Neal Amundson

About

From 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 MinnesotaUniversity 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.

Published Works

• Mathematics of Adsorption in Beds. VI. The Effect of Longitudinal Diffusion in Ion Exchange and Chromatographic Columns
• An analysis of chemical reactor stability and control—I
• Chemical reactor stability and sensitivity
• Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle
• Some remarks on longitudinal mixing or diffusion in fixed beds
• Chemical reactor stability and sensitivity: II. Effect of parameters on sensitivity of empty tubular reactors
• A model for evaporation of a multicomponent droplet
• Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 2. An Extension
• A study of the shock layer in nonequilibrium exchange systems
• Uniqueness of the steady state solutions for chemical reactor occurring in a catalyst particle or in a tubular reaction with axial diffusion
Analysis of multicomponent separation by displacement development
An analysis of chemical reactor stability and control—II
Studies in the control of tubular reactors-I General Considerations
Some further observations on tubular reactor stability
Mathematics of Adsorption in Beds. V. Effect of Intra-particle Diffusion in Flow Systems in Fixed Beds
Shock layer in two solute chromatography: effect of axial dispersion and mass transfer
Solid-Fluid Interactions in Fixed and Moving Beds Fixed Beds with Small Particles
Some observations on tubular reactor stability
An analysis of an adiabatic adsorption column: Part 1. Theoretical development
Observations on fixed-bed dispersion models: The role of the interstitial fluid
Optimum temperature gradients in tubular reactors—I
Intraparticle diffusion and conduction in porous catalysts—I
Transport in composite materials: Reduction to a self adjoint formalism
Multicomponent Distillation Calculations on a Large Digital Computer
An analysis of chemical reactor stability and control—Va Two-phase systems in physical equilibrium—1
A single‐particle char gasification model
Creeping Profiles in Catalytic Fixed Bed Reactors. Continuous Models
A Note on the Mathematics of Adsorption in Beds
Some general observations on tubular reactor stability
Char gasification in a countercurrent reactor
Some observations on uniqueness and multiplicity of steady states in non-adiabatic chemically reacting systems
Stagewise Absorption and Extraction Equipment. Transient and Unsteady State Operation.
Stability in distributed parameter systems
An analysis of chemical reactor stability and control—III
Modelling of fluidized bed reactors—IV
An analysis of an adiabatic adsorption column: Part II. Adiabatic adsorption of a single solute
Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 6. Effect of Water Vapor on the Pseudo-Steady-State Structure
Stability of adiabatic packed bed reactors. Effect of flow variations and coupling between the particles
Qualitative and quantitative observations on the tubular reactor
Solid-Fluid Heat Exchange in Moving Beds
Effect of Intraparticle Diffusion: Agitated Nonflow Adsorption Systems
Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 5. Pseudo-Steady-State Structure and Parameter Sensitivity
Applications of Matrix Mathematics to Chemical Engineering Problems
Taylor diffusion in tubular reactors
Optimum temperature gradients in tubular reactors—II
Continuous models for polymerization
Stability of loop reactors
Analysis of a model for a nonisothermal continuous fluidized bed catalytic reactor
Mathematics of Adsorption. IV. Effect of Intraparticle Diffusion in Agitated Static Systems
On a conjecture of Aris: Proof and remarks
Stability of batch catalytic fluidized beds
Studies in char gasification—I A lumped model
Diffusion and reaction in a char particle and in the surrounding gas phase. A continuous model
Intraparticle Diffusion in Catalytic Heterogeneous Systems
Analysis of Polymerization Kinetics and the Use of a Digital Computer
Fluidized Bed Gasification Reactor Modeling. 1. Model Description and Numerical Results for a Single Bed
Maximum temperature rise in gas-solid reactions
Some problems concerning the non-adiabatic tubular reactor a-priori bounds, qualitative behavior, preliminary uniqueness and stability considerations
An Analysis of an adiabatic adsorption column
Creeping reaction zone in a catalytic, fixed-bed reactor: a cell model approach
Dynamics of a single particle during char gasification
Studies on the gasification of a single char particle
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
Nonlinear boundary-value problems arising in chemical reactor theory
Mathematics in chemical engineering: A 50 year introspection
Diffusing with Stefan and Maxwell
The non-adiabatic tubular reactor: Stability considerations
Asymptotic solution to moving-bed exchange equations
Analytical Solution for Simple Systems in Moving Bed Adsorbers
Pulsed-power volume-heating chemical vapor infiltration
An analysis of chemical reactor stability and control—Xa
Catalytic particle stability studies—III complex distributed resistances model
Modelling of fluidized bed reactors—II
Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 3. Stability
Fluidized bed char combustion diffusion limited models
Fixed Beds with Large Particles
Intraparticle diffusion and conduction in porous catalysts—II
An analytical study of single particle char gasification
Modelling of fluidized bed reactors—V Combustion of carbon particles—an extension
Two Problems on Moving Beds
Chemical vapor infiltration of SiC with microwave heating
An analysis of chemical reactor stability and control—XIII Segregated two phase systems
Mathematical modelling of fluidized bed reactors—III
Boundary value problems in transport with mixed or oblique derivative boundary conditions—I
Boundary value problems in transport with mixed and oblique derivative boundary conditions-II
An analysis of an adiabatic adsorption column part IV: Adsorption in the high temperature range
Global asymptotic stability in distributed parameter systems: comparison function approach
The Rate-Determining Steps in Radial Adsorption Analysis
POLYMER MOLECULAR WEIGHT DISTRIBUTIONS
Combustion of coke deposits in a catalyst pellet
Equilibrium Theory of Creeping Profiles in Fixed-Bed Catalytic Reactors
Intraparticle effects in char combustion steady state analysis
Catalytic particle stability studies—II Lumped thermal resistance model
Fluidized bed char combustion kinetic models
The Mathematics of Adsorption in Beds. III. Radial Flow. Leon,Lapidus
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
Studies in char gasification—II
Boundary value problems in transport with mixed and oblique derivative boundary conditions, steady state and transient solutions
Solution of Transient Stagewise Operations on an Analog Computer
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
The inaugural P.V. Danckwerts memorial lecture presented at the Royal Society 12 May 1986 P.V. Danckwerts—his research career and its significance
An optimization problem related to the modeling of atmospheric organic aerosols
A dynamic optimization problem related to organic aerosols
Tubular reactor sensitivity
The effect of recycle on a linear reactor
Self-adjoint operators from selected nonsymmetric matrices: application to kinetics and rectification
Modelling of fluidized bed reactors—VI(a)
Modelling of fluidized bed reactors—VI(b)
Single particle char combustion and gasification
Diffusion and reaction in a stagnant boundary layer about a carbon particle. 8. Comparison of lumped and distributed chemical kinetics
Fluidized Bed Gasification Reactor Modeling. 2. Effect of the Residence Time Distribution and Mixing of the Particles. Staged Beds Modeling
Local stability of tubular reactors
Some general considerations of reversible chemical reactions in batch and tubular reactors
Intraparticle effects in char combustion II. Steady state analysis
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
Catalytic particle stability studies—I. Lumped resistance model
Studies in the control of tubular reactors—III stabilization by observer design
Studies in char gasification—III
Boundary value problems in transport with oblique and mixed derivative boundary conditions
An Elementary Theory of Adsorption in Fluidized Beds. Mathematics of Adsorption in Beds.
A study of iterative optimization
Diffusion and reaction in a stagnant boundary layer about a carbon particle, part 7: Transient behavior and effect of water vapor
Intraparticle effects in char combustion. III transient studies
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
On the steady state fractionation of multicomponent and complex mixtures in an ideal cascade
An analysis of chemical reactor stability and sensitivity — XIV the effect of the steady state hypothesis
Preliminary report on burning of single particles of retorted shale
An optimization problem related to the modeling of atmospheric inorganic aerosols
Diffusion and Reaction in a Stagnant Boundary Layer about a Carbon Particle. 4. The Dynamical Behavior
Canonical form and mathematical interpretation of electrolyte solution systems
Maximal and minimal solutions, effectiveness factors for chemical reaction in porous catalysts
The combustion behavior of retorted shale particles
Reactor model assessment for the combustion of char in spouted beds of sand
An analysis of chemical reactor stability and control—XVI
Diffusion and Reaction in Carbon Burning
Studies in char gasification—IV
Interfacial surfactant concentrations on an oscillating droplet: Solution of a singular boundary-initial value problem
Shock layer analysis of adiabatic adsorption in fixed beds with axial dispersion
Diffusion and reaction in a stagnant boundary layer about a carbon particle. 8a. Effect of the carbon dioxide reduction reaction
Quasilinear hyperbolic systems and waves, Alan Jeffrey, Pitman Publishing, London, 230 pages,$ 6.90
Intraparticle effects in char combustion ii steady state analysis
Reaction and Diffusion in Carbon Combustion
Mathematical methods in chemical engineering, 2nd Edition, V. G. Jenson And G. Jeffreys, Academic Press(London),$19.50. Publication date: December, 1977, 599 pages
An analysis of chemical reactor stability and control-XV The multicomponent spray reactor
Studies in char gasification-V
LETTERS
CORRECTION- Stability of Adiabatic Packed Bed Reactors, an Elementary Treatment
Heat Transfer and Heat Release in Fluidized Beds
Modelling of an Oil Shale Combustion Reactor: Particle Model Effects in an Idealized Fluidized Bed
MORE ON OBLIQUE AND MIXED, SECOND DERIVATIVE BOUNDARY VALUE PROBLEMS
Erratum
Diffusion in Catalytic Heterogeneous Systems: Studies in Vapor Phase Esterification
DIFFUSION IN CATALYTIC HETEROGENEOUS SYSTEMS - STUDIES IN VAPOR PHASE ESTERIFICATION
More Less

Other Resources

• en.wikipedia.org

Schools

University of Houston

State research university in Houston, Texas, United States

View profile

University of Minnesota

Public research university in Minneapolis and Saint Paul, Minnesota, United States

View profile

Influence Rankings by Discipline