Chemical separation process for highly saline water. 2. System analysis and modeling

H. K. Abdel-Aal; A. A. Ibrahim; M. A. Shalabi; D. K. Al-Harbi

doi:10.1021/ie9405697

Chemical separation process for highly saline water. 2. System analysis and modeling

H. K. Abdel-Aal^*, A. A. Ibrahim, M. A. Shalabi, D. K. Al-Harbi

^*Corresponding author for this work

King Fahd University of Petroleum & Minerals

Research output: Contribution to journal › Article › peer-review

3 Scopus citations

Abstract

The reactions and equilibrium relationships underlying the absorption process of CO₂ gas in ammoniated brine solutions as proposed in part 1 are described first. A numerical solution of a set of nonlinear equations developed in the form of an algorithm, to calculate the concentration of unreacted ammonia, is obtained next. Calculated values are compared with experimental data for the system under investigation. The instantaneous absorption rate is evaluated by using the approximate approach (film model) and the exact solution (penetration theory).

Original language	English
Pages (from-to)	805-810
Number of pages	6
Journal	Industrial and Engineering Chemistry Research
Volume	35
Issue number	3
DOIs	https://doi.org/10.1021/ie9405697
State	Published - Mar 1996

ASJC Scopus subject areas

General Chemistry
General Chemical Engineering
Industrial and Manufacturing Engineering

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10.1021/ie9405697

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title = "Chemical separation process for highly saline water. 2. System analysis and modeling",

abstract = "The reactions and equilibrium relationships underlying the absorption process of CO2 gas in ammoniated brine solutions as proposed in part 1 are described first. A numerical solution of a set of nonlinear equations developed in the form of an algorithm, to calculate the concentration of unreacted ammonia, is obtained next. Calculated values are compared with experimental data for the system under investigation. The instantaneous absorption rate is evaluated by using the approximate approach (film model) and the exact solution (penetration theory).",

author = "Abdel-Aal, \{H. K.\} and Ibrahim, \{A. A.\} and Shalabi, \{M. A.\} and Al-Harbi, \{D. K.\}",

year = "1996",

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journal = "Industrial and Engineering Chemistry Research",

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AU - Abdel-Aal, H. K.

AU - Ibrahim, A. A.

AU - Shalabi, M. A.

AU - Al-Harbi, D. K.

PY - 1996/3

Y1 - 1996/3

N2 - The reactions and equilibrium relationships underlying the absorption process of CO2 gas in ammoniated brine solutions as proposed in part 1 are described first. A numerical solution of a set of nonlinear equations developed in the form of an algorithm, to calculate the concentration of unreacted ammonia, is obtained next. Calculated values are compared with experimental data for the system under investigation. The instantaneous absorption rate is evaluated by using the approximate approach (film model) and the exact solution (penetration theory).

AB - The reactions and equilibrium relationships underlying the absorption process of CO2 gas in ammoniated brine solutions as proposed in part 1 are described first. A numerical solution of a set of nonlinear equations developed in the form of an algorithm, to calculate the concentration of unreacted ammonia, is obtained next. Calculated values are compared with experimental data for the system under investigation. The instantaneous absorption rate is evaluated by using the approximate approach (film model) and the exact solution (penetration theory).

UR - https://www.scopus.com/pages/publications/0030108705

U2 - 10.1021/ie9405697

DO - 10.1021/ie9405697

M3 - Article

AN - SCOPUS:0030108705

SN - 0888-5885

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EP - 810

JO - Industrial and Engineering Chemistry Research

JF - Industrial and Engineering Chemistry Research

IS - 3

ER -

Chemical separation process for highly saline water. 2. System analysis and modeling

Abstract

ASJC Scopus subject areas

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