Search Results - "Hiaki, T."
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Thermodynamic stabilization of semiclathrate hydrates by hydrophilic group
Published in RSC advances (01-01-2017)“…Introducing hydrophilic groups into carboxylates is a way to modify semiclathrate hydrate frameworks and change the properties of the hydrates. In this study,…”
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Isothermal Vapor−Liquid Equilibria for the 2-Propanol + Water System Containing Poly(ethylene glycol) at 298.15 K
Published in Journal of chemical and engineering data (12-09-1996)“…Isothermal vapor−liquid equilibrium measurements were performed for the 2-propanol + water system containing poly(ethylene glycol) (PEG) at 298.15 K by a flow…”
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Isobaric Vapor−Liquid Equilibria of Octane + 1-Butanol, +2-Butanol, and +2-Methyl-2-propanol at 101.3 kPa
Published in Journal of chemical and engineering data (1996)“…Isobaric vapor−liquid equilibria were measured for three binary systems of 1-butanol + octane, 2-butanol + octane, and 2-methyl-2-propanol + octane at 101.3…”
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Measurements of bubble point pressure for CO2 + decane and CO2 + lubricating oil
Published in Fluid phase equilibria (10-05-2004)Get full text
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Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
Published in Fluid phase equilibria (01-02-2005)“…A synthetic type apparatus was designed to measure hydrogen solubility in four pure aromatic or cyclic hydrocarbons, benzene, cyclohexane, toluene, and…”
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Measuring methods of infinite dilution activity coefficients and a database for systems including water
Published in Fluid phase equilibria (15-05-1997)“…Experimental techniques for the determination of infinite dilution activity coefficients and their improvements are reviewed. Generally, the measuring…”
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Prediction of vapor–liquid equilibrium for binary systems containing HFEs by using artificial neural network
Published in Fluid phase equilibria (30-06-2002)“…A method using artificial neural network (ANN) was applied to estimate the vapor–liquid equilibrium (VLE) for the binary systems containing hydrofluoroethers…”
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Vapor–liquid equilibria determination for a hydrofluoroether with several alcohols
Published in Fluid phase equilibria (01-06-1999)Get full text
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Permeation Model of Hydrocarbon Gases in Poly(4-methyl-1-pentene) Film Using Cubic Equation of State and Concentration-Dependent Diffusion Equation
Published in Industrial & engineering chemistry research (21-07-2004)“…Gas permeation rates were measured for poly(4-methyl-1-pentene) (PMP) supported on an aluminum oxide film at temperatures from 298 to 423 K. The permeate gases…”
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One-Pot Synthesis of Nickel Particles in Supercritical Water
Published in Industrial & engineering chemistry research (18-01-2006)“…Nickel particles were directly synthesized from 0.1 mol/kg nickel formate aqueous solution in supercritical water at 673 K and 30 MPa for 3−30 min with a…”
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Vapor Pressures of Hydrofluoroethers
Published in Journal of chemical and engineering data (01-07-2002)“…Vapor pressures for 50 hydrofluoroethers have been measured from pressures of less than 30 kPa to 101.3 kPa. Measurements were made by the isoteniscope method…”
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Synthesis of Ni–Cu Particles by Hydrogen Reduction in Hot-compressed Water
Published in Chemistry letters (01-01-2006)“…Synthesis of Cu and Ni–Cu particles from their aqueous formate solution by hydrogen reduction in hot-compressed water was carried out at 673 K with a titanium…”
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Vapor–liquid equilibria for bis(2,2,2-trifluoroethyl)ether with several organic compounds containing oxygen
Published in Fluid phase equilibria (25-09-2000)“…Isobaric vapor–liquid equilibria for bis(2,2,2-trifluoroethyl)ether+alcohols, ketones, or esters systems were measured at 101.3kPa. The alcohols used are…”
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Prediction of infinite dilution activity coefficients for systems including water based on the group contribution model with mixture-type groups: II. Extension and application
Published in Fluid phase equilibria (30-04-2002)“…Group contribution models such as ASOG or UNIFAC were known to be inaccurate in the prediction of infinite dilution activity coefficients ( γ ∞) for most of…”
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Vapor–liquid equilibria for 1,1,2,3,3,3-hexafluoropropyl, 2,2,2-trifluoroethyl ether with several organic solvents
Published in Fluid phase equilibria (30-03-2002)“…The isobaric vapor–liquid equilibria (VLE) for the binary systems 1,1,2,3,3,3-hexafluoropropyl, 2,2,2-trifluoroethyl ether (HFE-449mec-f), i.e. CF 3CHFCF 2OCH…”
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Isobaric Vapor−Liquid Equilibria for 2-Methoxy-2-methylpropane + Ethanol + Octane and Constituent Binary Systems at 101.3 kPa
Published in Journal of chemical and engineering data (11-03-1999)“…Isobaric vapor−liquid equilibria for 2-methoxy-2-methylpropane (MTBE) + ethanol + octane and for the constituent binary systems MTBE + ethanol and MTBE +…”
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Isobaric Vapor−Liquid Equilibria for Binary and Ternary Systems Composed of 2-Methoxy-2-methylpropane, Ethanol, 2-Methyl-2-propanol, and Octane at 101.3 kPa
Published in Journal of chemical and engineering data (01-07-2000)“…Isobaric vapor−liquid equilibria for two ternary systems, 2-methoxy-2-methylpropane (MTBE) + ethanol + 2-methyl-2-propanol and ethanol + 2-methyl-2-propanol +…”
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Vapor–liquid equilibria for 1,1,2,2-tetrafluoroethyl, 2,2,2-trifluoroethyl ether with several organic compounds containing oxygen
Published in Fluid phase equilibria (05-06-2001)“…Isobaric vapor–liquid equilibria for 1,1,2,2-tetrafluoroethyl, 2,2,2-trifluoroethyl ether (CHF 2CF 2OCH 2CF 3)+alcohols, ketones, or esters systems were…”
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Vapor−Liquid Equilibria of the Three Binary Systems: Water + Tetraethylene Glygol (TEG), Ethanol + TEG, and 2-Propanol + TEG
Published in Industrial & engineering chemistry research (04-05-1998)“…Vapor−liquid equilibrium and liquid density were measured for the three binary systems water + tetraethylene glycol (TEG), ethanol + TEG, and 2-propanol + TEG…”
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