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Acetone Oxime
The Experts below are selected from a list of 444 Experts worldwide ranked by ideXlab platform
Hongxing Wang – One of the best experts on this subject based on the ideXlab platform.
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Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian Huang, Ye ChangshenAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
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liquid liquid equilibrium for the ternary system Acetone Oxime methyl ether Acetone water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian HuangAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
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isobaric vapor liquid equilibria of the binary system Acetone Acetone Oxime methyl ether at 101 3 kpa
Fluid Phase Equilibria, 2013Co-Authors: Hongxing WangAbstract:Abstract Isobaric vapor–liquid equilibria (VLE) were measured for the binary system Acetone + Acetone Oxime methyl ether (AOME) at 101.3 kPa. The activity coefficients were correlated satisfactorily with NRTL and Wilson models. The thermodynamic consistency of the obtained VLE data was checked by Herington method and passed the test. The results show that the correlated data of NRTL and Wilson models are both in keep with the experimental data, and the UNIFAC parameters of the new group (C N) were determined using the obtained VLE data. The azeotrope behavior is not happen for the binary system of Acetone + AOME, which can provide the basis data to design the separation process, and promote the development of new technology to produce O -methylhydroxyamine hydrochloride effectively and economically.
Zhixian Huang – One of the best experts on this subject based on the ideXlab platform.
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Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian Huang, Ye ChangshenAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
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liquid liquid equilibrium for the ternary system Acetone Oxime methyl ether Acetone water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian HuangAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
Jia Dong – One of the best experts on this subject based on the ideXlab platform.
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Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian Huang, Ye ChangshenAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
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liquid liquid equilibrium for the ternary system Acetone Oxime methyl ether Acetone water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian HuangAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
Ye Changshen – One of the best experts on this subject based on the ideXlab platform.
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Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian Huang, Ye ChangshenAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
Cheng Lin – One of the best experts on this subject based on the ideXlab platform.
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Liquid–Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether–Acetone–Water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian Huang, Ye ChangshenAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.
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liquid liquid equilibrium for the ternary system Acetone Oxime methyl ether Acetone water
Journal of Chemical & Engineering Data, 2013Co-Authors: Jia Dong, Hongxing Wang, Cheng Lin, Zhixian HuangAbstract:In the production of Acetone Oxime methyl ether (AOME) and its related products, AOME usually needs to be separated from the AOME, Acetone, and water mixture. As the base data, the liquid–liquid equilibrium data for the AOME–Acetone–water ternary system were measured at 293.15 K, 303.15 K, 313.15 K, and 323.15 K, respectively, under atmospheric pressure. Then, the nonrandom two-liquid (NRTL) and T-K-Wilson models were used to correlate the experimental data. The root-mean-square deviation (RMSD) between the calculated values and the experimental data is less than 0.0054 for the NRTL equation, and the RMSD is up to 0.046 for T-K-Wilson equation. Therefore, for this ternary system, the NRTL equation is more suitable than the T-K-Wilson equation for predicting liquid activity coefficients of the system. At the same time, the experimental data also show that the temperature has little effect on the miscibility gap within the experimental temperature range.