Oxidation of Propylene in Liquid Phase Using Packed Columns

Yano, Takeo; Suetaka, Toru; Umehara, Tadashi; Yamashita, Toshikazu

doi:10.1246/nikkashi.1972.1740

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1974

1975

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“…At first glance, it may be thought that the purpose is just to find the hydrodynamic conditions where k L , the coefficient for physical mass transfer in the model, is equal to the coefficient of the industrial apparatus (Charpentier and Laurent, 1974; Yano et al, 1973). But such a correlation could be obtained in a much easier way by performing only physical absorption experiments and without going into the problems associated with a chemical reaction in the system.…”

Section: Department Of Chemical Engineering Ben-gurion University Of mentioning

confidence: 99%

Further considerations on the Danckwerts‐Gillham method for design of gas absorbers

Merchuk¹

1975

AIChE Journal

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binary mixture (fructose-water, Figure 2) since a! depends only on the values of C2 and bi, where C 2 is defined as the ratio of dead volume of the bottom reservoir to the displacement.Chen and Hill (1971) have shown that there are three possible regions of pump operations. Regions 1, 2, and 3, depending on the relative magnitudes of penetration distances Lli and L2ir and the height of the column h. AS long as for the continuous pump and

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Section: Department Of Chemical Engineering Ben-gurion University Of mentioning

confidence: 99%