
Entrained Bed Reactor Quak Foo Lee Department of Chemical and Biological Engineering
Entrained Bed Reactor • Entrained bed, pneumatic transport reactor • Riser reactor, raining bed reactor • Dilute suspension of solids and usually reactors have large L/D ratio • Near plug flow • If feed particles are all of the same size, them all have same residence time
Entrained Bed Reactor • Advantage is one can control the residence time • Small particle and co-current flow • Simplified analysis • Flat velocity profile for gas • Plug flow of solids • Isothermal • Constant fluid properties
Reactor Configurations Gas + Solid Down flow Up flow D L Gas + Solid
Riser Reactor Upward particle velocity Superficial gas velocity Settling velocity of particle Gas + Solids Terminal velocity of a single particle in an unbounded fluid Note: Concentration of solids is low
Reynolds Number Region Strokes Region
Example • If we considered U0 ~Up, and we have 1 mol of gas reacting with 1 mol of solid of Mwt = 100 g/mol and p = 2 g/cm3
For uniform gas composition • Plug flow of solids Where, = time for complete reaction
For Strokes Region and SCM • With no Mass Transfer (MT) of Product Layer Diffusion (PLD) Resistance:
Critical Point Goes through a maximum at some critical R Hcrit Hmax HXs=1 Rcrit R
Find Hcrit and Rcrit • Differentiate HXs=1
Find Hcrit and Rcrit • Substitute Rcrit into HXs=1 to get Hcrit Note: To transport largest particles through the system:
Within the Strokes Region Substitute U0 into Hcrit to get Up flow
Notes • Comparison indicates Rcrit ~ 0.77 Rmax • One would do a similar calculation for any expression for τ and also can use more general equation for CD. • Note: for CA,f to be constant, e.g. at some over reactor height, we need small gas conversion (or large molar excess of species A in gas phase).
Down Flow – Raining Bed Gas + Solid For some simplified case: At For chemical reaction controlling: Down flow
Recall Up flow Down flow Ratio