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Reactors estimating

A helical ribbon impeller, 45 in (1.14 m) diameter, is operated in a 47-in (1.19-m) diameter reactor estimate the fluid viscosity from torque readings. The impeller is a single-turn helix with a 1 1 pitch, so the height of the impeller is the same as the diameter, 45 in (1.14 m). It is a double-flight helix, each blade of which is 4.5 in (0.114 m) wide. [Pg.457]

For a three-phase fluidized-bed coal-liquefaction reactor, estimate... [Pg.361]

Ethylene (C2H4, 30,000 Ib/hr) at 1,000 psia and 0 F is heated to 600 F and then fed to a plug-flow reactor. Estimate the heat exchanger duty necessary to accomplish the heating. [Pg.329]

A, B, C,. . . A a BR b Ca Names of substances Free radical, as CH3 Activity Batch reactor Estimate of kinetic parameters, vector Concentration of substance A kg mol/m3 lb-mol/ft3... [Pg.3]

Continuously stirred tubular reactors, estimated value. [Pg.92]

Shah YT, Kelkar BG, Godbole SP, Deckwer W-D. 1982. Design parameters colmnn reactors estimations for bubble. AIChE J 28(3) 353-379. [Pg.203]


See other pages where Reactors estimating is mentioned: [Pg.1017]    [Pg.227]    [Pg.191]    [Pg.227]    [Pg.288]    [Pg.239]   


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