Phenomena Kecepatan Bubble dan Aliran Gas Liquid Dalam Mikro-Canal

Widianto, Aloisiyus Yuli (2010) Phenomena Kecepatan Bubble dan Aliran Gas Liquid Dalam Mikro-Canal. In: Seminar Nasional Teknik Kimia Kejuangan Pengembangan Teknologi Kimia Untuk Pengelolaan Sumber Daya Alam Indonesia, 26 Januari 2010, Fakultas Teknologi Industri, UPN "Veteran" Yogyakarta.

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Micro-reactor are reactors with three dimensional structures, the inner dimensions of which are under a millimeter in size. Micro-structured reactors can be advantageously used as process engineering tools for acquiring information which allow in a short time and with greater safety, a process to be transferred to the pilot and production scale. Information for micro-structured reactors can also be used for optimizing process plats already in operation. Micro-structured reactors are suitable for the exothermic/endothermic reaction and or limited by mass transfer. The objects of the experiment are to study phenomenon of bubble velocity for gas-liquid flow as Taylor flow at 2 conditions of which are first constant-volumetric flow rate of gas 0,75 ml/min and volumetric flow rate of ethanol varies between 0,2 ml/min-1 ml/min, and second for constant-volumetric flow rate of ethanol 0,3ml/min and volumetric flow rate of gas varies between 0,3 ml/min- 1 ml/min. Two configuration of reactors(canal take form "t": canal take from serpent/meander) are used in this experiment. Results of experiment show the the bubble velocity has fluctuated to time with certain period amplitude. Bubble velocities are proportional inverse to dimension of bubble.

Item Type: Conference or Workshop Item (Paper)
Uncontrolled Keywords: micro-canal, hydrodynamic, gas-liquid flow
Subjects: T Technology > TP Chemical technology
Divisions: Faculty of Engineering > Department of Chemical Engineering
Depositing User: Adpesdam Ubaya
Date Deposited: 19 Mar 2012 03:55
Last Modified: 02 Dec 2021 03:01

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