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 2-7
... Volume abc ; surface area = 2 ( ab + ac + be ) ; diagonal √a2 + b2 + c2 where a , b . c are the lengths of the sides . - ww • • Prism . Volume = ( area of base ) · ( altitude ) ; lateral surface area ( perimeter of right section ) ...
... Volume abc ; surface area = 2 ( ab + ac + be ) ; diagonal √a2 + b2 + c2 where a , b . c are the lengths of the sides . - ww • • Prism . Volume = ( area of base ) · ( altitude ) ; lateral surface area ( perimeter of right section ) ...
Pagina 4-19
... volume batch processes to A na2 dna VRO = NAI ΤΑ ( 4-75 ) If ra is expressed in terms of molal concentrations , these can be converted to expressions involving na by noting that CVR = n ; and n ; at any time may be related to na using ...
... volume batch processes to A na2 dna VRO = NAI ΤΑ ( 4-75 ) If ra is expressed in terms of molal concentrations , these can be converted to expressions involving na by noting that CVR = n ; and n ; at any time may be related to na using ...
Pagina 4-23
... Volume in reactor at any time is assumed to be the initial volume plus volume of feed added . A = Design Equations molar heat capacity of the feed , B.t.u./ dnc ( mole ) ( ° F . ) = ( ri r2 ) do B.t.u./(mole ) ( ° F . ) D = reactor ...
... Volume in reactor at any time is assumed to be the initial volume plus volume of feed added . A = Design Equations molar heat capacity of the feed , B.t.u./ dnc ( mole ) ( ° F . ) = ( ri r2 ) do B.t.u./(mole ) ( ° F . ) D = reactor ...
Sommario
Alphabetical Index at back of book | 1-1 |
SECTION | 1-2 |
MATHEMATICS | 1-46 |
Copyright | |
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