The Experts below are selected from a list of 443844 Experts worldwide ranked by ideXlab platform
Guangming Chen - One of the best experts on this subject based on the ideXlab platform.
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vapor liquid equilibrium for the mixture Nitrogen N2 methane ch4 in the temperature range of 110 to 125 k
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
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Vapor–Liquid Equilibrium for the Mixture Nitrogen (N2) + Methane (CH4) in the Temperature Range of (110 to 125) K
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
Xiao Hong Han - One of the best experts on this subject based on the ideXlab platform.
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vapor liquid equilibrium for the mixture Nitrogen N2 methane ch4 in the temperature range of 110 to 125 k
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
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Vapor–Liquid Equilibrium for the Mixture Nitrogen (N2) + Methane (CH4) in the Temperature Range of (110 to 125) K
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
Qin Wang - One of the best experts on this subject based on the ideXlab platform.
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vapor liquid equilibrium for the mixture Nitrogen N2 methane ch4 in the temperature range of 110 to 125 k
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
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Vapor–Liquid Equilibrium for the Mixture Nitrogen (N2) + Methane (CH4) in the Temperature Range of (110 to 125) K
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
Yu Jia Zhang - One of the best experts on this subject based on the ideXlab platform.
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vapor liquid equilibrium for the mixture Nitrogen N2 methane ch4 in the temperature range of 110 to 125 k
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
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Vapor–Liquid Equilibrium for the Mixture Nitrogen (N2) + Methane (CH4) in the Temperature Range of (110 to 125) K
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
Zan Jun Gao - One of the best experts on this subject based on the ideXlab platform.
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vapor liquid equilibrium for the mixture Nitrogen N2 methane ch4 in the temperature range of 110 to 125 k
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...
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Vapor–Liquid Equilibrium for the Mixture Nitrogen (N2) + Methane (CH4) in the Temperature Range of (110 to 125) K
Journal of Chemical & Engineering Data, 2012Co-Authors: Xiao Hong Han, Yu Jia Zhang, Zan Jun Gao, Qin Wang, Guangming ChenAbstract:The design and operation of low temperature processes involving natural gas requires the phase equilibrium knowledge about the mixture (Nitrogen (N2) + methane (CH4)) over extensive pressure and temperature ranges. In this work, the experimental apparatus for the vapor–liquid equilibrium is built, and vapor–liquid equilibrium data of the mixture (N2 + CH4) have been measured in the temperature range from (110 to 125) K. The experimental method used in this work is a single-cycle type. The vapor–liquid equilibrium experimental data of the mixture (N2 + CH4) are correlated by the Peng–Robinson equation-of-state + the first Modified Huron Vidal mixing rule + Wilson model, and the adjustable parameters of the activity coefficient are given. The correlated results show that they exhibit a good agreement with the experimental data. The average vapor composition deviation and the maximum vapor composition deviation are 0.0057 and 0.0166, respectively; the average relative pressure deviation and the maximum press...