Kiyofumi Kurihara

发表

Computer-aided reverse design for ionic liquids by QSPR using descriptors of group contribution type for ionic conductivities and viscosities

Hiroshi Yamamoto, Hiroyuki Matsuda, Hiroshi M. Yamamoto, 2007 .

Separation Effects of Renewable Solvent Ethyl Lactate on the Vapor–Liquid Equilibria of the Methanol + Dimethyl Carbonate Azeotropic System

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2017 .

Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2015 .

Liquid–Liquid Equilibria for Extraction of Citrus Essential Oil Using Ionic Liquids

Miwa Kawai, K. Tochigi, Hiroyuki Matsuda, 2014, Journal of Solution Chemistry.

Estimation of NRTL Parameters Using Auto Vapor^|^#8211;Liquid Equilibrium Measuring Equipment and Application of Distillate Curve Map to Batch Distillation

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2013 .

Determination of ASOG Parameters for Selecting Azeotropic Mixtures Containing Hydrofluoroethers

K. Otake, S. Urata, K. Tochigi, 2002 .

Prediction of The Ionic Conductivity and Viscosity of Ionic Liquids by QSPR Using Descriptors of Group Contribution Type

Hiroshi Yamamoto, Hiroyuki Matsuda, Hiroshi M. Yamamoto, 2007 .

Thermophysical Properties of Ionic Liquid Systems and Their Applications

K. Tochigi, Shigeki Takishima, Hiroyuki Matsuda, 2014 .

Prediction of Thermophysical Properties Using Polynomial Expansion Equation and Genetic Algorithm

Y. Takahashi, K. Tochigi, Hiroyuki Matsuda, 2012 .

Isobaric vapor-liquid equilibria for acetone + chloroform + benzene and the three constituent binary systems

Kazuo Kojima, K. Kojima, K. Tochigi, 1991 .

Vapor−Liquid Equilibrium Data for the Quaternary System Acetone + Chloroform + Methanol + Benzene at 101.3 kPa

K. Kojima, Kiyofumi Kurihara, K. Ochi, 2000 .

High-Pressure Vapor−Liquid and Solid−Gas Equilibria Using a Peng−Robinson Group Contribution Method

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1998 .

Prediction of vapor–liquid equilibrium for systems containing hydrofluoroethers using ASOG group contribution method

T. Sako, K. Tochigi, Kiyofumi Kurihara, 2001 .

Mixing rule containing regular-solution and residual excess free energy.

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1987 .

Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1–C4) and dimethyl carbonate

S. Kikkawa, J. Gmehling, D. Constantinescu, 2012 .

Isobaric Vapor–Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2012 .

Determination and correlation of vapor–liquid equilibrium for binary systems consisting of close-boiling components

K. Kojima, Kiyofumi Kurihara, K. Ochi, 2007 .

Vapor-liquid equilibrium data for the binary decafluoropentane (HFC-43-10meec) + heptane, decafluoropentane + butyl ethyl ether, octafluorobutane (HFC-338pcc) + butyl ethyl ether, and heptafluoro propyl methyl ether (HFE-347mcc) + HFC-338pcc systems at 101.3 kPa

K. Tochigi, Kiyofumi Kurihara, J. Mizukado, 2005 .

Vapor−Liquid Equilibrium Data for Methanol + 1,3-Dioxolane + Water and Constituent Binary Systems at 101.3 kPa

K. Kojima, Kiyofumi Kurihara, K. Ochi, 2003 .

Vapor−Liquid Equilibrium Data for the Six Binaries Heptafluoropropyl Methyl Ether (HFE-347mcc) or 1,1,1,2,3,3-Hexafluoro-3-propane (HFE-449mec-f) with 1-Propanol, 2-Butanone, or Ethyl Acetate

K. Otake, K. Tochigi, Kiyofumi Kurihara, 2002 .

An implicit type EOS-GE(VP) model employing vapor pressure standard state I. Prediction of high-pressure vapor-liquid equilibria based on low temperature data

K. Kojima, Kiyofumi Kurihara, 1995 .

Prediction of ternary vapor-liquid equilibria by mixing rule containing regular solution and residual excess free energy terms

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1988 .

Solid–liquid equilibria for selected binary systems containing diphenyl carbonate

Y. Ohashi, K. Tochigi, Hiroyuki Matsuda, 2019, Fluid Phase Equilibria.

Determination of Vapor–Liquid Equilibria at Elevated Pressures Using Ebulliometer

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2016 .

Determination and correlation of liquid–liquid equilibria for nine binary acetonitrile+ n- alkane systems

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2011 .

Solid−Liquid Equilibria in Three Binary Mixtures Containing Diphenyl Carbonate

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2011 .

Measurement of Vapor–Liquid Equilibria for Binary Systems Using a Hold-Up Compensable Ebulliometer

S. Kikkawa, K. Tochigi, Hiroyuki Matsuda, 2007 .

Determination of NRTL Parameters for Aqueous Solutions using a Vapor Hold-Up Compensable Ebulliometer

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2007 .

Liquid-Liquid Solubilities for the Binary Systems of Methanol with Octane and 2, 2, 4-Trimethylpentane

K. Kojima, Kiyofumi Kurihara, K. Ochi, 2002 .

Measurement and correlation of excess molar enthalpies for the partially miscible systems 2-butanone+water and methanol+hexane

K. Kojima, Kiyofumi Kurihara, K. Ochi, 2001 .

Measurement and correlation of excess molar enthalpies for the 2-butanol+water and methanol+cyclohexane systems with limited miscibility at 283.15, 288.15 and 298.15 K

K. Kojima, Kiyofumi Kurihara, K. Ochi, 1998 .

Determination and correlation of LLE and SLE data for the system aniline+cyclohexane

K. Kojima, Kiyofumi Kurihara, K. Ochi, 1997 .

An implicit type EOS-GE(VP) model employing vapor pressure standard state. II. Prediction of excess enthalpy using the EOS-GE model

K. Kojima, Kiyofumi Kurihara, 1995 .

COMPUTER-AIDED MOLECULAR DESIGN FOR VISCOSITIES AND MELTING POINTS OF IONIC LIQUIDS

Hiroshi M. Yamamoto, K. Tochigi, Hiroyuki Matsuda, 2006 .

Prediction of liquid-liquid equilibria at high pressure for binary systems using EOS-GE models: methanol + hydrocarbon systems

K. Kojima, Hiroyuki Matsuda, Kiyofumi Kurihara, 2002 .

Measurement and prediction of activity coefficients of solvents in polymer solutions using gas chromatography and a cubic-perturbed equation of state with group contribution

K. Tochigi, Kiyofumi Kurihara, K. Ochi, 2005 .

PREDICTION OF PHASE EQUILIBRIA FOR THE SYSTEMS CONTAINING AMMONIA USING PRASOG

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1998 .

Prediction of VLE using ASOG and zero pressure GE mixing rule consistent the second virial coefficient condition

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1995 .

Measurement and prediction of high-pressure vapor–liquid equilibria for binary mixtures of carbon dioxide + n-octane, methanol, ethanol, and perfluorohexane

M. C. Ramos, C. McCabe, K. Tochigi, 2010 .

Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2009 .

Evaluation of thermodynamic consistency of isobaric and isothermal binary vapor–liquid equilibrium data using the PAI test II, alcohol + n-alkane, +aromatic, +cycloalkane systems

Kazuo Kojima, Yusuke Egawa, K. Kojima, 2007 .

Determination and correlation of solubilities of famotidine in water + co-solvent mixed solvents

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2011 .

Prediction of Antoine constants using a group contribution method

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2010 .

The calculation of excess molar enthalpies of liquid mixtures at high pressures and temperatures from measurements at ambient conditions

K. Kojima, Wenbin Dai, Hiroyuki Matsuda, 2004 .

Excess molar enthalpies for binary carbon dioxide + diethyl carbonate system at 298.15–308.15 K and 5.0–6.5 MPa

Hiroyuki Matsuda, Kiyofumi Kurihara, K. Ochi, 2005 .

Excess Molar Enthalpies of the Binary Carbon Dioxide + Dimethyl Carbonate System at Temperatures of (298.15 to 308.15) K and Pressures of (5.0 to 7.5) MPa

Hiroyuki Matsuda, Kiyofumi Kurihara, K. Ochi, 2005 .

Liquid–liquid equilibria containing fluorous solvents as environmentally benign solvent

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2013 .

Excess molar enthalpies of the binary system carbon dioxide + butyl levulinate at 298.15 and 303.15 K and 5.0–7.0 MPa

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2019 .

Determination and correlation of heat of mixing of the carbon dioxide + tert-butyl methyl ether system at 298.15 and 303.15 K and 5.0–7.0 MPa

Tomohiro Kobayashi, K. Tochigi, Hiroyuki Matsuda, 2016 .

Determination and correlation of excess molar enthalpies of the binary carbon dioxide+ethyl acetate system at 298.15 to 308.15K and 5.0 to 7.0MPa

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2014 .

Determination and correlation of liquid–liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems

K. Kojima, Hiroyuki Matsuda, Kiyofumi Kurihara, 2007 .

Isothermal Vapor-Liquid Equilibria for Methanol + Ethanol + Water, Methanol + Water, and Ethanol + Water

K. Kojima, Kiyofumi Kurihara, T. Minoura, 1995 .

Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbo

J. Gmehling, D. Constantinescu, K. Tochigi, 2011 .

Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2016 .

Estimation of kinematic viscosities and thermal conductivities for liquid mixtures using ASOG-VLE, ASOG-VISCO and ASOG-ThermConduct models

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2022, Fluid Phase Equilibria.

Estimation of kinematic viscosities for multi-component systems using modified Eyring and activity coefficient model

K. Tochigi, V. K. Rattan, Hiroyuki Matsuda, 2019, Fluid Phase Equilibria.

Isothermal Vapor−Liquid Equilibria for Benzene + Cyclohexane + 1-Propanol and for Three Constituent Binary Systems

K. Kojima, Kiyofumi Kurihara, Masanori Uchiyama, 1997 .

Prediction of solubilities of pharmaceutical compounds in water + co-solvent systems using an activity coefficient model

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2010 .

Evaluation of thermodynamic consistency of isobaric and isothermal binary vapor–liquid equilibrium data using the PAI test

Kazuo Kojima, Yusuke Egawa, K. Kojima, 2004 .

Determination of valley and ridge of isobaric vapor–liquid equilibrium for ternary system

K. Kojima, K. Tochigi, Hiroyuki Matsuda, 2007 .

Measurement and correlation of excess molar enthalpies for the systems containing supercritical carbon dioxide and alcohols

K. Kojima, Wenbin Dai, Kiyofumi Kurihara, 2002 .

Ebulliometric Determination and Prediction of Vapor–Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate

H. Yamada, K. Tochigi, Hiroyuki Matsuda, 2011 .

Estimation of kinematic viscosities at high pressures for binary mixtures CO2 + solvent using modified Eyring–Wilson and McAllister models

K. Tochigi, V. K. Rattan, Hiroyuki Matsuda, 2019, Molecular Physics.

Estimation of kinematic viscosities for CO2 expanded liquids by ASOG-VISCO model

K. Tochigi, V. K. Rattan, Hiroyuki Matsuda, 2018, Fluid Phase Equilibria.

Isobaric vapor-liquid equilibria for methanol + ethanol + water and the three constituent binary systems

Kazuo Kojima, K. Kojima, Kiyofumi Kurihara, 1993 .

Vapor-liquid equilibria for binary systems carbon dioxide + 1,1,1,2,3,3-hexafluoro-3-(2,2,2-trifluoroethoxy)propane or 1-ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane at 303.15–323.15 K

C. McCabe, T. Tsuji, K. Tochigi, 2020 .

Vapor−Liquid Equilibria for Acetone + Chloroform + Methanol and Constituent Binary Systems at 101.3 kPa

K. Kojima, Kiyofumi Kurihara, T. Hiaki, 1994 .

Isobaric Vapor−Liquid Equilibria for Tetrahydropyran and Alcohol Systems

Satoru Kato, Y. Miyano, K. Tochigi, 2008 .

Estimation of Thermal Conductivities for Binary and Ternary Liquid Mixtures Using Excess Thermal Conductivity Model

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2022, Journal of Solution Chemistry.

Measurement of Isobaric Vapor–Liquid Equilibria for Binary Systems Containing Tetrahydrofuran Using an Automatic Apparatus

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2011 .

Excess molar enthalpies in the binary system of carbon dioxide + ethyl lactate at 298.15 and 303.15 K and 5.0–7.0 MPa

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2023, Fluid Phase Equilibria.

PREDICTION OF HIGH PRESSURE VAPOR-LIQUID EQUILIBRIA WITH MIXING RULE USING ASOG GROUP CONTRIBUTION METHOD

K. Kojima, K. Tochigi, Kiyofumi Kurihara, 1985 .

Catalytic transfer hydrogenation of cellulose to hydrocarbons using straight-chain aliphatic hydrocarbon as a solvent

Yusuke Kakuta, Kiyofumi Kurihara, Kentaro Kimura, 2021 .

Catalytic transfer hydrogenation of cellulose to hydrocarbons using straight-chain aliphatic hydrocarbon as a solvent

Yusuke Kakuta, Kiyofumi Kurihara, Kentaro Kimura, 2021, Biomass Conversion and Biorefinery.

Study of Multi-Component Batch Distillation Calculation with Parameters Estimated Using Simple Distillation

K. Tochigi, Hiroyuki Matsuda, Kiyofumi Kurihara, 2011 .

Effect of formation behavior of hydrocarbons and solid component from cellulose on catalytic transfer hydrogenation in straight-chain aliphatic hydrocarbon solvent

Yusuke Kakuta, Kiyofumi Kurihara, Kentaro Kimura, 2021, Biomass Conversion and Biorefinery.

Isothermal vapor–liquid equilibria at 383.15–413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point

J. Gmehling, D. Constantinescu, K. Tochigi, 2019, Fluid Phase Equilibria.