Zobrazeno 1 - 10
of 19
pro vyhledávání: '"Mitsuyuki Nakajima"'
Publikováno v:
Journal of Chemical Engineering of Japan. 48:436-443
Publikováno v:
Chemical Engineering Journal. :671-677
A gas recycling method for establishing stable operations of a fluidized catalyst bed is studied in order to perform reactions accompanied by a decrease in the number of moles. Two operation modes using gas recycling are evaluated to prevent defluidi
Publikováno v:
KAGAKU KOGAKU RONBUNSHU. 38:272-277
Publikováno v:
Chemical Engineering Journal. 166:1126-1131
In industrial fluidized bed processes, the system often involved a change in volumetric flow. Defluidization occurs when reactions involving a decrease in gas volume are carried out in a fluidized catalyst bed. This is due to decrease in gas velocity
Autor:
Takami Kai, Jumpei Horinouchi, Tsutomu Nakazato, Mitsuyuki Nakajima, Toshio Tsutsui, Takeshige Takahashi
Publikováno v:
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN. 42:S137-S141
There are many industrially useful reactions accompanied by the change of the gas volume due to the stoichiometry. Although it is important to consider the effects of the gas-volume changes for the accurate estimation of the reactor performance, the
Publikováno v:
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN. 42:733-738
Defluidization and a decline in fluidization quality were observed in reactions involving a decrease in gas volume. This was due to a reduction in gas velocity in the emulsion phase owing to the reactions. The decrease in the gas velocity led to a re
Publikováno v:
KAGAKU KOGAKU RONBUNSHU. 34:351-357
Publikováno v:
KAGAKU KOGAKU RONBUNSHU. 30:256-261
反応によってガス体積(モル数)が減少する反応を流動触媒層で行った場合の流動化状態を調べるために, ガラス製の反応器を使用して層内で起きる現象を観察した. その結果, 反応が進行
Autor:
Mitsuyuki NAKAJIMA
Publikováno v:
Journal of the Society of Powder Technology, Japan. 30:514-521
Autor:
Takami Kai, Mitsunobu Furukawa, Kei Mizuta, Mitsuyuki Nakajima, Tsutomu Nakazato, Toshio Tsutsui
Publikováno v:
AIChE Journal.
A significant defluidization occurs when carrying out reactions involving a decrease in gas volume in a fluidized catalyst bed. The cause of this phenomenon is a decrease in the gas velocity in the emulsion phase below the minimum fluidization veloci