Chemical Engineers' Handbook, Volume 4,Parte 1963Robert H. Perry McGraw-Hill, 1963 - 1919 pagine Textbook on chemical industry engineering - covers theoretics, definitions, technical aspects, etc. |
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Pagina 4-1
Robert H. Perry. SECTION 4 REACTION KINETICS , REACTOR DESIGN , AND THERMODYNAMICS BY CONTENTS REACTION KINETICS AND REACTOR DESIGN Table 4-1 . Rate Equations. Robert H. Perry , Ph.D. , Professor , Department of Chemical Engineering ...
Robert H. Perry. SECTION 4 REACTION KINETICS , REACTOR DESIGN , AND THERMODYNAMICS BY CONTENTS REACTION KINETICS AND REACTOR DESIGN Table 4-1 . Rate Equations. Robert H. Perry , Ph.D. , Professor , Department of Chemical Engineering ...
Pagina 4-22
... reactor yields 1 CACACACвo - CA ° 2 k ( 0 - 00 ) In Сво - Сло САС ВО ( 4-89 ) For the stirred ( completely back - mixed ) tank flow reac- tor , a material balance on component A gives FCA F PF PF CA + KCACBVR where CA is the feed ...
... reactor yields 1 CACACACвo - CA ° 2 k ( 0 - 00 ) In Сво - Сло САС ВО ( 4-89 ) For the stirred ( completely back - mixed ) tank flow reac- tor , a material balance on component A gives FCA F PF PF CA + KCACBVR where CA is the feed ...
Pagina 20-39
... reactor over the kiln and replacing the bucket elevator with a pneumatic catalyst air lift . Referring to Fig . 20-51 , the charge is first heated with fractionator streams , combined with recycle , and charged to the reactor as a ...
... reactor over the kiln and replacing the bucket elevator with a pneumatic catalyst air lift . Referring to Fig . 20-51 , the charge is first heated with fractionator streams , combined with recycle , and charged to the reactor as a ...
Sommario
Alphabetical Index at back of book | 1-1 |
SECTION | 1-2 |
MATHEMATICS | 1-46 |
Copyright | |
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