According to Wikipedia, Neal Russell Amundson was an American chemical engineer and applied mathematician. He was the Chair of the Department of Chemical Engineering at the University of Minnesota for over 25 years. Later, he was the Cullen Professor of Chemical & Biomolecular Engineering and Mathematics at the University of Houston. Amundson was considered one of the most prominent chemical engineering educators and researchers in the United States. The Chemical Engineering and Materials Science building at the University of Minnesota-Twin Cities bears his name.

- Mathematics of Adsorption in Beds. VI. The Effect of Longitudinal Diffusion in Ion Exchange and Chromatographic Columns (821)
- An analysis of chemical reactor stability and control—I: The possibility of local control, with perfect or imperfect control mechanisms (333)
- On the theory of multicomponent chromatography (235)
- Breakage and Coalescence in Dispersed Phase Systems (179)
- Chemical reactor stability and sensitivity (173)
- Analysis of Breakage in Dispersed Phase Systems (166)
- Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle (163)
- Some remarks on longitudinal mixing or diffusion in fixed beds (129)
- A model for evaporation of a multicomponent droplet (111)
- Chemical reactor stability and sensitivity: II. Effect of parameters on sensitivity of empty tubular reactors (111)
- Theory and application of hyperbolic systems of quasilinear equations (109)
- An analysis of chemical reactor stability and control—II: The evolution of proportional control☆ (85)
- A study of the shock layer in nonequilibrium exchange systems (80)
- Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 2. An Extension (80)
- Stability of Adiabatic Packed Bed Reactors. An Elementary Treatment (72)
- Studies in the control of tubular reactors-I General Considerations (67)
- Uniqueness of the steady state solutions for chemical reactor occurring in a catalyst particle or in a tubular reaction with axial diffusion (65)
- Mathematics of Adsorption in Beds. V. Effect of Intra-particle Diffusion in Flow Systems in Fixed Beds (59)
- Shock layer in two solute chromatography: effect of axial dispersion and mass transfer (57)
- Multicomponent adsorption in continuous countercurrent exchangers (53)
- Analysis of multicomponent separation by displacement development (51)
- Dynamic behavior of a porous char particle burning in an oxygen‐containing environment: Part I: Constant particle radius (51)
- Intraparticle diffusion and conduction in porous catalysts—II: Complex reactions (49)
- Optimum temperature gradients in tubular reactors—I: General theory and methods (48)
- A single‐particle char gasification model (48)
- Oscillatory behavior of a two‐phase natural‐circulation loop (48)
- Continuous polymerization models—I: Polymerization in continuous stirred tank reactors (47)
- Solid-Fluid Interactions in Fixed and Moving Beds Fixed Beds with Small Particles (47)
- Mathematical methods in chemical engineering : matrices and their application (45)
- Transport in composite materials: Reduction to a self adjoint formalism (44)
- An analysis of an adiabatic adsorption column: Part 1. Theoretical development (43)
- An analysis of chemical reactor stability and control—III: The principles of programming reactor calculations. Some extensions☆ (43)
- An analysis of chemical reactor stability and control—Va Two-phase systems in physical equilibrium—1☆ (40)
- Linear operator methods in chemical engineering with applications to transport and chemical reaction systems (40)
- Char gasification in a countercurrent reactor (40)
- Observations on fixed‐bed dispersion models: The role of the interstitial fluid (39)
- Modelling of fluidized bed reactorsIV?Combustion of carbon particles (38)
- A new inorganic atmospheric aerosol phase equilibrium model (UHAERO) (38)
- Continuous polymerization models—part II: Batch reactor polymerization (38)
- A Note on the Mathematics of Adsorption in Beds (38)
- Stability of loop reactors (37)
- Solid-Fluid Heat Exchange in Moving Beds (37)
- Multicomponent Distillation Calculations on a Large Digital Computer (37)
- An analysis of chemical reactor stability and control—VIII: The direct method of Lyapunov. Introduction and applications to simple reactions in stirred vessels (36)
- Diffusion and Reaction in a stagnant Boundary Layer about a Carbon Particle. 5. Pseudo-Steady-State structure and Parameter Sensitivity (36)
- Quasilinear hyperbolic systems and waves, Alan Jeffrey, Pitman Publishing, London, 230 pages, $ 6.90 (35)
- Effect of Intraparticle Diffusion: Agitated Nonflow Adsorption Systems (35)
- Some further observations on tubular reactor stability (35)
- Creeping Profiles in Catalytic Fixed Bed Reactors. Continuous Models (34)
- Mathematics of Adsorption. IV. Effect of Intraparticle Diffusion in Agitated Static Systems (34)
- Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 6. Effect of Water Vapor on the Pseudo-Steady-State Structure (33)
- Stability of Adiabatic Packed-Bed Reactors. Effect of Axial Mixing (33)
- Stagewise Absorption and Extraction Equipment. Transient and Unsteady State Operation. (32)
- Statistical analysis of a reaction: Linear theory (32)
- Analysis of a model for a nonisothermal continuous fluidized bed catalytic reactor (32)
- Diffusion and reaction in a char particle and in the surrounding gas phase. A continuous model (32)
- Studies in char gasification-I A lumped model (32)
- Some observations on tubular reactor stability (32)
- Optimum temperature gradients in tubular reactors—II: Numerical study☆ (31)
- An analysis of an adiabatic adsorption column: Part II. Adiabatic adsorption of a single solute☆ (31)
- Maximum temperature rise in gas-solid reactions (30)
- An Analysis of an adiabatic adsorption column: Part III: Adiabatic adsorption of two solutes (29)
- Applications of Matrix Mathematics to Chemical Engineering Problems (28)
- Studies on the gasification of a single char particle (28)
- On optimum cross-current extraction (27)
- Dynamics of a single particle during char gasification (26)
- Fluidized Bed Gasification Reactor Modeling. 1. Model Description and Numerical Results for a Single Bed (26)
- Diffusing with Stefan and Maxwell (26)
- Intraparticle Diffusion in Catalytic Heterogeneous Systems (26)
- An analysis of chemical reactor stability and control—XI : Further considerations with polymerization models☆☆☆ (26)
- Stirred pots, tubular reactors, and self-adjoint operators (26)
- Mathematics in Chemical Engineering: A 50 Year Introspection (Journal Review) (25)
- Theory and application of single equations (25)
- On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part 1—Analytic solution of the equations for general mixtures (25)
- On a conjecture of Aris: Proof and remarks (25)
- Calculation of molecular weight distributions in polymerization (25)
- Qualitative and quantitative observations on the tubular reactor (24)
- An analysis of chemical reactor stability and control—XVI (23)
- Taylor diffusion in tubular reactors (23)
- Continuous models for polymerization (23)
- Stability of batch catalytic fluidized beds (22)
- Regeneration of Adiabatic Fixed Beds (22)
- Some general observations on tubular reactor stability (22)
- Stability of Nonadiabatic Packed Bed Reactors. Elementary Treatment (22)
- Dynamic behavior of a porous char particle burning in an oxygen‐containing environment: Part II: Transient analysis of a shrinking particle (22)
- An analysis of chemical reactor stability and control—Vb: Two-phase gas—liquid and concentrated liquid—liquid reacting systems in physical equilibrium—2 (22)
- Some observations on uniqueness and multiplicity of steady states in non‐adiabatic chemically reacting systems (22)
- Creeping reaction zone in a catalytic, fixed-bed reactor: a cell model approach (21)
- Analysis of Polymerization Kinetics and the Use of a Digital Computer (21)
- An analysis of chemical reactor stability and control—Xa: Polymerization models in two immiscible phases in physical equilibrium (20)
- An analysis of chemical reactor stability and control—VII : Two-phase chemical reacting systems with fast reactions (20)
- Primal-Dual Interior-Point Method for an Optimization Problem Related to the Modeling of Atmospheric Organic Aerosols (20)
- Fluidized bed char combustion diffusion limited models (20)
- Stability in distributed parameter systems (19)
- Analytical Solution for Simple Systems in Moving Bed Adsorbers (19)
- Diffusion and reaction in a char particle and in the surrounding gas phase. Two limiting models (19)
- Pulsed-power volume-heating chemical vapor infiltration (18)
- Asymptotic solution to moving-bed exchange equations (17)
- An analysis of chemical reactor stability and control—IX : Further investigations into the direct method of Lyapunov (17)
- Some problems concerning the non-adiabatic tubular reactor a-priori bounds, qualitative behavior, preliminary uniqueness and stability considerations (17)
- Transient dilation of bubbles and drops: Theoretical basis for dynamic interfacial measurements (17)
- Boundary value problems in transport with mixed and oblique derivative boundary conditions-II: Reduction to first order systems (17)
- Stability and control of addition polymerization reactions (17)
- An analysis of chemical reactor stability and control—VI : Two-phase chemical reacting systems with heat and mass transfer resistances (16)
- First-order partial differential equations with applications (16)
- The Rate-Determining Steps in Radial Adsorption Analysis (16)
- Modelling of fluidized bed reactors—V Combustion of carbon particles—an extension (16)
- Two Problems on Moving Beds (16)
- An analytical study of single particle char gasification (16)
- Nonlinear boundary-value problems arising in chemical reactor theory☆ (16)
- Modelling of fluidized bed reactors—II: Uniform catalyst temperature and concentration (15)
- Catalytic particle stability studies—III complex distributed resistances model☆ (15)
- Modelling of fluidized bed reactors—VI(b): The nonisothermal bed with stochastic bubbles (15)
- Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 3. Stability (15)
- Influence of Droplet Size-Age Distribution on Rate Processes in Dispersed-Phase Systems (15)
- On simple exchange waves in fixed beds (15)
- On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part 5. The extension to packed columns (14)
- A new atmospheric aerosol phase equilibrium model (UHAERO): organic systems (14)
- Boundary value problems in transport with mixed or oblique derivative boundary conditions—I: Formulation of equivalent integral equations (14)
- A Mathematical Model for Chemical Vapor Infiltration with Volume Heating (14)
- A dynamic optimization problem related to organic aerosols (13)
- Mathematical modelling of fluidized bed reactors—III: Axial dispersion model (13)
- Chemical vapor infiltration of SiC with microwave heating (13)
- An analysis of chemical reactor stability and control—XIII Segregated two phase systems (13)
- The non‐adiabatic tubular reactor: Stability considerations (13)
- Modelling of the Combustion of Single Char Particles (13)
- An analysis of an adiabatic adsorption column part IV: Adsorption in the high temperature range (13)
- Stability of adiabatic packed bed reactors. Effect of flow variations and coupling between the particles (12)
- An analysis of chemical reactor stability and control—IV.: Mixed derivative and proportional control (12)
- Combustion of coke deposits in a catalyst pellet (12)
- A phase equilibrium model for atmospheric aerosols containing inorganic electrolytes and organic compounds (UHAERO), with application to dicarboxylic acids (12)
- Global asymptotic stability in distributed parameter systems: comparison function approach (12)
- Studies in the control of tubular reactors—III stabilization by observer design (12)
- Primal-Dual Active-Set Algorithm for Chemical Equilibrium Problems Related to the Modeling of Atmospheric Inorganic Aerosols (11)
- Intraparticle effects in char combustion. III transient studies (11)
- The mathematical understanding of chemical engineering systems: Selected papers of Neal R. Amundson (11)
- On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part 3. Discussion of the numerical method of calculation (11)
- Studies in char gasification—III: The combustion zone (11)
- On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part IV. The calculation of the minimum reflux ratio (11)
- Fluidized bed char combustion kinetic models (11)
- Intraparticle effects in char combustion ii steady state analysis (10)
- Reduction of Powdered Iron Oxide - A Vertical-Flow Reactor (10)
- Fixed Beds with Large Particles (10)
- Chemical reactor theory: A review: dedicated to the memory of Richard H. Wilhelm (10)
- POLYMER MOLECULAR WEIGHT DISTRIBUTIONS (9)
- Boundary value problems in transport with mixed and oblique derivative boundary conditions, steady state and transient solutions (9)
- Transient behavior of single-phase natural-circulation loop systems (9)
- Catalytic particle stability studies—II Lumped thermal resistance model☆ (9)
- Studies in char gasification-II. The Davidson-Harrison two phase model of fluidization (9)
- The effect of recycle on a linear reactor (8)
- The inaugural P.V. Danckwerts memorial lecture presented at the Royal Society 12 May 1986 P.V. Danckwerts—his research career and its significance (8)
- Solution of Transient Stagewise Operations on an Analog Computer (8)
- Diffusion and reaction in a stagnant boundary layer about a carbon particle, part 7: Transient behavior and effect of water vapor (8)
- Single particle char combustion and gasification (8)
- Equilibrium Theory of Creeping Profiles in Fixed-Bed Catalytic Reactors (8)
- Diffusion and reaction in a stagnant boundary layer about a carbon particle. 8. Comparison of lumped and distributed chemical kinetics (8)
- Diffusion and Reaction in Carbon Burning (7)
- Mathematics of adsorption in beds. III. Radial flow. (7)
- Fluidized Bed Gasification Reactor Modeling. 2. Effect of the Residence Time Distribution and Mixing of the Particles. Staged Beds Modeling (7)
- Boundary value problems in transport with oblique and mixed derivative boundary conditions: More on steady state solutions (7)
- On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade: Part VI—The effect of variations of the relative volatilities, the flow rates and the plate efficiencies (7)
- The combustion behavior of retorted shale particles (6)
- Uniqueness of Steady State for an Isothermal Porous Catalyst (6)
- Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 4. The Dynamical Behavior (6)
- Equilibrium Theory of the Parametric Pump (6)
- Computational methods for the tubular chemical reactor (6)
- Reactor model assessment for the combustion of char in spouted beds of sand (6)
- Mathematics of adsorption in beds. II. (6)
- Preliminary report on burning of single particles of retorted shale (6)
- Canonical form and mathematical interpretation of electrolyte solution systems (6)
- Tubular reactor sensitivity (6)
- Self-adjoint operators from selected nonsymmetric matrices: application to kinetics and rectification (6)
- An analysis of chemical reactor stability and control—Xb (5)
- Interfacial viscoelastic response to oscillatory shear deformations (5)
- An Elementary Theory of Adsorption in Fluidized Beds. Mathematics of Adsorption in Beds. (5)
- Catalytic particle stability studies—I. Lumped resistance model (5)
- Maximal and minimal solutions, effectiveness factors for chemical reaction in porous catalysts (5)
- An analysis of chemical reactor stability and control—XII : Special problems in polymerization models☆☆☆ (5)
- On a mechanism for autocatalysis (5)
- An analysis of chemical reactor stability and sensitivity — XIV the effect of the steady state hypothesis (4)
- Mathematical models of fixed bed reactors (4)
- Shock layer analysis of adiabatic adsorption in fixed beds with axial dispersion (4)
- Local stability of tubular reactors (4)
- Multicomponent distillation on a large digital computer: II. Generalization with side‐stream stripping (4)
- Reduction of Powdered Iron Oxide - A Tubular Reactor (3)
- Some general considerations of reversible chemical reactions in batch and tubular reactors (3)
- Comments on the note by Mills (3)
- Reaction of a Continuous Mixture in a Bubbling Fluidized Bed (3)
- Interfacial surfactant concentrations on an oscillating droplet: solution of a singular boundary-initial value problem (3)
- A computationally efficient inorganic atmospheric aerosol phase equilibrium model (UHAERO) (3)
- Mathematical methods in chemical engineering, 2nd Edition, V. G. Jenson And G. Jeffreys, Academic Press (London), $19.50. Publication date: December, 1977, 599 pages (3)
- The Transient Behavior of Single-Phase Natural Circulation Water Loop Systems (3)
- A THEORETICAL STUDY OF THE TRANSIENT OPERATION AND STABILITY OF TWO-PHASE NATURAL CIRCULATION LOOPS (3)
- Studies in char gasification—IV: Multi-stage char gasifier (3)
- A Non-Self-Adjoint Problem in Heat Conduction (3)
- CHAR GASIFICATION: PARTICLE MODEL COMPARISON IN A STIRRED TANK REACTOR (2)
- A study of iterative optimization (2)
- Diffusion and reaction in a stagnant boundary layer about a carbon particle. 8a. Effect of the carbon dioxide reduction reaction (2)
- Polymerization Reactor Stability (2)
- Reaction, diffusion, and elementary functional analysis (2)
- Performance and Stability of Countercurrent Two-Phase Extractive Tublar Reactors (2)
- On Vibration Problems With Discretely Distributed Loads—A Rigorous Formalism (2)
- Pore structural effects in catalytic gasification of coal chars (2)
- RA of Minnesota (1)
- American University Graduate Work. (1)
- An analysis of chemical reactor stability and control-XV The multicomponent spray reactor (1)
- Diffusion in Catalytic Heterogeneous Systems: Studies in Vapor Phase Esterification (0)
- Modeling and Computation of Thermodynamic Equilibrium for Mixtures of Inorganic and Organic Species (0)
- Stabilization of unstable nonlinear distributed chemical reactors by observer design (0)
- Heat Transfer and Heat Release in Fluidized Beds (0)
- Interactive comment on “A computationally efficient inorganic atmospheric aerosol phase equilibrium model (UHAERO)” by N. R. Amundson et al (0)
- Studies in char gasification—III (0)
- Modelling of an Oil Shale Combustion Reactor: Particle Model Effects in an Idealized Fluidized Bed (0)
- Theory of Catalysis. (Book Reviews: The Mathematical Theory of Diffusion and Reaction in Permeable Catalysts Vol. 1, The Theory of the Steady State xvi, Vol. 2, Questions of Uniqueness, Stability, and Transient Behaviour) (0)
- BOUNDARY VALUE PROBLEMS IN TRANSPORT WITH MIXED AND OBLIQUE DERIVATIVE BOUNDARY CONDITIONS-II REDUCTION TO FIRST ORDER SYSTEMS DORAISWAhtI (0)
- Studies in char gasification-V: Ash recirculation model (0)
- Computational Methods for Multi-phase Multi-reaction Thermodynamical Equilibrium Problems (0)
- Modeling of Organic Effects on Aerosols Growth (0)
- Oral history interview with Neal R. Amundson (0)
- Micro-physical Consistent Modeling of the Deliquescence and Efflorescence Hysteresis (0)
- Rebirth as a Modern Program (0)
- More on oblique and mixed, second derivative boundary value problems (0)
- Diamond jubilee historical/review volume (0)
- CORRECTION- Stability of Adiabatic Packed Bed Reactors, an Elementary Treatment (0)
- JOURNAL REVIEW Mathematics in Chemical Engineering: A 50 Year Introspection (0)
- Modelling of fluidized bed reactors—VI(b): The nonisothermal bed with stochastic bubbles (0)

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