where Fauskes method including disengagement is mentioned: [Pg.167]    [Pg.48]   


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