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1.
The solubility of CO2 in triethylene glycol monomethyl ether (TEGMME) has been measured at 40, 70 and 100°C at pressures up to 8.8 MPa. The results were correlated with the Peng-Robinson (1976) equation of state. The interaction parameters and Henry's constants were derived. 相似文献
2.
The solubility of ethane in N-methylpyrrolidinone (NMP) has been measured at ?10, 25, 40, 50, 70, 75, 100, and 120°C at pressures up to 7.1 MPa. The solubility data obtained are compared with those of ethane in other physical solvents. The results were correlated with the Peng-Robinson (1976) equation of state and the interaction parameters were obtained. Henry's constants were also determined. 相似文献
3.
The solubility of H2S in n-hexadecane has been determined at 50, 100 and 150°C at pressures up to 7.4 MPa. The results were correlated with the Peng-Robinson (1976) equation of state and Henry's constants were derived for comparison with low pressure data in the literature. 相似文献
4.
The solubility of ethane in triethylene glycol monomethyl ether (TEGMME) has been measured at 40, 70 and 100°C at pressures up to 9.2 MPa. The solubility data obtained are compared with those of ethane in other physical solvents. The results were correlated with the Peng-Robinson (1976) equation of state and the interaction parameters were obtained. Henry's constants were also determined. 相似文献
5.
Solubilities expressed by Henry's law constants for carbon dioxide, hydrogen sulfide and sulfur dioxide in four physical solvents (propylene carbonate, N-formyl morpholine, Selexol, and methyl cyanoacetate) have been measured at several temperatures ranging from 25°C to 70°C, using gas-liquid chromatography. Thermodynamic properties including enthalpies and entropies of solution have been derived from the solubility data. 相似文献
6.
N-formyl morpholine (NFM) is a solvent that has been used to separate acid gases from gas streams. An advantage of NFM is the high solubility of acid gases compared with the low solubility of light hydrocarbons. The solubility of the light hydrocarbons in NFM is important, as the hydrocarbons constitute a loss to the process, and result in hydrocarbon emissions to the atmosphere. However, there are only a few experimental data sets dealing with the solubility of hydrocarbons in NFM. To provide data to be used in the design of plants in the natural gas processing industry, the solubility of propane (C3H8) in NFM was measured at 298.15, 313.15, and 343.15 K at pressures up to 20.15 MPa. The Peng-Robinson equation of state was employed to correlate the experimental data and to obtain binary interaction parameters. The binary interaction parameters were used to obtain the parameters of the Krichevsky-Ilinskaya equation and Henry's law constants for propane were calculated. Henry's law constants for propane were compared with those of hydrogen sulphide, carbon dioxide, methane, and ethane in NFM. 相似文献
7.
New extensive data are reported for the solubility of carbon dioxide in fourteen physical solvents, and compared to two other solvents widely used in industry (selexol® and sulfolane). The solubility data are expressed by Henry's law constants and have been measured at 25 °C, 40 °C and 60 °C, using an Autoclave cell. The study concludes that polyethylene glycol dimethyl ethers, and mixtures of these solvents are the best solvents for CO2 removal. 相似文献
8.
Yi-Wei Wang Frederick D. Otto Alan E. Mather Shuo Xu 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》1991,51(2):197-208
The solubilities of N2O and CO2 in aqueous sulfolane solutions and pure sulfolane solvent, and the diffusivities of N2O in aqueous sulfolane solutions were measured and correlated over the temperature range from 20° to 85°C; also, the data for density and viscosity that were needed in this experimental work were measured. This experiment revealed that the parameter of N2O analogy method depends not only on the temperature, but also on the character of the solvent. Therefore, different solvents possess different analogy parameters. Only for dilute aqueous solutions can the parameter be replaced by the analogy parameter of water. The results also proved that the sum of volume fractions contribution is a simple method to estimate the solubility in aqueous sulfolane solutions over the whole range of the concentrations and experimental temperatures, with an average deviation of less than 4·0%. 相似文献
9.
《分离科学与技术》2012,47(2):411-421
We have developed a ternary equation of state (EOS) model for the N2O/CO2/1-butyl-3-methylimidazolium acetate ([bmim][Ac]) system in order to understand the separation of N2O and CO2 using room-temperature ionic liquids (RTILs). The present model is based on a generic RK (Redlich-Kwong) EOS, with empirical interaction parameters for each binary system. The interaction parameters have been determined using our measured VLE (vapor-liquid-equilibrium) data for N2O/[bmim][Ac] and literature data for CO2/[bmim][Ac] and N2O/CO2. The binary EOS model for the N2O/[bmim][Ac] system correctly predicted the liquid-liquid phase separation found in VLLE experiments. The validity of the ternary EOS model has been checked by conducting VLE experiments for the N2O/CO2/[bmim][Ac] system over a temperature range from 296 to 313 K. With this EOS model, solubility (VLE) behavior has been calculated for various (T, P, and feed compositions) conditions. Over a range of N2O/CO2 feed ratios, the N2O/CO2 gas selectivity [α N 2 O/CO 2 = (y N 2 O /x N 2 O )/(y CO 2 /x CO 2 )] increases by at least 5 orders of magnitude when adding [bmim][Ac] (α = 1 × 102 to 1 × 107), compared with the absence of the ionic liquid (α = 0.96 to 0.98). The addition of [bmim][Ac] may provide a practical means of separating CO2 and N2O. Supplemental materials are available for this article. Go to the publisher's online edition of Separation Science and Technology to view the free supplemental file. 相似文献
10.
Methods for predicting Henry's law constants Hij are important as experimental data are scarce. We introduce a new machine learning approach for such predictions: matrix completion methods (MCMs) and demonstrate its applicability using a data base that contains experimental Hij values for 101 solutes i and 247 solvents j at 298 K. Data on Hij are only available for 2661 systems i + j. These Hij are stored in a 101 × 247 matrix; the task of the MCM is to predict the missing entries. First, an entirely data-driven MCM is presented. Its predictive performance, evaluated using leave-one-out analysis, is similar to that of the Predictive Soave-Redlich-Kwong equation-of-state (PSRK-EoS), which, however, cannot be applied to all studied systems. Furthermore, a hybrid of MCM and PSRK-EoS is developed in a Bayesian framework, which yields an unprecedented performance for the prediction of Hij of the studied data set. 相似文献
11.
The solubility of methane in 3 kmol/m3 solutions of monoethanolamine, diethanolamine, and triethanolamine was measured from 25° to 125°C and pressures up to about 13 MPa. Measurements were also made for the solubility of methane in water at 25° to 125°C and pressures up to 18 MPa in order to confirm the accuracy of the experimental technique. It is demonstrated that methane is more soluble (in terms of mole fraction) in the amine solution than in pure water. Furthermore, the solubility is an increasing function of the size of the alkanolamine. The solubility data were modeled using a Henry's-law approach and the results summarized in terms of salting-in coefficients. 相似文献
12.
The solubility of 1, 1, 1, 2,2-pentafluoroethane (HFC125), 1, 1, 1, 2-tetrafluoroethane (HFC134a), 1, 1, 1-trifluoroethane (HFC143a) and 1,1-difluoroethane (HFC152a) in four well-known hydrocarbons have been measured at temperatures between 293.15 and 363.15 K and pressures between 0.05 and 2 MPa. Henry's constant, and the activity coefficient for HFCs at infinite dilution, have been derived for measurements below 0.28 MPa. The measurements were made with an isochoric method and their uncertainty is less than 2% for Henry's constant and less than 3% at high pressure. For several mixtures, the experimental data have been correlated with the UNIQUAC method and binary interaction parameters have been derived, resulting in a deviation from the data of less than 4%. 相似文献
13.
Solubility of carbon dioxide in a mixture of polyethylene glycol dimethyl ethers (Genosorb 1753) was determined at 298.15, 313.15, 323.15 and 333.15 K at pressures up to 7940 kPa. The obtained solubility data are compared with those of CO2 in other physical solvents. The results were correlated with the Peng–Robinson (Peng and Robinson, Ind. Eng. Chem. Fundam. 15, 59–64 1976) equation of state, and the interaction parameters are reported. Data at 323.15 K were predicted. Henry's Law constants were obtained from the data and the excess properties (excess Gibbs free energy, excess entropy and excess enthalpy) of the liquid mixture over the full range of composition were predicted at each temperature using the NRTL activity coefficient model. Enthalpy of solution and the enthalpy of mixing were determined at infinite dilution. In addition, the heats of absorption were determined using Clausius–Clapeyron equation. La solubilité du dioxyde de carbone (CO2) dans un mélange de polyéthylène glycol diméthyl éthers (Genosorb 1753) a été déterminée à 298.15, 313.15, 323.15 et 333.15 K à des pressions allant jusqu'à 7940 kPa. Les données de solubilité obtenues sont comparées avec celles de CO2 dans d'autres solvants physiques. Les résultats ont été corrélés avec l'équation d'état de Peng–Robinson (Peng and Robinson, Ind. Eng. Chem. Fundam. 15, 59–64 1976) et les paramètres d'interaction sont présentés. La solubilité à 323.15 K a été prédite. Les constantes de la loi d'Henry ont été obtenues à partir des données. Les propriétés en excès (l'énergie libre de Gibbs d'excès, l'entropie et l'enthalpie d'excès) du mélange liquide sur toute la gamme de composition a ont été prédites à chaque température en utilisant le modèle NRTL. L'enthalpie de solution et l'enthalpie de mélange ont été déterminées dilution infinie. Finalement, les chaleurs d'absorption ont été déterminées en utilisant l'équation de Clausius–Clapeyron. © 2011 Canadian Society for Chemical Engineering 相似文献
14.
Solubility data of methane in ethylene glycol and 1-4 butylene glycol and carbon dioxide in ethylene glycol and 1-2 propylene glycol in the presence of the ionic liquid 1-butyl-3-methylimidazolium bromide have been measured in the temperature range (303–423) K at pressures up to 14 MPa. Henry's law constant of each solute in the studied solvent at saturation pressure is given. The experiments were performed in an autoclave type phase equilibrium apparatus using the total pressure method. For mixtures containing carbon dioxide and ethylene glycol no influence was observed. For mixtures containing carbon dioxide and 1-2 propylene glycol it was observed salting-out effect at 303.2 K and 323.2 K and salting-in effect at the remaining temperatures. For mixtures containing methane and ethylene glycol or 1-4 butylene glycol salting-in effect was observed. 相似文献
15.
In this set of experiments a magnetic suspension balance (MSB) was employed to measure the apparent solubilities of N2 and CO2 in polypropylene (PP) and ethene/octene copolymer melts, while the swollen volume predicted by the Sanchez–Lacombe (SL) equation of state (EOS) was used to account for the buoyancy effect. The swollen volume of the polymer/gas mixture, as well as the gas solubilities for both PP and the ethene/octene copolymer, are discussed. It was observed that the branched molecular structure limited the molecular movement, and therefore the volume swelling of the polymer/gas mixture. In a similar context, the solubility of both N2 and CO2 were less in the branched polymer (ethene/octene copolymer) than in the linear PP. © 2006 Wiley Periodicals, Inc. J Appl Polym Sci 103: 2945–2953, 2007 相似文献
16.
T. Merker C.‐M. Hsieh S.‐T. Lin H. Hasse J. Vrabec 《American Institute of Chemical Engineers》2013,59(6):2236-2250
The gas solubility of pure oxygen and of pure carbon dioxide as well as of their gaseous mixture are measured in the ternary liquid mixture cyclohexane + cyclohexanone + cyclohexanol at 313.6 K with a high‐pressure view‐cell technique using the synthetic method. The new experimental data are used to assess the capability of molecular simulation and conductor‐like screening model (COSMO)‐SAC to predict multicomponent fluid‐phase coexistence behavior. These methods are also compared systematically on the basis of experimental binary fluid‐phase coexistence data. In that comparison also the Peng–Robinson (PR) equation of state is included as a reference. Molecular simulation and COSMO‐SAC yield good results and are found to be far superior to the PR equation of state both in predictive and in adjusted mode. © 2013 American Institute of Chemical Engineers AIChE J, 59: 2236–2250, 2013 相似文献
17.
用SRK状态方程计算二氧化碳在N-甲基二乙醇胺水溶液中的溶解度 总被引：5，自引：0，他引：5
本文对二氧化碳在Ｎ－甲基二乙醇胺水溶液中的溶解度数据进行了收集和评估,并用ＳＲＫ状态方程对文献数据进行了关联计算。结果表明本模型对二氧化碳溶解度的计算精度与实验的测定精度相当。可用于过程的模拟计算。 相似文献
18.
The solubilities of chlorodifluoromethane (HCFC22), 1, 2-dichlorotetrafluoroethane (CFC114) and 1,1-difluoroethane (HFC 152a) in n-hexadecane have been measured at temperatures between 303. 15 and 343. IS K and Henry's constants have been derived. The measurements were made with two different methods, a GLC method and an isochoric method. In general the results of the methods differ less than their combined margin of error, which is estimated to be less than 5% for the GLC method and less than 2% for the isochoric method. 相似文献
19.
The solubility of hydrogen in different crude oil fractions was estimated using the modified UNIFAC group contribution method. Functional group concentrations were estimated from suggested group model structures. An optimization technique was carried out on critical properties to test the group model structure. The validity of this approach was verified by comparing the predicted and experimental hydrogen solubilities. The experimental hydrogen solubilities were measured by means of pulse response techniques. 相似文献
20.
Shuo Xu Yi-Wei Wang Frederick D. Otto Alan E. Mather 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》1993,56(3):309-316
The physicochemical properties of the mixed solvent of 2-piper-idineethanol (2-PE), sulfolane (TMS) and water were determined over a wide range of temperatures and compositions. The density, the viscosity and the dissociation constant, as well as the solubility of N2O in this mixed solvent were correlated as a function of temperature and composition over the entire experimental range. The models are useful not only for the ternary solvent system, but also for the binary solvent systems, such as 2-PE+H2O and TMS+H2O. From the regression, it has been found that the interaction of aqueous 2-PE solution and aqueous TMS solution is negligible. 相似文献