1986
DOI: 10.1016/0098-1354(86)87003-x
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A tridiagonal matrix model for multistage flash desalination plants

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Cited by 88 publications
(18 citation statements)
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“…The condensate subsystem including the product tray has been dynamically modelled by [12,13,27] and quasi-stationary by [25] and [10]. Finally, saltwater properties are obtained in general from [ 18] and [29]. For steam and water properties, commentaries given for the brine heater are also valid here.…”
Section: Fwmentioning
confidence: 99%
“…The condensate subsystem including the product tray has been dynamically modelled by [12,13,27] and quasi-stationary by [25] and [10]. Finally, saltwater properties are obtained in general from [ 18] and [29]. For steam and water properties, commentaries given for the brine heater are also valid here.…”
Section: Fwmentioning
confidence: 99%
“…The correlation depends on the velocity of brine, brine temperature, and diameter tube [7]. The dependence of the NEA on the stage flashing temperature, the liquid level inside the flashing chamber and the brine flow rate per unit of chamber width is considered [8]. Also, hydraulic correlations to describe the inter-stages transport flow-rate of the flashing brine are adopted [9].…”
Section: Assumptions and Mathematical Modelmentioning
confidence: 99%
“…5. Non-equilibrium allowance (NEA) is taken into account according to the correlation developed in [5]. 6.…”
Section: Superstructure For the Desaltor Rigorous Modelmentioning
confidence: 99%