ISSN: 0021-9568

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Journal of Chemical & Engineering Data Q1 Unclaimed

American Chemical Society United States

Unfortunately this journal has not been claimed yet. For this reason, some information may be unavailable.

Journal of Chemical & Engineering Data is a journal indexed in SJR in Chemical Engineering (miscellaneous) and Chemistry (miscellaneous) with an H index of 132. It has a price of 3678 €. It has an SJR impact factor of 0,719 and it has a best quartile of Q1. It is published in English. It has an SJR impact factor of 0,719.

Journal of Chemical & Engineering Data focuses its scope in these topics and keywords: aqueous, thermodynamic, mixture, heat, solutions, functions, hfc, hydrate, ethylene, carbonsolubility, ...

Type: Journal

Type of Copyright:

Languages: English

Open Access Policy: Open Choice

Type of publications:

Publication frecuency: -

Categories: Chemical Engineering (miscellaneous) (Q1) Chemistry (miscellaneous) (Q2)

Price

3678 €

Inmediate OA

1839 €

Embargoed OA

0 €

Non OA

Metrics

0,719

SJR Impact factor

132

H Index

574

Total Docs (Last Year)

1645

Total Docs (3 years)

25306

Total Refs

4243

Total Cites (3 years)

1626

Citable Docs (3 years)

2,56

Cites/Doc (2 years)

44,09

Ref/Doc

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Aims and Scope

Best articles by citations

New Static Apparatus for Vapor Pressure Measurements: Reconciled Thermophysical Data for Benzophenone

Thermodynamic Properties of the Mixed Electrolytes {(y)NH4Cl + (1 -y)(NH4)2SO4}(aq) at the Temperature 298.15 K

Extensive Accuracy Test of the Force-Field-Based Quasichemical Method PAC-MAC

Conductivities of 1-Alkyl-3-methylimidazolium Chloride Ionic Liquids in Disaccharide + Water Solutions at 298.15 K

Activity Coefficients of RbF in the RbF + RbBr + H2O and RbF + RbNO3 + H2O Ternary Systems Using the Potentiometric Method at 298.2 K

Measurement and Correlation of Phase Equilibria for Water + Decane + 2-Propanol, Water + Hexane + 2-Propanol, and Water + Decane + 2-Butanol Ternary Systems at 573 and 593 K and 15.0 and 20.0 MPa

Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures

Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate

Measurement and Correlation of the Physicochemical Properties of Novel Aqueous Bis(3-aminopropyl)amine and Its Blend with N-Methyldiethanolamine for CO2 Capture

Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine

Measurement and Correlation Studies of the Saturated Vapor Pressure, Density, Refractive Indices, and Viscosity of Methyl 4-tert-Butylbenzoate

Isopiestic Measurements on Aqueous Solutions of Heavy Metal Sulfates: MSO4 + H2O (M = Mn, Co, Ni, Cu, Zn). 2. T = 373.15 K

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A Systematic Investigation of the Thermodynamic Properties of Aqueous Barium Sulfate up to High Temperatures and High Pressures

Excess Enthalpies of Binary Mixtures of 1-Hexene with Somen-Alkanes at 298.15 K

Excess Enthalpy and Vapor-Liquid Equilibrium at Atmospheric Pressure for the Binary Systems 2-Methyl-2-propanol + 2,4,4-Trimethyl-1-pentene and 2-Butanol + 2,4,4-Trimethyl-1-pentene

Effect of Composition, Temperature, and Pressure on the Viscosities and Densities of Three Diesel Fuels

Phase Equilibria Data and Thermodynamic Analysis for Liquid-Hydrate-Vapor (LHV) with High Ethanol Concentrations

Thermal conductivities of ternary liquid mixtures

Phase Equilibria for Perfluoroethane + (n-Perfluorohexane orn-Perfluorooctane) Binary Systems: Measurement and Modeling

Molecular Behavior of Water on Titanium Dioxide Nanotubes: A Molecular Dynamics Simulation Study

Physicochemical Characterization of Ionic Liquid Binary Mixtures Containing 1-Butyl-3-methylimidazolium as the Common Cation

Sensitivity Analysis of CO2 Injection within Saline Aquifers for Storage Purposes in the Form of Hydrate Using a Reactive Transport Simulator

Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols atT= (288.15, 298.15, and 308.15) K

New Method Based on the UNIFAC-VISCO Model for the Estimation of Ionic Liquids Viscosity Using the Experimental Data Recommended by Mathematical Gnostics