Hysteresis and Periodic Activity Behavior in Catalytic Chemical Reaction Systems

The mathematical theory of diffusion and reaction in permeable catalysts

1976 • 1,129 citations

Diffusion and Heat Exchange in Chemical Kinetics

1955 • 835 citations

On the dynamic behavior of continuous stirred tank reactors

1974 • 722 citations

The behaviour of porous catalyst particles in view of internal mass and heat diffusion effects

1962 • 416 citations

Diffusion and heat exchange in chemical kinetics

1956 • 189 citations

Thermisch und kinetisch verursachte Instabilitäten im Reaktionsverhalten einzelner Katalysatorkörner

1972 • 171 citations

On stability criteria of chemical reaction engineering

1969 • 125 citations

Modeling of chemical reactors — XVI Steady state axial heat and mass transfer in tubular reactors An analysis of the uniqueness of solutions

1970 • 115 citations

Stabiles und instabiles Verhalten eines adiabatischen Rohrreaktors am Beispiel der katalytischen CO-Oxydation

1967 • 112 citations

Dynamisches Verhalten und Kinetik der Kohlenmonoxid‐Oxidation am Platin‐Katalysator

1972 • 101 citations

Heat and mass transfer in monolithic honeycomb catalysts—I.

1975 • 93 citations

Analysis of nonstationary heat and mass transfer in a porous catalyst particle I*1

1969 • 83 citations

Steady-state simulation of an ammonia synthesis converter

1965 • 79 citations

An analysis of chemical reactor stability and control—II

1958 • 77 citations

A model equation arising from chemical reactor theory

1973 • 76 citations

Experimental Study of a Catalytic Trickle Bed Reactor

1974 • 74 citations

Stabilität und Zeitverhalten von Durchfluß‐Kreislauf‐Reaktoren

1970 • 72 citations

Uniqueness criteria for lumped and distributed parameter chemically reacting systems

1971 • 64 citations

Packed bed axial thermal conductivity

1972 • 62 citations

Modeling of chemical reactors—XVIII stability and oscillatory behaviour of the CSTR

1970 • 62 citations

Stability of catalytic wires

1969 • 57 citations

Der Übergang vom Zünd/Lösch‐Verhalten zu stabilen Reaktionszuständen bei einem adiabatischen Rohrreaktor

1971 • 48 citations

QUALITATIVE OBSERVATIONS OF HEAT AND MASS TRANSFER EFFECTS ON THE BEHAVIOUR OF A TRICKLE BED REACTOR

1975 • 42 citations

Ignition on catalytic wires: Kinetic parameter determination by the heated-wire technique

1974 • 37 citations

Heat and mass transfer in monolithic honeycomb catalysts—III

1978 • 35 citations

Modeling of chemical reactors—XIX transient axial heat and mass transfer in tubular reactors the stability considerations—I

1970 • 34 citations

Modeling of chemical reactors—XXI effect of simultaneous heat and mass transfer inside and outside of a pellet on reaction rate—I

1970 • 30 citations

XX.The rate of heating of wires by surface combustion

1934 • 29 citations

Experimental Study of Multiple Steady States in Adiabatic Catalytic Systems

1974 • 27 citations

On the explosion, glow, and oscillation phenomena in the oxidation of carbon monoxide

1974 • 23 citations

Theory of branching reactions with chain interaction

1970 • 21 citations

Communications on the theory of diffusion and reaction - VI. The effectiveness of spherical catalyst particles in steep external gradients

1970 • 20 citations

Kinetics and kinetic oscillation in carbon monoxide oxidation

1974 • 20 citations

Modeling of chemical reactors—XXVII. Steady state axial heat and mass transfer in tubular reactors. Effect of different values of Peclet numbers on the region of multiplicity

1973 • 19 citations

CATALYTIC OXIDATION OF CO ON CuO/Al₂O₃.I. REACTION RATE MODEL DISCRIMINATION

1973 • 19 citations

On the dynamic behavior of catalytic wires

1974 • 19 citations

A photoelectric study of the low pressure explosion limit of the wet carbon monoxide-oxygen reaction

1968 • 17 citations

Über die Knallgaskatalyse durch Palladiummischkristalle

1920 • 16 citations

STUDY OF MULTIPLE STEADY STATES IN SINGLE PELLET OF CATALYST

1971 • 15 citations

Modeling of chemical reactors—XX heat and mass transfer in porous catalyst the particle in a non-uniform external field

1970 • 13 citations

Transient heat and mass transfer in a porous catalyst III. *1Reaction with finite values of Sherwood and Nusselt number. Effect of volume contraction

1971 • 11 citations

Zur Kenntnis des Zweiphasenmodells des katalytischen Reaktors

1973 • 5 citations

Heat and mass transfer in heterogeneous catalysis. XXII. Study on effects of heat and mass transfer between the external surface of catalyst particle and the bulk of reaction mixture on reaction rate of hydrogen with oxygen

1971 • 3 citations

Heat and mass transfer in heterogeneous catalysis. XXXII. Experimental study of dynamic behaviour of the catalytic tubular flow reactor

1973 • 3 citations

Modeling and stability of catalytic fixed bed reactors

1970 • 3 citations