Title of article
CaCO3–CO2–H2O system in falling film on a bank of horizontal tubes: Model verification
Author/Authors
Al-Rawajfeh، نويسنده , , Aiman Eid Al-Rawajfeh، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2010
Pages
9
From page
1050
To page
1058
Abstract
The purpose of this work is to model the CaCO3–CO2–H2O system in falling film on a bank of horizontal tubes. The model was applied on a 5-effects reference thermal vapor compression multiple-effect distiller (MED-TVC) operating at top brine temperatures (TBT) of 60–70 °C. The model can predict pH values, CaCO3 deposition and fouling resistance with greater accuracy. Through the MED stages, the HCO3− and CO2 concentrations slightly increased while the CO32− concentration slightly decreased. The pH decreased from 8.8 in the first stage to 8.4 in the 5th stage. The CO2 release rates as well as the CaCO3 deposition rates increase with increasing top brine temperature (TBT). CO2 release rates decrease from 36.4 g/t feed water in the first stage to 32.5 g/t in the last stage. The specific CaCO3 deposition decreases from 127.3 g/t feed water in the first stage to 100.1 g/t in the last stage.
Keywords
MED-TVC distillers , CO2 release rates , CaCO3 scale formation , Fouling resistance , MODELING
Journal title
Journal of Industrial and Engineering Chemistry
Serial Year
2010
Journal title
Journal of Industrial and Engineering Chemistry
Record number
1709203
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