AIChE Symposium Series, Volume 91, Issue 309American Institute of Chemical Engineers, 1972 - Chemical engineering |
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Page 36
... reducing agent is about 2 times faster than that using CH4 as the reducing gas . The regeneration kinetics can be described either by the zeroth or the first order reaction model depending on the temperature ranges and type of reducing ...
... reducing agent is about 2 times faster than that using CH4 as the reducing gas . The regeneration kinetics can be described either by the zeroth or the first order reaction model depending on the temperature ranges and type of reducing ...
Page 37
... reducing agent XA = 8.33x10t X1 = 5.0x10 * t -In ( 1 - X ) = 3.67x10 ° 3 t XA H2 used as the reducing agent X1 = 3.3x10-3 t ( for XA < 0.9 ) -In ( 1 - X ) = 7.0x103 t ( overall ) conversion of CuSO4 to Cu in regeneration stage ; time of ...
... reducing agent XA = 8.33x10t X1 = 5.0x10 * t -In ( 1 - X ) = 3.67x10 ° 3 t XA H2 used as the reducing agent X1 = 3.3x10-3 t ( for XA < 0.9 ) -In ( 1 - X ) = 7.0x103 t ( overall ) conversion of CuSO4 to Cu in regeneration stage ; time of ...
Page 39
... reducing gas Weight Change Percentage ( wt . % ) 2 9 127 10 10 Δ 8000 ppm 5000 ppm 2500 ppm Δ Δ ব ব ব ব 44 Flow rate : 600 ml / min ထ Conversion of Cupric Sulfate to Copper ( % ) 100 80 Temperature : 500 ° C 60 Flow rate : 320.0 ml ...
... reducing gas Weight Change Percentage ( wt . % ) 2 9 127 10 10 Δ 8000 ppm 5000 ppm 2500 ppm Δ Δ ব ব ব ব 44 Flow rate : 600 ml / min ထ Conversion of Cupric Sulfate to Copper ( % ) 100 80 Temperature : 500 ° C 60 Flow rate : 320.0 ml ...
Contents
Foreword | 1 |
NOXSO SO₂NO Flue Gas Treatment Process Adsorption Chemistry and Kinetics | 18 |
Sulphation and Regeneration of SolGel Derived Regenerative Sorbents | 32 |
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Common terms and phrases
activated carbons adsorbed adsorption adsorptive capacities alkyl alumina Aluminosiliceous amine amino-functional anisole bed volumes benzoic acid bulk density catalytic cations Chem Chemical chitosan chlorobenzene CO₂ copolymers copolymers functionalized copper oxide copper oxide sorbents CuO loading CVOC cycle dealuminated decrease dual-function efficiently remove fixed-bed flow rate flue gas desulfurization g/cm³ H₂O Haslbeck increases interactions kinetic m²/g materials MCM-41 type methane methanol micropores ml/min molecules Na₂O nitrogen NO₂ NOXSO process parameters penicillin phenol phenoxyacetate pickup polymeric polymeric resins polymers pore volume porosity precursor presorbed pressure process streams properties reactor regeneration curve resin S-VBC samples selectively and efficiently showed shown in Figure Siliceous simulation SO₂ sorption sodium sol-gel sol-gel derived solvent sorbent sorption sorption capacity storage inhibitors sulfur supported copper oxide surface area synthesized Table TCE sorption templating tertiary thermal TR/CA tyrosinase waste minimization XUS resin y-alumina supported zeolites
References to this book
Nanoporous Materials: Science and Engineering G. Q. Lu,George Xiu Song Zhao No preview available - 2004 |