Basic principles and calculations in chemical engineering by David M. Himmelblau, James B. Riggs PDF

By David M. Himmelblau, James B. Riggs

ISBN-10: 0133057984

ISBN-13: 9780133057980

ISBN-10: 0133766667

ISBN-13: 9780133766660

''Over the earlier decade the sphere of chemical engineering has broadened considerably, encompassing a variety of topics. besides the fact that, the fundamental underlying ideas have remained an identical. to assist readers hold speed, this quantity keeps to supply a finished advent to the rules and methods utilized in the sphere of chemical, petroleum, and environmental engineering.'' ''As in earlier variants, author Read more...

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Basic principles and calculations in chemical engineering by David M. Himmelblau, James B. Riggs PDF

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The disc identification tag is notched on one side of its neck and a notched label on the ring makes it impossible to seat the disc in an upside-down position. Even in poor light the operator can feel that the disc is incorrectly seated; in any event the pressure side of the holder will not seat properly and premature failure will occur. ) 38 3. DETERMINING THE SET PRESSURE AND BURSTING PRESSURE The two most important parameters of a safety valve are the relief rate at relieving conditions and the set pressure, that is the pressure at which the safety valve commences to lift.

L)? (e) Is the fluid in the discharge system aggressive to the discharge side of the safety valve? If the answer to all five questions is no, use a safety valve; either a single valve or several valves in parallel to provide the required discharge capacity. If the answer to one or more questions is yes, use a bursting disc either alone or in combination with a safety valve. 1 32 RELIEP DEVICES whnical nseictions? a) Is the pressurerise too rapid for a safety valve? b) Is the process fluid too toxic?

B) Is the process fluid too toxic? c) Is the pocess fluid too corrosive? d) Is h e pmcess fluid likely to pmduw ' gums. solids or icing? e) Is the fluid in the disehage aggressive? All no B ~ *Fs Cm a single safety valve meet L the ryuired relief rate? f) Is the loss of mmlsafter a NPW acceptable? g) CM rhe p o e c S S be Shut d0W 10repke a disc? Oyes No g) Multi ssfay valves in Bursting discs in perallel Is Ihe life of a bursting disc between operating and set pnssure tight? h) Is the process nggmsive?

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Basic principles and calculations in chemical engineering by David M. Himmelblau, James B. Riggs


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