Generalized Least Energy of Separation for Desalination and Other Chemical Separation Processes

Increasing global demand for fresh water is driving the development and implementation of a wide variety of seawater desalination technologies driven by different combinations of heat, work, and chemical energy. This paper develops a consistent basis for comparing the energy consumption of such tech...

Full description

Bibliographic Details
Main Authors: Mistry, Karan Hemant (Contributor), Lienhard, John H. (Contributor)
Other Authors: Massachusetts Institute of Technology. Department of Mechanical Engineering (Contributor)
Format: Article
Language:English
Published: MDPI AG, 2013-08-30T14:47:34Z.
Subjects:
Online Access:Get fulltext
LEADER 02441 am a22002053u 4500
001 80326
042 |a dc 
100 1 0 |a Mistry, Karan Hemant  |e author 
100 1 0 |a Massachusetts Institute of Technology. Department of Mechanical Engineering  |e contributor 
100 1 0 |a Mistry, Karan Hemant  |e contributor 
100 1 0 |a Lienhard, John H.  |e contributor 
700 1 0 |a Lienhard, John H.  |e author 
245 0 0 |a Generalized Least Energy of Separation for Desalination and Other Chemical Separation Processes 
260 |b MDPI AG,   |c 2013-08-30T14:47:34Z. 
856 |z Get fulltext  |u http://hdl.handle.net/1721.1/80326 
520 |a Increasing global demand for fresh water is driving the development and implementation of a wide variety of seawater desalination technologies driven by different combinations of heat, work, and chemical energy. This paper develops a consistent basis for comparing the energy consumption of such technologies using Second Law efficiency. The Second Law efficiency for a chemical separation process is defined in terms of the useful exergy output, which is the minimum least work of separation required to extract a unit of product from a feed stream of a given composition. For a desalination process, this is the minimum least work of separation for producing one kilogram of product water from feed of a given salinity. While definitions in terms of work and heat input have been proposed before, this work generalizes the Second Law efficiency to allow for systems that operate on a combination of energy inputs, including fuel. The generalized equation is then evaluated through a parametric study considering work input, heat inputs at various temperatures, and various chemical fuel inputs. Further, since most modern, large-scale desalination plants operate in cogeneration schemes, a methodology for correctly evaluating Second Law efficiency for the desalination plant based on primary energy inputs is demonstrated. It is shown that, from a strictly energetic point of view and based on currently available technology, cogeneration using electricity to power a reverse osmosis system is energetically superior to thermal systems such as multiple effect distillation and multistage flash distillation, despite the very low grade heat input normally applied in those systems. 
520 |a Center for Clean Water and Clean Energy at MIT and KFUPM (Project R13-CW-10) 
546 |a en_US 
655 7 |a Article 
773 |t Entropy