| 1 |
Equilibrium Study in the KNO3 + NH4NO3 + H2O System at Temperatures from 293.15 to 323.15 K
Wrobel-Kaszanek A, Druzynski S, Kielkowska U, Mazurek K
Journal of Chemical and Engineering Data, 64(2), 784, 2019 |
| 2 |
Solubility, Density, and Viscosity Data for the KVO3 + Fe(VO3)(3) + H2O System from (293.15 to 323.15) K
Mazurek K, Druzynski S, Kielkowska U, Wrobel-Kaszanek A
Journal of Chemical and Engineering Data, 64(9), 4084, 2019 |
| 3 |
Studies on Mutual Solubility of Salts in the NH4HCO3-(NH4)(2)SO4-H2O System
Druzynski S, Wrobel-Kaszanek A, Mazurek K, Kielkowska U
Journal of Chemical and Engineering Data, 64(8), 3457, 2019 |
| 4 |
Separation of vanadium ions from the post-leaching solution of spent vanadium catalyst
Mazurek K, Grzesiak P
Przemysl Chemiczny, 96(6), 1390, 2017 |
| 5 |
Solubility in the reciprocal quaternary K+Na+-SO42--VO3--H2O system at (293.15 and 313.15)K
Druzynski S, Mazurek K, Kielkowska U, Szalla A, Wrobel A
Fluid Phase Equilibria, 404, 75, 2015 |
| 6 |
Phase Diagram for the Na2SO4 + KVO3 + NaVO3 + K2SO4 + H2O System at 303.15 K and 323.15 K
Mazurek K, Druzynski S
Journal of Chemical and Engineering Data, 60(6), 1715, 2015 |
| 7 |
Investigations on the Solubility, Density, and Viscosity in the NaVO3 + Na2SO4 + H2O System from 293.15 K to 323.15 K
Mazurek K, Druzynski S
Journal of Chemical and Engineering Data, 59(5), 1468, 2014 |
| 8 |
Investigations on the Solubility in the KVO3 + K2SO4 + H2O System from 293.15 K to 323.15 K
Mazurek K
Journal of Chemical and Engineering Data, 58(4), 980, 2013 |
| 9 |
Studies on the optimum conditions for leaching the spent vanadium catalyst from metallurgical plants with sodium hydroxide solutions
Mazurek K
Przemysl Chemiczny, 91(2), 234, 2012 |
| 10 |
EFFECT OF KCL EXCESS AND INERT CARRIER ON THE YIELD OF KVO3 SYNTHESIS
Bialowicz K, Mazurek K, Kielkowska U, Trypuc M
Chemical Engineering Communications, 197(12), 1467, 2010 |
