Jonathan P. White, Thomas W. Chamberlain, Richard A. Bourne, David Taylor, Colin Brennan, Frans L. Muller. The mole fraction solubilities were between 7.9 × 10-4and 6.3 × 10-3for H2in methanol and between 7 × 10-4and 6.9 × 10-3for H2in methyl formate. Eng. A. Aloui, F. Delbecq, P. Sautet, C. De Bellefon. Eng. The static–analytic method takes advantage of a movable pneumatic capillary sampler (Rolsi™, Armines’ patent). Selva Pereda, Susana B. Bottini, Esteban A. Brignole. Equations of state (EOS), simple correlations and Artificial Neural Networks (ANN) have been compared to find the best modeling technique. Hydrogen content in the liquid phase was measured using a gas absorption method and Fugatron HYD-100 instrument. SOLUBILITY OF GAS IN WATER An open container of water (e.g. Efficient Batch-Mode Parahydrogen-Induced Polarization of Propane. These coefficients, combined with experimental data for the vapor pressure of methanol and with Henry's constants, partial molar volumes and Margules coefficients for dissolved gases in methanol, yield a correlation for calculating solvent losses as a function of temperature, pressure and gas composition. Foster, J. Chem. Jian Wang, Cun-Qin Lv, Jian-Hong Liu, Rong-Rong Ren, Gui-Chang Wang. Palladium(II) complexes containing a P,N chelating ligand. Nikita Cant, J. Chem. To assist designers in estimating the amount of absorption solvent lost during gas-sweetening operations, the University of California derived a correlation for calculating the solubility of methanol in gaseous mixtures at temperatures of -130/sup 0/ to 104/sup 0/F (-90/sup 0/ to 40/sup 0/C) and pressures of 1160 psi (80 bars). https://doi.org/10.1016/j.ijhydene.2020.10.066, https://doi.org/10.1016/j.cej.2020.124290, https://doi.org/10.1016/j.cej.2018.08.194, https://doi.org/10.1016/j.mcat.2018.05.017, https://doi.org/10.1016/j.jct.2012.12.013, https://doi.org/10.1016/j.molcata.2012.06.012, https://doi.org/10.1007/s11144-009-0095-0, https://doi.org/10.1252/kakoronbunshu.32.376, https://doi.org/10.1016/j.tca.2004.12.001, https://doi.org/10.1016/S0378-3812(02)00096-1, https://doi.org/10.1016/S0378-3812(01)00699-9, https://doi.org/10.1007/s11746-002-0438-1, https://doi.org/10.1252/kakoronbunshu.28.468, https://doi.org/10.1252/kakoronbunshu.28.759, https://doi.org/10.1016/S0022-328X(99)00109-6. Article Views are the COUNTER-compliant sum of full text article downloads since November 2008 (both PDF and HTML) across all institutions and individuals. Peters. A remarkable solvent effect on reductive amination of ketones. These metrics are regularly updated to reflect usage leading up to the last few days. Noncovalent Anchoring of Asymmetric Hydrogenation Catalysts on a New Mesoporous Aluminosilicate: Application and Solvent Effects. A comparison analysis is performed with measurements from Bezanehtak et al. Find more information about Crossref citation counts. The data are congruent. Abstract published in Advance ACS Abstracts, August 1, 1996. K. Bezanehtak,, G. B. Combes,, F. Dehghani, and, N. R. Foster, . The apparatus was used following a synthetic mode at 278.25 K from 0.04 to 0.33 MPa in order to compare the data obtained through the two techniques. Bottini, E.A. No data on the solubility of gases in propylene carbonate have been reported. Gas–liquid reactions under supercritical conditions—phase equilibria and thermodynamic modeling. The molar mass of molecular hydrogen is about 2 mg/milimole and so 1 mg is about the same as 0.5 moles so 1 ppm = 1 mg/L =0.5 mM. Journal of Molecular Catalysis A: Chemical. Oleg G. Salnikov, Danila A. Barskiy, Aaron M. Coffey, Kirill V. Kovtunov, Igor V. Koptyug, Eduard Y. Chekmenev. Theoretical investigation of solvent effects on the selective hydrogenation of furfural over Pt(111). [K. Bezanehtak, G.B. For example, methanol has been effectively used to remove water (and acid gases such as carbon dioxide and hydrogen sulfide) from natural gas  prior to its subsequent liquefaction. The solubilities of hydrogen gas in liquid phase methanol and methyl formate were measured under pressures up to 1500 kPa and temperatures to 140 °C. You have to login with your ACS ID befor you can login with your Mendeley account. [M.S. The Henry's law constants were about 620 MPa for H2 in methanol and 630 MPa for H2 in methyl formate at a temperature of 20 °C. Citations are the number of other articles citing this article, calculated by Crossref and updated daily. [Q. Liu, F. Takemura, A. Yabe, J. Chem. Journal of the American Oil Chemists' Society. Shiro Kajiyama, Fumio Takemura, Akira Yabe. Solvent-based fatty alcohol synthesis using supercritical butane. Isothermal hydrogen solubility in methanol has been measured at six temperatures: 248.41, 263.38, 278.01, 278.25, 291.20 and 308.20 K up to 3.4 MPa. The mole fraction solubilities were between 7.9 × 10-4 and 6.3 × 10-3 for H2 in methanol and between 7 × 10-4 and 6.9 × 10-3 for H2 in methyl formate. Get article recommendations from ACS based on references in your Mendeley library. The apparatus used in this work can be operated either as a static–analytic technique with a “on line” gas chromatograph or as a synthetic one. CO This article is cited by Calculated and experimental equilibrium data for methanol-hydrogen sulfide at 258°K 21 12. Solubility of Carbon Monoxide and Hydrogen in Methanol and Methyl Formate: 298–373 K and 0.3–3.3 MPa. Thermodynamic analysis. D. S. Brands, E. K. Poels, A. C. Dimian, A. Bliek. Modeling hydrogen solubility in primary normal alcohols (methanol, ethanol, 1-propanol and 1-butanol) has been studied in this article. Brignole. Vapor−Liquid Equilibrium for Binary Systems of Carbon Dioxide + Methanol, Hydrogen + Methanol, and Hydrogen + Carbon Dioxide at High Pressures. Hydrogen solubility in methanol, (methanol + carbon dioxide) and (methanol + carbon dioxide + oxygen) was measured and correlated at different temperatures (268 < T /K < 288) and pressures (0.37 < P /MPa < 3.5). Decoupling the relative rate of hydrogen uptake via convection and mass transfer by a single catalytic pellet in a scaled down trickle bed reactor.