Inhibition of calcium carbonate precipitation in NaCl brines from 25 to 90°C
暂无分享,去创建一个
[1] M. Tomson,et al. Mathematical Inhibitor Model for Barium Sulfate Scale Control , 1996 .
[2] M. Tomson,et al. The Nucleation Kinetics of Barium Sulfate in NaCl Solutions up to 6 m and 90°C , 1995 .
[3] J. E. Oddo,et al. The Inhibition of gypsum and barite nucleation in NaCl brines at temperatures from 25 to 90°C , 1994 .
[4] J. Morse,et al. The carbonic acid system and calcite solubility in aqueous Na-K-Ca-Mg-Cl-SO4 solutions from 0 to 90°C , 1993 .
[5] John W. Morse,et al. Prediction of halite, gypsum, and anhydrite solubility in natural brines under subsurface conditions , 1993 .
[6] P. Koutsoukos,et al. The precipitation of calcium carbonate in aqueous solutions , 1991 .
[7] P. Koutsoukos,et al. Calcium carbonate scale formation and prevention in a flow-through system at various temperatures , 1990 .
[8] L. A. Rogers,et al. Use of inhibitors for scale control in brine-producing gas and oil wells , 1990 .
[9] M. Tomson,et al. Effect of multiple precipitation inhibitors on calcium carbonate nucleation , 1988 .
[10] O. J. Vetter,et al. Oilfield Scale---Can We Handle It? , 1976 .
[11] A. E. Nielsen. Kinetics of precipitation , 1964 .
[12] R. A. Ruehrwein,et al. Effect of Polyelectrolytes on the Precipitation of Calcium Carbonate , 1957 .