Primary Amine

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Long Zhang - One of the best experts on this subject based on the ideXlab platform.

Sanzhong Luo - One of the best experts on this subject based on the ideXlab platform.

Jin-pei Cheng - One of the best experts on this subject based on the ideXlab platform.

Yi Zhang - One of the best experts on this subject based on the ideXlab platform.

  • measurement and modeling for vanadium extraction from the navo3 h2so4 h2o system by Primary Amine n1923
    The Journal of Chemical Thermodynamics, 2015
    Co-Authors: Pengge Ning, Yi Zhang
    Abstract:

    Abstract In this work, the solvent extraction of vanadium by using the Primary Amine N1923 as extractant was studied. Within different vanadium concentration ranges, the extraction reactions were determined using the slope method at T = 298.15 K based on the vanadium phase diagram. The slopes (the stoichiometric ratio) were determined as 5/3, 1 and 11/3 for ( RNH 2 ) 5 / 3 H 3 VO 4 , ( RNH 2 ) H 3 V 3 O 9 and ( RNH 2 ) 11 / 3 H 6 V 10 O 28 , respectively. The thermodynamic model was established through regression of the experimental results with the Pitzer equation for both aqueous and organic phases by the General Algebraic Modelling System (GAMS). Three different sets of parameters and chemical equilibrium constants K were determined, which corresponded to the three extraction reactions. The orders of the lnK values are V 10 > V 3 > V 1 (organic V species), and the distribution coefficients ( D V ) are D V 1 > D V 3 > D V 10 . The new model was applied to predict the regularities of extraction yield along with different initial conditions, and the results agree well with the experimental values.

  • selective extraction and deep separation of v v and cr vi in the leaching solution of chromium bearing vanadium slag with Primary Amine lk n21
    Separation and Purification Technology, 2014
    Co-Authors: Pengge Ning, Xiao Lin, Hongbin Cao, Yi Zhang
    Abstract:

    In this report the extraction of V(V) and Cr(VI) from a synthetic feed solution and real leaching solution of the chromium-bearing vanadium slag (V-Cr slag) using Primary Amine LK-N21 was studied. Detailed fundamental research work was conducted to investigate the Primary Amine extracting V(V) and Cr(VI). The mechanism and the difference between the two metals of extraction were studied and the experimental results were compared with previously published data. The optimum technological parameters for the separation of two metals were determined including: pH value in feed solution, phase ratio, mixing time, as well as others. The results showed that Primary Amine LK-N21 can extract V(V) selectively by hydrogen bonding association. Cr(VI) competed V(V) to combine with the Primary Amine, and the concentration of Cr(VI) decided the percentage extraction of V(V) and Cr(VI). Primary Amine LK-N21 extracted more than 90% of V(V) which resulted in over 90% of Cr(VI) left in the leaching solution of the V-Cr slag in the optimal conditions. Based on the results of experiments, V(V) and Cr(VI) can be separated with a high degree of selectivity. (C) 2014 Published by Elsevier B.V.

  • selective extraction and deep removal of tungsten from sodium molybdate solution by Primary Amine n1923
    Separation and Purification Technology, 2009
    Co-Authors: Pengge Ning, Yi Zhang
    Abstract:

    Selectively extracting tungsten to purify sodium molybdate solution was studied using Primary Amine N1923, including various conditions, such as equilibrium pH values, concentrations of extractant in organic phase and metals in feed solution, contact time of extraction and stripping, types of acidic solutions added, temperature of extraction and the dosage of stripping agent. Graphical method using McCabe-Thiele diagram and counter-current extraction simulation (CCES) were used to determine the required stages of deep removal of tungsten. The results show that appropriate concentrations of tungsten and molybdenum in feed solution have great influence on the difficult degree of the separation between the two metals. Organic phase including 0.051 M of N1923 modified by LK-N21X diluted in kerosene can extract 92.7% of tungsten in sulfuric acid solution at equilibrium pH value of 7.07 for 10 min in one-stage extraction at 15.5 degrees C, and the separation factor reaches 329 under those optimum conditions. A two-stage CCES removes 99.83% of tungsten and obtains the purified sodium molybdate solution where W/Mo (mass ratio) reaches 2.9 x 10(-5). Stripping can be accomplished by NaOH solution completely and quickly. Furthermore, the extraction and stripping reactions of tungsten and molybdenum in equilibrium were proposed. (C) 2009 Elsevier B.V. All rights reserved.

Pengge Ning - One of the best experts on this subject based on the ideXlab platform.

  • measurement and modeling for vanadium extraction from the navo3 h2so4 h2o system by Primary Amine n1923
    The Journal of Chemical Thermodynamics, 2015
    Co-Authors: Pengge Ning, Yi Zhang
    Abstract:

    Abstract In this work, the solvent extraction of vanadium by using the Primary Amine N1923 as extractant was studied. Within different vanadium concentration ranges, the extraction reactions were determined using the slope method at T = 298.15 K based on the vanadium phase diagram. The slopes (the stoichiometric ratio) were determined as 5/3, 1 and 11/3 for ( RNH 2 ) 5 / 3 H 3 VO 4 , ( RNH 2 ) H 3 V 3 O 9 and ( RNH 2 ) 11 / 3 H 6 V 10 O 28 , respectively. The thermodynamic model was established through regression of the experimental results with the Pitzer equation for both aqueous and organic phases by the General Algebraic Modelling System (GAMS). Three different sets of parameters and chemical equilibrium constants K were determined, which corresponded to the three extraction reactions. The orders of the lnK values are V 10 > V 3 > V 1 (organic V species), and the distribution coefficients ( D V ) are D V 1 > D V 3 > D V 10 . The new model was applied to predict the regularities of extraction yield along with different initial conditions, and the results agree well with the experimental values.

  • selective extraction and deep separation of v v and cr vi in the leaching solution of chromium bearing vanadium slag with Primary Amine lk n21
    Separation and Purification Technology, 2014
    Co-Authors: Pengge Ning, Xiao Lin, Hongbin Cao, Yi Zhang
    Abstract:

    In this report the extraction of V(V) and Cr(VI) from a synthetic feed solution and real leaching solution of the chromium-bearing vanadium slag (V-Cr slag) using Primary Amine LK-N21 was studied. Detailed fundamental research work was conducted to investigate the Primary Amine extracting V(V) and Cr(VI). The mechanism and the difference between the two metals of extraction were studied and the experimental results were compared with previously published data. The optimum technological parameters for the separation of two metals were determined including: pH value in feed solution, phase ratio, mixing time, as well as others. The results showed that Primary Amine LK-N21 can extract V(V) selectively by hydrogen bonding association. Cr(VI) competed V(V) to combine with the Primary Amine, and the concentration of Cr(VI) decided the percentage extraction of V(V) and Cr(VI). Primary Amine LK-N21 extracted more than 90% of V(V) which resulted in over 90% of Cr(VI) left in the leaching solution of the V-Cr slag in the optimal conditions. Based on the results of experiments, V(V) and Cr(VI) can be separated with a high degree of selectivity. (C) 2014 Published by Elsevier B.V.

  • selective extraction and deep removal of tungsten from sodium molybdate solution by Primary Amine n1923
    Separation and Purification Technology, 2009
    Co-Authors: Pengge Ning, Yi Zhang
    Abstract:

    Selectively extracting tungsten to purify sodium molybdate solution was studied using Primary Amine N1923, including various conditions, such as equilibrium pH values, concentrations of extractant in organic phase and metals in feed solution, contact time of extraction and stripping, types of acidic solutions added, temperature of extraction and the dosage of stripping agent. Graphical method using McCabe-Thiele diagram and counter-current extraction simulation (CCES) were used to determine the required stages of deep removal of tungsten. The results show that appropriate concentrations of tungsten and molybdenum in feed solution have great influence on the difficult degree of the separation between the two metals. Organic phase including 0.051 M of N1923 modified by LK-N21X diluted in kerosene can extract 92.7% of tungsten in sulfuric acid solution at equilibrium pH value of 7.07 for 10 min in one-stage extraction at 15.5 degrees C, and the separation factor reaches 329 under those optimum conditions. A two-stage CCES removes 99.83% of tungsten and obtains the purified sodium molybdate solution where W/Mo (mass ratio) reaches 2.9 x 10(-5). Stripping can be accomplished by NaOH solution completely and quickly. Furthermore, the extraction and stripping reactions of tungsten and molybdenum in equilibrium were proposed. (C) 2009 Elsevier B.V. All rights reserved.