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Kari Keskinen

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Papers by Kari Keskinen

Research paper thumbnail of Two-Stage Gas Washing Method Applying Sulfide Precipitation and Alkaline Absorption

Research paper thumbnail of Vapor–liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method

Fluid Phase Equilibria, 2013

ABSTRACT Isothermal vapor-liquid equilibrium (VLE) of three binary mixtures was measured with a s... more ABSTRACT Isothermal vapor-liquid equilibrium (VLE) of three binary mixtures was measured with a static total pressure apparatus: dimethylsulfide +ethanol at 350.4K, +dimethylether at 336.7K, +methylacetate at 350.3 K. The Barker method was used to convert the total pressure and total composition measurements into vapor-liquid equilibrium data. Legendre polynomial and Wilson model were used as the liquid activity coefficient model to obtain the compositions of the vapor and liquid phases. All systems exhibited positive deviation from Raoult's law. The dimethylsulfide + ethanol system showed azeotropic behavior (x(1az) = 0.058, T-az = 350.4 K, P-az = 341.9 kPa).

Research paper thumbnail of Vapor–Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol

Journal of Chemical & Engineering Data, 2013

ABSTRACT The isothermal vapor–liquid equilibrium (VLE) of binary systems of methoxymethane (dimet... more ABSTRACT The isothermal vapor–liquid equilibrium (VLE) of binary systems of methoxymethane (dimethylether, DME) + thiophene, DME + 2-methylpropane-2-thiol, and DME + diethylsulfide was measured with a static total pressure apparatus. Barker’s method was used to obtain phase equilibrium data from the total pressure measurements. Additionally 5 VLE data points of the binary system of 1-hexene + 1-propanethiol were measured with a glass recirculation still. The system reacted partly during the VLE measurements to form a sulfide at thiol mole fractions higher than x(1-propanethiol) = 0.1. The formation of the sulfide was verified by gas chromatographic analysis. The measured nonreacted points at low thiol concentration showed that the system 1-hexene + 1-propanethiol exhibited azeotropic behavior.

Research paper thumbnail of Vapour–liquid equilibrium for the ethyl ethanoate+1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane

Fluid Phase Equilibria, 2005

Isothermal vapour–liquid equilibrium was measured for ethyl ethanoate+ 1-butene,+ cis-2-butene,+ ... more Isothermal vapour–liquid equilibrium was measured for ethyl ethanoate+ 1-butene,+ cis-2-butene,+ trans-2-butene,+ 2-methylpropene,+ n-butane and+ 2-methylpropane at 318.4 K with an automated static total pressure measurement apparatus. The experimental data ...

Research paper thumbnail of Isothermal binary vapour–liquid equilibrium for butanes and butenes with dimethylsulphide

Fluid Phase Equilibria, 2008

Isothermal vapour–liquid equilibrium was measured for dimethylsulphide+ 1-butene (312.58 K), dime... more Isothermal vapour–liquid equilibrium was measured for dimethylsulphide+ 1-butene (312.58 K), dimethylsulphide+ cis-2-butene (312.59 K), dimethylsulphide+ trans-2-butene (317.30 K), dimethylsulphide+ 2-methylpropene (312.60 K), dimethylsulphide+ n-butane (317.41 K ...

Research paper thumbnail of Analysis of a gas flow in structured packed bed columns using CFD

Research paper thumbnail of Process for preparing a diesel fuel fraction by oligomerisation

Research paper thumbnail of Optimization of an ethanol-from-biomass process

Research paper thumbnail of Kemian laitetekniikan taulukoita ja piirroksia

Research paper thumbnail of Studies on Computer Aided Modelling, Simulation and Optimization in Process Development

Research paper thumbnail of Laboratory Polymerization Data in Planning Plant Operation - a Case Study

Research paper thumbnail of Fuzzy Simulations with Program IFTHEN

Research paper thumbnail of An Energy Self-Sufficient Continuous Process for Production of Ethanol from Biomass and Municipal Solid Waste

Research paper thumbnail of Representation of Uncertain or Qualitative Data and Knowledge by Linguistic and Fuzzy Models

Research paper thumbnail of On the Importance of the Selection of the Thermodynamic Model in Chemical Process Simulation

Research paper thumbnail of Sidechain alkylation of toluene by propene

Research paper thumbnail of Process and Reactor System for Oligomerization of Olefins

Research paper thumbnail of Distributed Genetic Algorithm for Fitting of Model Parameters of Chemical Reaction Kinetics

Research paper thumbnail of Design Aspects for Distillation of a Close Boiling Organic Mixture: Propane/Propene as an Example

Research paper thumbnail of Modelling of a configuration combining distillation and reaction in a side-reactor

Research paper thumbnail of Two-Stage Gas Washing Method Applying Sulfide Precipitation and Alkaline Absorption

Research paper thumbnail of Vapor–liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method

Fluid Phase Equilibria, 2013

ABSTRACT Isothermal vapor-liquid equilibrium (VLE) of three binary mixtures was measured with a s... more ABSTRACT Isothermal vapor-liquid equilibrium (VLE) of three binary mixtures was measured with a static total pressure apparatus: dimethylsulfide +ethanol at 350.4K, +dimethylether at 336.7K, +methylacetate at 350.3 K. The Barker method was used to convert the total pressure and total composition measurements into vapor-liquid equilibrium data. Legendre polynomial and Wilson model were used as the liquid activity coefficient model to obtain the compositions of the vapor and liquid phases. All systems exhibited positive deviation from Raoult's law. The dimethylsulfide + ethanol system showed azeotropic behavior (x(1az) = 0.058, T-az = 350.4 K, P-az = 341.9 kPa).

Research paper thumbnail of Vapor–Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol

Journal of Chemical & Engineering Data, 2013

ABSTRACT The isothermal vapor–liquid equilibrium (VLE) of binary systems of methoxymethane (dimet... more ABSTRACT The isothermal vapor–liquid equilibrium (VLE) of binary systems of methoxymethane (dimethylether, DME) + thiophene, DME + 2-methylpropane-2-thiol, and DME + diethylsulfide was measured with a static total pressure apparatus. Barker’s method was used to obtain phase equilibrium data from the total pressure measurements. Additionally 5 VLE data points of the binary system of 1-hexene + 1-propanethiol were measured with a glass recirculation still. The system reacted partly during the VLE measurements to form a sulfide at thiol mole fractions higher than x(1-propanethiol) = 0.1. The formation of the sulfide was verified by gas chromatographic analysis. The measured nonreacted points at low thiol concentration showed that the system 1-hexene + 1-propanethiol exhibited azeotropic behavior.

Research paper thumbnail of Vapour–liquid equilibrium for the ethyl ethanoate+1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane

Fluid Phase Equilibria, 2005

Isothermal vapour–liquid equilibrium was measured for ethyl ethanoate+ 1-butene,+ cis-2-butene,+ ... more Isothermal vapour–liquid equilibrium was measured for ethyl ethanoate+ 1-butene,+ cis-2-butene,+ trans-2-butene,+ 2-methylpropene,+ n-butane and+ 2-methylpropane at 318.4 K with an automated static total pressure measurement apparatus. The experimental data ...

Research paper thumbnail of Isothermal binary vapour–liquid equilibrium for butanes and butenes with dimethylsulphide

Fluid Phase Equilibria, 2008

Isothermal vapour–liquid equilibrium was measured for dimethylsulphide+ 1-butene (312.58 K), dime... more Isothermal vapour–liquid equilibrium was measured for dimethylsulphide+ 1-butene (312.58 K), dimethylsulphide+ cis-2-butene (312.59 K), dimethylsulphide+ trans-2-butene (317.30 K), dimethylsulphide+ 2-methylpropene (312.60 K), dimethylsulphide+ n-butane (317.41 K ...

Research paper thumbnail of Analysis of a gas flow in structured packed bed columns using CFD

Research paper thumbnail of Process for preparing a diesel fuel fraction by oligomerisation

Research paper thumbnail of Optimization of an ethanol-from-biomass process

Research paper thumbnail of Kemian laitetekniikan taulukoita ja piirroksia

Research paper thumbnail of Studies on Computer Aided Modelling, Simulation and Optimization in Process Development

Research paper thumbnail of Laboratory Polymerization Data in Planning Plant Operation - a Case Study

Research paper thumbnail of Fuzzy Simulations with Program IFTHEN

Research paper thumbnail of An Energy Self-Sufficient Continuous Process for Production of Ethanol from Biomass and Municipal Solid Waste

Research paper thumbnail of Representation of Uncertain or Qualitative Data and Knowledge by Linguistic and Fuzzy Models

Research paper thumbnail of On the Importance of the Selection of the Thermodynamic Model in Chemical Process Simulation

Research paper thumbnail of Sidechain alkylation of toluene by propene

Research paper thumbnail of Process and Reactor System for Oligomerization of Olefins

Research paper thumbnail of Distributed Genetic Algorithm for Fitting of Model Parameters of Chemical Reaction Kinetics

Research paper thumbnail of Design Aspects for Distillation of a Close Boiling Organic Mixture: Propane/Propene as an Example

Research paper thumbnail of Modelling of a configuration combining distillation and reaction in a side-reactor

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