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AN INVESTIGATION OF THE REACTION BETWEEN CARBON-MONOXIDE AND HYDROGEN ON A NICKEL CATALYST AT PRESSURES ABOVE ONE ATMOSPHERE PDF

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Preview AN INVESTIGATION OF THE REACTION BETWEEN CARBON-MONOXIDE AND HYDROGEN ON A NICKEL CATALYST AT PRESSURES ABOVE ONE ATMOSPHERE

AN INVESTIGATION CF THE REACTION BETWEEN CARBON MCI I OX IDE AMD HYDROGEN CN A NICKEL CATALYST AT PRESSURES ABOVE ONE ATMOSPHERE by John Ardell Pursley A Dissertation Submitted in partial Fulfillment of the Requirements for the Degree of Doctor of Philosophy in the University of Michigan Doctoral Committee: Professor R. R. White, Chairman Associate Professor M. J. Sinnott Assistant Professor C. M. Sliepcevich 'ssociate Frofessor iC. F. '/Yestrum, Jr. ssociate Professor 3. R. Williams January, 19 %1 - ii- TO HENRY K. DICE - iii - ACKNOWLEDGEMENT Itie author -wishes to express his appreciation to all those who have directly or indirectly aided in this investigation and in particular to: Professor R.R. White, chairman of the doctoral committee and supervisor of the Michigan Gas Association Fellowship, whose foresight and guidance have created an integrated research program on the fundamentals of catalysis of which this manuscript represents but a small part. The doctoral committee members for their advice and criticism. The wisdom of the Michigan Gas Association by which this fellowship was established and has been supported for the past fifty years. To John N. Dev/, friend and professional associate, who has been concerned with all the details of this research program. To the graduate students and, in particular, to William A. Doemer of the Department of Chemical and Metallurgical En­ gineering for suggestions and criticisms. TABLE OF CONTENTS Page LIST OF FIGURES vii LIST OF TABLES vii LIST OF GRAPHS viii TABLE CF NOMENCLATURE X SUMMARY xvi INTRODU CTION 1 THEORETICAL BASIS 3 EQUIPMENT AND OPERATING PROCEDURE 1U General 2h Equipment Rack 2h Control Panels 25 Piping 25 Valves 26 Wiring 27 Flov/ and Pressure Control 28 Hydrogen Control 28 Carbon Monoxide Control 31 '.Thermostat 32 Startup and Operation 33 Gas Sampling 35 Thermal Conductivity Cells 36 Voltage Regulator 37 Sampling System 37 Reactor 38 Preheater 39 Reaction Tube 39 - V - TABLE OF CONTENTS (cont'd) Page Product Condenser 1+0 Jacket 1+0 Jacket Temperature Control 1+1 Temperature Measurement 1+2 Compression System 1+3 Flow 1+3 Compressor uu Power Control 1+5 Startup and Opera-Mcn 1+6 Methods of Analysis 1+7 PRELIMINARY TESTS 1+9 Wall Effect 1+9 Catalyst Stability 55 Carbon Deposition 55 Poisoning 56 Thermal Deactivation 57 Pretreatmcnt 61 EXPERIMENTAL DATA 61+ Materials 61+ Experimental Errors 66 Catalyst Test Data 70 CORRELATION OF DATA 85 Effect of Products 85 Effect of Temperature 86 P - vi - TABLE OF CONTENTS (cont'd) Page Effect of Mass Transfer 88 Between Bulk of Gas Stream and Catalyst Particle 89 Diffusion in the Catalyst Particle 90 Surface Reaction 97 CONCLUSIONS 113 APPENDIX H U BIBLIOGRAPHY I36 - vii - LIST CF FIGURES No. Title Page la. Catalyst Testing Unit, Front View 15 lb. Catalyst Testing Unit, Rear View 16 2. Sampling System 17 3a. Control panel, Rear View 18 3L. Control Panel, Rear View Details 19 lia • Flow Diagram, Reactor Control System 20 Ub. Flow Diagram, Reactor 21 Uc • Flow Diagram, Compressor System 22 —/ p1 . Wiring Diagram, Control System 23 LIST OF TABLES 1. Experimental Data 7S 2a. Possible Rate Controlling Steps 83 2b. Rate Equation Constants 10U 3. Material Balances 128 Experimental Errors 129 5. Spectrometer Calibration Data 132 6. Pressure Gauge Calibration Data 1— 1 7. Equipment Manufacturers 131; - viii - LIST OF GRAPHS Title Page Ho. la. Wall Effect (Reactangular Coordinates) 53 lb. Wall Effect (Logrithmic Coordinates) 5U 2. Carbon Deposition 58 3. Poisoning 59 Thermal Deactivation 60 h- 5. Pretreated Catalyst Stability 63 6a a Feed Compositions 73 6b. Feed Rates 7h 7. Catalyst Bod Temperature Rise 37 8a. Effect of Hass Velocity on Reaction Rate 91 8b. Effect of Mass Velocity on Conversion 92 9a. Diffusion in the Catalyst Particle (Pressure Effect) 95 9b. Diffusion in the Catalyst Particle (Concentration Effect) 96 10a. Reaction Rate Constants; P/r0) vs. (P)°-S 99 10b. Reaction Rate Constants; 100 PC0/ro) vs- (PH2)0*^ 10c. Reaction Rate Constants; pc(/ r0) vs. (p^) 101 11a. Reaction Rate Constants: P ^ A o ) VS. (P) 102 lib. Reaction Rate Constants: 103 PC0)(PH2)0‘5/ro vs‘ (PH2> 12a. Effect of Pressure on the Reaction Itate (500°F) 105 12b. Effect of Pressure on the Reaction Rate (550°F) 106 12c. Effect of Pressure on the Reaction Rate (600°F) 107- 13a. Effect of Concentration on the Reaction Rate (250 psia) 100 13b. Effect of Concentration on the Reaction Rate (175 psia) 109 13c. Effect of Concentration on the Reaction Rate (100 psia) 110 ■MM - ix - LIST OF GRAPHS (cont'd) No. Title Page 13d. Effect of Concentration on the Reaction Rate (15 psia) 111 111. Infra-Red Spectrophotometer Calibration 133 - X - TABLE OF NOMENCLATURE 1 A constant 1/(k)JT A reactant A in the overall reaction a number of mols of A consumed in the overall reaction activity of reactant A in the fluid phase a3 activity of reactant B in the fluid phase D a ^ activity of carbon monoxide in the gas phase ap activity of any component, F, in the fluid phase a„ activity of the diffusing component in the gas phase O a^2 activity of hydrogen in the gas phase aj activity of the inert components I in the fluid phase am mean surface of pellets per unit mass ap surface area per single nellet a^ activity of product R in the fluid phase aQ activity of product S in the fluid phase B constant b/(k)fT B reactant B in the overall reaction b constant Kjj(l-X)^ b number of mols of B consumed in the overall reaction C active center 1 C constant c/(k)ff C observed overall rate factor for a reaction c constant KC0(X) f KH2(1-X) c empirical constant c average radius of pores in a particle c the molal concentration of vacant active centers per unit mass of catalyst

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