Transient and thermo-economic analysis of MED-MVC desalination system

Abstract An exergo-economic model is used to assess the performance of a multi-effect desalination plant integrated to a mechanical vapor compressor unit (MED-MVC) with a water production capacity of 1500 m3/day. The results show that the second law efficiency ( η I I ) is 2.8%. The MVC and evaporator units are responsible for about 39 and 52% of the total exergy destruction, respectively. The total water price (TWP) is 1.70 $/m3 when calculated using a simple conventional economic model and 1.63 $/m3 when calculated using an exergy-based cost model. Increasing the number of effects from 1 to 6 results in a 39% reduction in the specific power consumption (SPC), a 70% increase in η I I and a 24% decrease in TWP. A dynamic model is developed to investigate the effect of fluctuations of compressor work ( W ˙ c ) and inlet seawater temperature ( T s w ) on the plant behavior and performance. The dynamic model results show that the disturbance in W ˙ c has a significant effect on the plant transient behavior and may cause the plant to cease operation while a disturbance in T s w has only a moderate impact. Increasing T s w above a certain value of the steady-state condition without proper control on the plant response could lead to evaporator dry out. In term of performance, a reduction in W ˙ c causes a decrease in the plant production capacity and SPC, while it increases the plant performance ratio (PR). On the other hand, a reduction in the inlet T s w causes a reduction in the plant production capacity and PR and an increase in SPC for the same compressor work. Furthermore, a comparison between a MED-MVC system and a MED integrated to a thermal vapor compressor system (MED-TVC) reveals that the latter system is rather sensitive to the reduction in T s w due to the presence of the condenser unit in the MED-TVC. The response of the MED-MVC system is slower than the MED-TVC which is due to the high thermal capacity of the preheaters for the feed in the MED-MVC.

[1]  Massimo Morbidelli,et al.  Dynamic modeling of multistage flash desalination plants , 2000 .

[2]  O. A. Kotb Optimum numerical approach of a MSF desalination plant to be supplied by a new specific 650 MW power plant located on the Red Sea in Egypt , 2015 .

[3]  Hassan K. Abdulrahim,et al.  The effect of stage temperature drop on MVC thermal performance , 2011 .

[4]  Mahmoud M. El-Halwagi,et al.  Sustainable Design Through Process Integration: Fundamentals and Applications to Industrial Pollution Prevention, Resource Conservation, and Profitability Enhancement , 2011 .

[5]  Lidia Roca,et al.  Dynamic modeling and performance of the first cell of a multi-effect distillation plant , 2014 .

[6]  Ahmed H. Eissa,et al.  Transient model, simulation and control of a single-effect mechanical vapour compression (SEMVC) desalination system , 2004 .

[7]  C. Sommariva,et al.  Modelling, simulation, optimization and control of multistage flashing (MSF) desalination plants Part I: Modelling and simulation , 1993 .

[8]  Muhammad Wakil Shahzad,et al.  Multi effect desalination and adsorption desalination (MEDAD): A hybrid desalination method , 2014 .

[9]  L. Weimer,et al.  Maximizing water recovery/reuse via mechanical vapor‐recompression (MVR) evaporation , 1983 .

[10]  Manuel Berenguel,et al.  Modeling of a Solar Seawater Desalination Plant for Automatic Operation Purposes , 2008 .

[11]  Ahmed Ouammi,et al.  An optimization model for a mechanical vapor compression desalination plant driven by a wind/PV hybrid system , 2011 .

[12]  A. K. Adak,et al.  Development of a dynamic simulator (INFMED) for the MED/VC plant , 2010 .

[13]  Francisco Rodríguez,et al.  Predictive Control Applied to a Solar Desalination Plant Connected to a Greenhouse with Daily Variation of Irrigation Water Demand , 2016 .

[14]  Narmine H. Aly,et al.  Mechanical vapor compression desalination systems — A case study , 2003 .

[15]  L. Roca,et al.  Optimal operating conditions analysis for a multi-effect distillation plant according to energetic and exergetic criteria. , 2017, Desalination.

[16]  M. A. Darwish Thermal analysis of vapor compression desalination system , 1988 .

[17]  Walid El-Mudir,et al.  Performance evaluation of a small size TVC desalination plant , 2004 .

[18]  Yunus Cerci,et al.  The minimum work requirement for distillation processes , 2000 .

[19]  J. Caballero,et al.  Shale gas flowback water desalination: Single vs multiple-effect evaporation with vapor recompression cycle and thermal integration , 2017 .

[20]  Alfred Leipertz,et al.  Economical aspects of the improvement of a mechanical vapour compression desalination plant by dropwise condensation , 2010 .

[21]  John H. Lienhard,et al.  On exergy calculations of seawater with applications in desalination systems , 2010 .

[22]  Z. Ayub Plate Heat Exchanger Literature Survey and New Heat Transfer and Pressure Drop Correlations for Refrigerant Evaporators , 2003 .

[23]  Salah Frioui,et al.  Investment and production costs of desalination plants by semi-empirical method , 2008 .

[24]  Ramy H. Mohammed,et al.  Transient performance of MED processes with different feed configurations , 2018, Desalination.

[25]  Na Wang,et al.  Crystallization techniques in wastewater treatment: An overview of applications. , 2017, Chemosphere.

[26]  Nafiz Kahraman,et al.  Exergy analysis of a MSF distillation plant , 2005 .

[27]  M. J. Moran,et al.  Thermal design and optimization , 1995 .

[28]  N. Abbasov,et al.  Dynamic models of heat exchangers , 2006 .

[29]  M. Lucas,et al.  The mechanical vapour compression process applied to seawater desalination: a 1,500 ton/day unit installed in the nuclear power plant of Flamanville, France , 1985 .

[30]  A. S. Nafey,et al.  Thermo-economic analysis of solar thermal power cycles assisted MED-VC (multi effect distillation-vapor compression) desalination processes , 2011 .

[31]  Mohammadsadegh Ahmadi,et al.  Process modeling and performance analysis of a productive water recovery system , 2017 .

[32]  Antonio Valero,et al.  Thermoeconomics and Industrial Symbiosis. Effect of by-product integration in cost assessment , 2012 .

[33]  J. W. Burdett,et al.  Dynamics of a multiple‐effect evaporator system , 1971 .

[34]  Tahar Khir,et al.  Exergoeconomic optimization of a double effect desalination unit used in an industrial steam power plant , 2018, Desalination.

[35]  Menachem Elimelech,et al.  The Global Rise of Zero Liquid Discharge for Wastewater Management: Drivers, Technologies, and Future Directions. , 2016, Environmental science & technology.

[36]  James F. Manwell,et al.  A wind/diesel hybrid system with desalination for Star Island, NH: feasibility study results , 2009 .

[37]  C. Marsh,et al.  Dynamics and Control of Falling Film Evaporators with Mechanical Vapour Recompression , 1999 .

[38]  Kyaw Thu,et al.  Performance investigation of advanced adsorption desalination cycle with condenser–evaporator heat recovery scheme , 2013 .

[39]  Hassan E.S. Fath,et al.  Thermoeconomic design of a multi-effect evaporation mechanical vapor compression (MEE–MVC) desalination process , 2008 .

[40]  R. Matz,et al.  Low-temperature vapour compression and multi-effect distillation of seawater. Effects of design on operation and economics☆ , 1985 .

[41]  H. Ettouney,et al.  Fundamentals of Salt Water Desalination , 2002 .

[42]  Y. M. El-Sayed,et al.  Designing desalination systems for higher productivity , 2001 .

[43]  Alireza Yazdizadeh,et al.  Dynamic modeling of multi-effect desalination with thermal vapor compressor plant , 2014 .

[44]  S. Oh,et al.  Desalination processes evaluation at common platform: A universal performance ratio (UPR) method , 2018 .

[45]  Lidia Roca,et al.  Dynamic modeling and simulation of a solar-assisted multi-effect distillation plant , 2015 .

[46]  JoséM. Veza,et al.  Mechanical vapour compression desalination plants : a case study , 1995 .

[47]  I. Dincer,et al.  Exergoeconomic optimization of a new four-step magnesium–chlorine cycle , 2017 .

[48]  S. A. Al-Malek,et al.  Design of a solar-assisted mechanical vapor compression (MVC) desalination unit for remote areas in the UAE , 2006 .

[49]  M. A. Marwan,et al.  Dynamic response of multi-effect evaporators , 1997 .

[50]  Giorgio Micale,et al.  A dynamic model for MED-TVC transient operation , 2017 .

[51]  H. Ettouney Design of single-effect mechanical vapor compression , 2006 .

[52]  Parmod Budhiraja,et al.  Studies of scale formation and optimization of antiscalant dosing in multi-effect thermal desalination units , 2008 .