Wolfram Demonstrations Project
Brian G. Higgins
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Demonstrations 61 - 80 of 95
Excess Enthalpy and Heat Capacity for an Ethanol-Water MixtureSimple Batch Distillation of an Ethanol-Water MixtureVapor-Liquid Equilibrium for an Ethanol-Water MixtureImpulse Response of Two and Three Continuous Stirred-Tank Reactors in Series: Exact and Approximate SolutionsEdgeworth Expansion for Near-Normal Data
Excess Enthalpy and Heat Capacity for an Ethanol-Water Mixture
Simple Batch Distillation of an Ethanol-Water Mixture
Vapor-Liquid Equilibrium for an Ethanol-Water Mixture
Impulse Response of Two and Three Continuous Stirred-Tank Reactors in Series: Exact and Approximate Solutions
Edgeworth Expansion for Near-Normal Data
Particle Position Distribution Using a Brownian Dynamic SimulationIntegral Evaluation Using the Monte Carlo MethodThermodynamic Properties of Acetylene Using Cubic Equations of StateFisher-Kolmogoroff EquationSolution of the Laplace Equation Using Coordinates Fitted to the Boundary Conditions
Particle Position Distribution Using a Brownian Dynamic Simulation
Integral Evaluation Using the Monte Carlo Method
Thermodynamic Properties of Acetylene Using Cubic Equations of State
Fisher-Kolmogoroff Equation
Solution of the Laplace Equation Using Coordinates Fitted to the Boundary Conditions
Transient Heat Conduction with Temperature-Dependent Thermal ConductivityBreaking the Azeotrope between Cyclohexane and Benzene Using AnilineLocus of a Pressure-Sensitive Binary AzeotropeLocus of Binary and Ternary Azeotropes in Chloroform-Methanol-Acetone MixtureFanning Friction Factor for Smooth and Rough Pipes
Transient Heat Conduction with Temperature-Dependent Thermal Conductivity
Breaking the Azeotrope between Cyclohexane and Benzene Using Aniline
Locus of a Pressure-Sensitive Binary Azeotrope
Locus of Binary and Ternary Azeotropes in Chloroform-Methanol-Acetone Mixture
Fanning Friction Factor for Smooth and Rough Pipes
Start-up of Poiseuille Flow in a Newtonian FluidConcentration and Temperature Profiles in an Axially Dispersed Adiabatic Tubular ReactorReaction-Diffusion in a Drop Using Orthogonal CollocationSolving Stefan-Maxwell Equations Using Orthogonal Collocation and Shooting MethodMass Transfer with Reaction in a Spherical Drop
Start-up of Poiseuille Flow in a Newtonian Fluid
Concentration and Temperature Profiles in an Axially Dispersed Adiabatic Tubular Reactor
Reaction-Diffusion in a Drop Using Orthogonal Collocation
Solving Stefan-Maxwell Equations Using Orthogonal Collocation and Shooting Method
Mass Transfer with Reaction in a Spherical Drop

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