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PFTR via Multistage CSTR

075 vs. 0.05%, tuyeres look dim, blast pressure normal, slag is more viscous, burden descent irregular water leak/burden maldistribution/faulty process control giving weighing errors. [Pg.253]

burden hangs and slips water leak/burden maldistribution/faulty process control giving weighing errors. [Pg.253]

Incineration rotating hearth with single, fixed plough. Combustion air enters tangentially and exits the top. [Pg.253]

Phases Gas plus reacting solid. Solid residence time, 0.004-2 s gas residence time, 1 s solid particle diameter 0.002-0.4 mm. Capacity solids 0.3-0.55 kg wet solids/s. [Pg.253]

For fast reactions, bulk phase film diffusion may control. Incineration diam. [Pg.253]

See other pages where PFTR via Multistage CSTR is mentioned: [Pg.1420]    [Pg.253]    [Pg.253]    [Pg.424]    [Pg.1420]    [Pg.253]    [Pg.253]    [Pg.424]   


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CSTR multistage

CSTR-PFTR

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