Hydrodynamics Mass Transfer in a Gas-Liquid Vertical Column (Paperback)
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A bauble column (BC) is a gas liquid contactor used to achieve mass transfer between liquid & gas. It has a wide range of applications in chemical & process engineering. The gas hold- Up (Eg) & the volumetric liquid phase mass transfer coefficient (KLa) were studied experimentally in the present work by using ethanol water mixture as liquid phase & air as a gas phase. The study was developed to express the effects of the process variables on Eg & KLg the exponential work was designed for this purpose in the following experimental range: 1.Weight percent of ethanol in water (0- 0.8) Wt%. 2.Superficial gas velocity of air (0.01-0.11) m/S. 3.Operation temperature (26-27) °C. 4.Operating pressure (1× 105 - 6×105) N/m2.

Von Händler/Antiquariat, AHA-BUCH GmbH [51283250], Einbeck, NDS, Germany.
This item is printed on demand - Print on Demand Titel. Neuware - A bauble column (BC) is a gas - liquid contactor used to achieve mass transfer between liquid & gas. It has a wide range of applications in chemical & process engineering. The gas hold- Up (Eg) & the volumetric liquid phase mass transfer coefficient (KLa) were studied experimentally in the present work by using ethanol - water mixture as liquid phase & air as a gas phase. The study was developed to express the effects of the process variables on Eg & KLg the exponential work was designed for this purpose in the following experimental range: 1.Weight percent of ethanol in water (0- 0.8) Wt%. 2.Superficial gas velocity of air (0.01-0.11) m/S. 3.Operation temperature (26-27) °C. 4.Operating pressure (1× 105 - 6×105) N/m2 104 pp. Englisch.

Von Händler/Antiquariat, BuySomeBooks [52360437], Las Vegas, NV, U.S.A.
Paperback. 104 pages. Dimensions: 8.7in. x 5.9in. x 0.2in.A bauble column (BC) is a gas liquid contactor used to achieve mass transfer between liquid and gas. It has a wide range of applications in chemical and process engineering. The gas hold- Up (Eg) and the volumetric liquid phase mass transfer coefficient (KLa) were studied experimentally in the present work by using ethanol water mixture as liquid phase and air as a gas phase. The study was developed to express the effects of the process variables on Eg and KLg the exponential work was designed for this purpose in the following experimental range: 1. Weight percent of ethanol in water (0- 0. 8) Wt. 2. Superficial gas velocity of air (0. 01-0. 11) ms. 3. Operation temperature (26-27) C. 4. Operating pressure (1 105 - 6105) Nm2 This item ships from multiple locations. Your book may arrive from Roseburg,OR, La Vergne,TN.

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Hanna Fadi,Paperback, English-language edition,Pub by LAP Lambert Academic Publishing AG & Co. KG.

Von Händler/Antiquariat, Paperbackshop-US [8408184], Secaucus, NJ, U.S.A.
New Book. This item is printed on demand. Shipped from US This item is printed on demand.