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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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OP-IV-11ADVANCEMENT OF SLURRY BUBBLE COLUMN REACTORS FORCLEAN LIQUID FUELS PRODUCTIONMuthanna H. Al-Dahhan, N. Rados, A. Shaikh, L. Han, C. WuChemical Reaction Engineering Laboratory (CREL), Department <strong>of</strong> Energy, Environmental,and Chemical Engineering, Washington University,One Brookings Drive, Campus Box 1198, St. Louis, MO, 63130-4899, USAGas to Liquid Fischer Tropsch (FT) syn<strong>the</strong>sis is a acknowledged route for production <strong>of</strong>clean fuels and chemicals from syn<strong>the</strong>sis gas (a mixture <strong>of</strong> hydrogen and carbon monoxide)obtained from natural gas, coal or biomass. FT conversions are associated with highexo<strong>the</strong>rmic heat for which an efficient mean <strong>of</strong> heat removal is needed. Therefore, slurrybubble column reactors operated in churn turbulent flow regimes are <strong>the</strong> reactor <strong>of</strong> choice forsuch conversions. Successful commercialization <strong>of</strong> <strong>the</strong>se reactors needs thoroughunderstanding <strong>of</strong> prevailing hydrodynamics and transports for proper design, scale up,performance and operation.To achieve <strong>the</strong>se, 5 companies [ConocoPhillips (USA), Eni (Italy), Johnson Mat<strong>the</strong>y(UK), Sasol (South Africa) and Statoil-GTL-F1 (Norway-South Africa)] have supported anextensive research effort since 1999. For such effort our laboratory at Washington Universityis collaborating with Ohio State University and with Rensselaer Polytechniq <strong>Institute</strong>. AtWashington University advanced measurement techniques have been used and developedwhich provide <strong>the</strong> needed fundamental understanding <strong>of</strong> <strong>the</strong>se complex reactors. Thesetechniques are: Computer automated radioactive particle tracking (CARPT) techniques for <strong>the</strong>measurement <strong>of</strong> 3D flow structure, velocity, turbulent parameters, residence time, etc.;computed tomography (CT) and dual source computed tomography (DSCT) for <strong>the</strong>measurement <strong>of</strong> <strong>the</strong> cross sectional phases distribution along <strong>the</strong> reactor height; 4-pointoptical probe for bubble dynamics measurements (bubble size, velocity, local gas holdup andinterfacial area); overall gas dynamic tracer technique; optical probe for mass transfermeasurement and overall mass transfer coefficient measurement; heat transfer probe thatmimicked <strong>the</strong> heat exchanging internals; dynamics pressure transducers. A number <strong>of</strong>achievements have been made due to such advanced fundamental understanding <strong>of</strong>bubble/slurry bubble column. These are: advanced mechanistic reactor scale models; noninvasivetechnique for flow regime identification, new methodology for scale up bubblecolumn, new methodology to measure FT gases mass transfer coefficients; true and accuratetracer response for <strong>the</strong> liquid and slurry; accurate characterization <strong>of</strong> <strong>the</strong> gas phase extentmixing; detailed flow behavior and transport parameters mapping in a mimicked FT160

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