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Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

International journal of thermophysics, 2019-11, Vol.40 (11), Article 102

2019

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Utilizing environment-friendly eugenol as a diluent with trioctylamine for the reactive extraction of aqueous levulinic acid

Scientific reports, 2024-09, Vol.14 (1), p.22389-14, Article 22389

2024

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Extraction of Levulinic Acid from Aqueous Solution Using Trioctylamine at Different Temperatures

Journal of solution chemistry, 2024-11, Vol.53 (11), p.1544-1559

2024

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Correction to: Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

International journal of thermophysics, 2023, Vol.44 (12), Article 171

2023

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Densities, Viscosities, and Thermal Conductivities of the Ionic Liquid 7-Methyl-1,5,7-triazabicyclo[4.4.0]dec-5-enium Acetate and Its Mixtures with Water

International journal of thermophysics, 2020, Vol.41 (12), Article 160

2020

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Correction: Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

International journal of thermophysics, 2022, Vol.43 (12), Article 184

2022

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Measurements and modeling of CO2 solubility in 1,8-diazabicyclo-[5.4.0]-undec-7-ene—Glycerol solutions

Fluid phase equilibria, 2014-07, Vol.374, p.25-36

2014

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Prototyping a calorimeter mixing cell with direct metal laser sintering

Chemical engineering research & design, 2016-04, Vol.108, p.146-151

2016

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Physical Properties of 7-Methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene (mTBD)

International journal of thermophysics, 2019-07, Vol.40 (7), p.1-23, Article 71

2019

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Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor–Liquid–Liquid Equilibria

Journal of chemical and engineering data, 2016-08, Vol.61 (8), p.2700-2711

2016

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Hydrodeoxygenation of Propylphenols on a Niobia‐Supported Platinum Catalyst: Ortho, Meta, Para Isomerism, Reaction Conditions, and Phase Equilibria

Advanced sustainable systems (Online), 2020-10, Vol.4 (10), p.n/a

2020

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Volumetric Properties of Aqueous Solutions of Zinc Sulfate at Temperatures from 298.15 to 393.15 K and Pressures up to 10 MPa

Journal of chemical and engineering data, 2021-01, Vol.66 (1), p.45-57

2021

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Application of GaInSn Liquid Metal Alloy Replacing Mercury in a Phase Equilibrium Cell: Vapor Pressures of Toluene, Hexylbenzene, and 2‑Ethylnaphthalene

Journal of chemical and engineering data, 2020-07, Vol.65 (7), p.3270-3276

2020

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A Volumetric Pitzer Model for Aqueous Solutions of Zinc Sulfate up to Near-Saturation Concentrations at Temperatures from 293.15 to 393.15 K and Pressures up to 10 MPa

Journal of chemical and engineering data, 2021-01, Vol.66 (1), p.58-64

2021

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Reactive Extraction of Levulinic Acid from Aqueous Solutions Using Trioctylamine with Diluents 2-Ethyl-1-hexanol, 4-Methylpentan-2-one, and Isoamyl Alcohol

Journal of chemical and engineering data, 2023-10

2023

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Hydrogen solubility in heavy oil systems: Experiments and modeling

Fuel (Guildford), 2014-12, Vol.137, p.393-404

2014

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Vapor−Liquid Equilibrium for the Binary Systems of 3-Methylpentane + 2-Methyl-2-propanol at 331 K and + 2-Butanol at 331 K

Journal of chemical and engineering data, 2001-05, Vol.46 (3), p.754-758

2001

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Application-Related Consideration of the Thermal Stability of [mTBDH][OAc] Compared to Amidine-Based Ionic Liquids in the Presence of Various Amounts of Water

Industrial & engineering chemistry research, 2022-01, Vol.61 (1), p.259-268

2022

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Conceptual design of a distillation process for the separation of styrene monomer from polystyrene pyrolysis oil: experiment and simulation

Chemical engineering research & design, 2023-07, Vol.195, p.65-75

2023

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Vapor–Liquid Equilibrium of Ethanol + Sulfur Dioxide and Ethanol + Water + Sulfur Dioxide at Six Temperatures

Journal of chemical and engineering data, 2024-04

2024

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Toward solvent screening in the extractive desulfurization using ionic liquids: QSPR modeling and experimental validations

Fuel (Guildford), 2021-10, Vol.302, p.121159, Article 121159

2021

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Isobaric Vapor–Liquid Equilibrium of the Binary Mixtures Toluene + Styrene and Styrene + α‑Methylstyrene

Journal of chemical and engineering data, 2023-03, Vol.68 (3), p.654-663

2023

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Vapor- liquid equilibrium for the n-dodecane + phenol and n-hexadecane + phenol systems at 523 K and 573 K

Fluid phase equilibria, 2021-06, Vol.537, p.112991, Article 112991

2021

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Micro-scale piloting of a process for production of 2-methoxy-2,4,4-trimethylpentane

Chemical engineering and processing, 2017-12, Vol.122, p.143-154

2017

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110th Anniversary: Critical Properties and High Temperature Vapor Pressures for Furan, 2‑Methylfuran, 2‑Methoxy-2-methylpropane, 2‑Ethoxy-2-methylbutane, n‑Hexane, and Ethanol and Bubble Points of Mixtures with a New Apparatus

Industrial & engineering chemistry research, 2019-12, Vol.58 (49), p.22350-22362

2019

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Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

Utilizing environment-friendly eugenol as a diluent with trioctylamine for the reactive extraction of aqueous levulinic acid

Extraction of Levulinic Acid from Aqueous Solution Using Trioctylamine at Different Temperatures

Correction to: Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

Densities, Viscosities, and Thermal Conductivities of the Ionic Liquid 7-Methyl-1,5,7-triazabicyclo[4.4.0]dec-5-enium Acetate and Its Mixtures with Water

Correction: Vapor Pressures, Densities, and PC-SAFT Parameters for 11 Bio-compounds

Measurements and modeling of CO2 solubility in 1,8-diazabicyclo-[5.4.0]-undec-7-ene—Glycerol solutions

Prototyping a calorimeter mixing cell with direct metal laser sintering

Physical Properties of 7-Methyl-1,5,7-triazabicyclo[4.4.0]dec-5-ene (mTBD)

Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor–Liquid–Liquid Equilibria

Hydrodeoxygenation of Propylphenols on a Niobia‐Supported Platinum Catalyst: Ortho, Meta, Para Isomerism, Reaction Conditions, and Phase Equilibria

Volumetric Properties of Aqueous Solutions of Zinc Sulfate at Temperatures from 298.15 to 393.15 K and Pressures up to 10 MPa

Application of GaInSn Liquid Metal Alloy Replacing Mercury in a Phase Equilibrium Cell: Vapor Pressures of Toluene, Hexylbenzene, and 2‑Ethylnaphthalene

A Volumetric Pitzer Model for Aqueous Solutions of Zinc Sulfate up to Near-Saturation Concentrations at Temperatures from 293.15 to 393.15 K and Pressures up to 10 MPa

Reactive Extraction of Levulinic Acid from Aqueous Solutions Using Trioctylamine with Diluents 2-Ethyl-1-hexanol, 4-Methylpentan-2-one, and Isoamyl Alcohol

Hydrogen solubility in heavy oil systems: Experiments and modeling

Vapor−Liquid Equilibrium for the Binary Systems of 3-Methylpentane + 2-Methyl-2-propanol at 331 K and + 2-Butanol at 331 K

Application-Related Consideration of the Thermal Stability of [mTBDH][OAc] Compared to Amidine-Based Ionic Liquids in the Presence of Various Amounts of Water

Conceptual design of a distillation process for the separation of styrene monomer from polystyrene pyrolysis oil: experiment and simulation

Vapor–Liquid Equilibrium of Ethanol + Sulfur Dioxide and Ethanol + Water + Sulfur Dioxide at Six Temperatures

Toward solvent screening in the extractive desulfurization using ionic liquids: QSPR modeling and experimental validations

Isobaric Vapor–Liquid Equilibrium of the Binary Mixtures Toluene + Styrene and Styrene + α‑Methylstyrene

Vapor- liquid equilibrium for the n-dodecane + phenol and n-hexadecane + phenol systems at 523 K and 573 K

Micro-scale piloting of a process for production of 2-methoxy-2,4,4-trimethylpentane

110th Anniversary: Critical Properties and High Temperature Vapor Pressures for Furan, 2‑Methylfuran, 2‑Methoxy-2-methylpropane, 2‑Ethoxy-2-methylbutane, n‑Hexane, and Ethanol and Bubble Points of Mixtures with a New Apparatus

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