Abstract

Measured viscosity and density data for ternary aqueous solutions of CaCl2 and KCl are presented at temperatures between 293 and 323 K with 5 K increment. A modified Jones–Dole was introduced by adding extra terms and proved to be suitable for modelling of the viscosity data. Goldsack and Franchetto, Hu and Exponential models are used to correlate the viscosity data, too. Al models are correlated as a function of temperature and concentration. All models had successfully predicted the viscosity with high precision reaching a maximum average absolute deviation (AAD) of less than 2.3%. The modified Jones–Dole showed the best results among other models. Viscosity of the ternary solution is higher than the viscosity of water by about 15% at low concentrations and reaches about 270% at the highest concentrations. The amount of CaCl2 has more significant effect on the ternary mixture viscosity compared to KCl. This has created difficulty in measuring the viscosity and consequently the challenge in finding the different models parameters. Ternary solution densities were successfully correlate with Kumar’s model with AAD of less than 0.4%. Comparison of the ternary solution density and viscosity with the few available data literature showed a good agreement.

Highlights

  • Measured viscosity and density data for ternary aqueous solutions of ­CaCl2 and KCl are presented at temperatures between 293 and 323 K with 5 K increment

  • The models used in this work were able to predict well the viscosity as function of both concentration and temperature and density of the specific system KCl + CaCl2 + H2O studied in this work

  • The Calculation method proposed in this work (Eq 5) has been compared to other investigated ternary aqueous solutions investigated in previous published ­work[18]; NaCl + CaCl2 + H2O and NaCl + MgCl2 + H2O and reached the same conclusion

Read more

Summary

Introduction

Measured viscosity and density data for ternary aqueous solutions of ­CaCl2 and KCl are presented at temperatures between 293 and 323 K with 5 K increment. In desalination, feed of saline water with high concentrations of electrolyte solutions are used to get the fresh water. In addition to the fresh water stream, another by-product stream is generated with substantially higher electrolytes concentration than the feed This stream is called concentrate or brine stream. Concentrate disposal with high concentration of electrolyte content of both KCl and ­CaCl2 among them is limited to desalination p­ rocesses[12] Other industries sharing this stream are mining processes such as oil and potash industries, salt dome for the storage of hydrocarbons and rejected brine from solar ponds used for heat g­ eneration[13,14,15]. The concentrated stream which contains both KCl and C­ aCl2 will be investigated for its viscosity and density

Results
Discussion
Conclusion
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call