Solubility Isotherm of the System Li2SO4–K2SO4–MgSO4–H2O at 273.15 K

2013 ◽  
Vol 58 (6) ◽  
pp. 1692-1696 ◽  
Author(s):  
Hongyan Zhou ◽  
Dewen Zeng ◽  
Haijun Han ◽  
Ouyang Dong ◽  
Dongdong Li ◽  
...  
Keyword(s):  
Solubility Isotherm

Isomorphic Co-Crystallization of Ammonium and Rubidium Bromocarnallites

1994 ◽  
Vol 59 (8) ◽  
pp. 1815-1819 ◽  
Author(s):  
Christomir Christov ◽  
Christo Balarew ◽  
Stefka Tepavitcharova
Keyword(s):  
Distribution Coefficients ◽  
Mixed Crystals ◽  
Solubility Isotherm ◽  
Continuous Series ◽  
Liquid Phases

The solubility isotherm of the system NH4Br.MgBr2.6 H2O - RbBr.MgBr2.6 H2O - H2O has been investigated at 75 °C and formation of a continuous series of mixed crystals is established. The factors determining the values of the distribution coefficients of the components between the crystalline and liquid phases are discussed.

Solubility isotherm of the Zn(NO3)2-HCONH2-H2O system at 25°C

2009 ◽  
Vol 54 (11) ◽  
pp. 1827-1829 ◽  
Author(s):  
E. A. Frolova ◽  
V. P. Danilov
Keyword(s):  
Solubility Isotherm

scholarly journals Utilization of the post-filtration lye from the SCS method of soda production

2007 ◽  
Vol 9 (4) ◽  
pp. 59-62 ◽  
Author(s):  
Mieczysław TrypuĆ ◽  
Sebastian Drużyński ◽  
Urszula Kiełkowska ◽  
Krzysztof Mazurek
Keyword(s):  
Quaternary System ◽  
Mutual Solubility ◽  
Solubility Isotherm ◽  
Temperature Range ◽  
Isothermal Saturation

Utilization of the post-filtration lye from the SCS method of soda production The mutual solubility of salts in the NaVO3-NaNO3-H2O system was investigated at 293 - 323 K temperature range by the method of isothermal saturation of solutions. A fragment of the solubility polytherm for that system was plotted, based on the obtained data. The investigated system is a part of the quaternary NH4NO3-NaVO3-NH4VO3-NaNO3 system, and it is necessary for plotting the solubility isotherm as a planar projection according to Janecke, since it defines one edge of its square. Knowledge of the isotherm for that quaternary system is necessary to determine the optimal utilization conditions for the post-filtration lye, formed during the soda production from NaNO3 by the Solvay method, using NaVO3.

Solubility isotherm for the Na2MoO4-Na2SO4-H2O system

2008 ◽  
Vol 53 (4) ◽  
pp. 628-635 ◽  
Author(s):  
S. B. Zhilova ◽  
Z. G. Karov ◽  
R. M. El’mesova
Keyword(s):  
Solubility Isotherm

scholarly journals Plotting of the solubility isotherm for the NH4NO3 + NaVO3 + H2O system

2008 ◽  
Vol 10 (4) ◽  
pp. 11-14 ◽  
Author(s):  
Mieczysław Trypuć ◽  
Sebastian Drużyński ◽  
Krzysztof Mazurek
Keyword(s):  
Ammonium Nitrate ◽  
Maximum Yield ◽  
Solubility Isotherm ◽  
Oblique Projection ◽  
Ammonium Vanadate ◽  
Triple Points

Plotting of the solubility isotherm for the NH4NO3 + NaVO3 + H2O system The equilibrium research was performed for the NH4NO3 + NaVO3 + NH4VO3 + NaNO3 + H2O system at 293 and 303 K. The location of the P1 and P2 triple points was determined on the equilibrium plots with the planar projection according to Jänecke method. The maximum yield of the conversion of ammonium nitrate(V) to ammonium vanadate(V) was calculated at P1 points. The results constitute the basis to design further equilibrium experiments aimed to precisely determine the lines separating the areas of the co-crystallization of salts in the investigated system on the equilibrium plots in the oblique projection on a plane according to Jänecke method.

Solubility Isotherm and Phase Diagram of the System Tm2O3-SeO2-H2O at 100°C

2001 ◽  
Vol 132 (9) ◽  
pp. 1031-1036 ◽  
Author(s):  
Georgi G. Gospodinov ◽  
Miluvka G. Stancheva
Keyword(s):  
Phase Diagram ◽  
Solubility Isotherm

Bimodal character of the solubility isotherm of histone H1 complexes with short oligonucleotides

2011 ◽  
Vol 45 (2) ◽  
pp. 343-346 ◽  
Author(s):  
T. N. Bocharova ◽  
N. P. Kvitko ◽  
E. A. Smirnova ◽  
A. A. Volodin
Keyword(s):  
Histone H1 ◽  
Solubility Isotherm
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