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 18-8
... pressure drop of a bubble - cap tray . However , since the tray itself is an integral component of the vapor - dispersion system of the sieve tray , the thickness is significant . In practice , it has been found that 0.1 < tray ...
... pressure drop of a bubble - cap tray . However , since the tray itself is an integral component of the vapor - dispersion system of the sieve tray , the thickness is significant . In practice , it has been found that 0.1 < tray ...
Pagina 18-12
... pressure drop for sieve trays per unit of active tray thickness area for 0.5 < < 0.7 is indicated perforation diameter , ن ) in Fig . 18-17a , b , c ( Teller , " Allen's Handbook for Oil and Chemical Industries , " 1958 ) . The pressure ...
... pressure drop for sieve trays per unit of active tray thickness area for 0.5 < < 0.7 is indicated perforation diameter , ن ) in Fig . 18-17a , b , c ( Teller , " Allen's Handbook for Oil and Chemical Industries , " 1958 ) . The pressure ...
Pagina 18-26
... Pressure Drop and Stability . Pressure drop and instability phenomena in packed columns are illustrated in Fig . 18-45 . Log pressure drop ダ Log ( gas velocity / unit of tower cross section ) ( G / ¢ ) FIG . 18-45 . Pressure - drop ...
... Pressure Drop and Stability . Pressure drop and instability phenomena in packed columns are illustrated in Fig . 18-45 . Log pressure drop ダ Log ( gas velocity / unit of tower cross section ) ( G / ¢ ) FIG . 18-45 . Pressure - drop ...
Sommario
Alphabetical Index at back of book | 1-1 |
SECTION | 1-2 |
MATHEMATICS | 1-46 |
Copyright | |
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