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. |
Dall'interno del libro
Risultati 1-3 di 83
Pagina 10-3
... coefficient , B.t.u./ ( hr . ) ( sq . ft . ) ( ° F . ) ; convection coefficient for condensate film in Eqs . ( 10-66 ) and ( 10-68 ) , B.t.u./(hr.)(sq . ft . ) ( ° F . ) . = effective combined coefficient for simul- taneous gas - vapor ...
... coefficient , B.t.u./ ( hr . ) ( sq . ft . ) ( ° F . ) ; convection coefficient for condensate film in Eqs . ( 10-66 ) and ( 10-68 ) , B.t.u./(hr.)(sq . ft . ) ( ° F . ) . = effective combined coefficient for simul- taneous gas - vapor ...
Pagina 10-21
... coefficient ( based on inside area ) : 15 B.t.u./(hr . ) ( sq . ft . ) ( F. ) . Equation ( 10-39 ) . Condensate film coefficient ( based on inside area ) : 985 B.t.u./ ( hr . ) ( sq . ft . ) ( F. ) . Equation ( 10-46 ) . Water film ...
... coefficient ( based on inside area ) : 15 B.t.u./(hr . ) ( sq . ft . ) ( F. ) . Equation ( 10-39 ) . Condensate film coefficient ( based on inside area ) : 985 B.t.u./ ( hr . ) ( sq . ft . ) ( F. ) . Equation ( 10-46 ) . Water film ...
Pagina 11-34
... coefficient quite appre- ciably . Meisenberg , Boarts , and Badger [ Trans . Am . Inst . Chem . Engrs . , 31 , 622 ( 1936 ) ] have determined steam - film coefficients in the presence of air : hs = 0.670 k3p2g AH 0.25 Ιμ ΔΤ 0.11 ( 1 ) ...
... coefficient quite appre- ciably . Meisenberg , Boarts , and Badger [ Trans . Am . Inst . Chem . Engrs . , 31 , 622 ( 1936 ) ] have determined steam - film coefficients in the presence of air : hs = 0.670 k3p2g AH 0.25 Ιμ ΔΤ 0.11 ( 1 ) ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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