Comparison of different operation modes of a single effect thermal desalination plant using waste heat from m-CHP units

被引:18
作者
Cioccolanti, Luca [1 ]
Savoretti, Andrea [2 ]
Renzi, Massimiliano [3 ]
Caresana, Flavio [1 ]
Comodi, Gabriele [1 ]
机构
[1] Univ Politecn Marche, Dipartimento Ingn Ind & Sci Matemat, Ancona, AN, Italy
[2] S TRA TE GIE Srl, Ancona, AN, Italy
[3] Libera Univ Bolzano, Bolzano, BZ, Italy
关键词
Stirling engine; Heat recovery; Low grade heat; Fresh water production; Prototype apparatus; PERFORMANCE EVALUATION; SALT CONCENTRATION; DISTILLATION; OPTIMIZATION; ENERGY; POWER; TEMPERATURE; SIMULATION; SYSTEMS; CHALLENGES;
D O I
10.1016/j.applthermaleng.2016.02.082
中图分类号
O414.1 [热力学];
学科分类号
摘要
This work is an in-depth analysis of the performance behavior of a small scale single effect thermal desalination plant. The prototype, which refers to the distributed micro cogeneration field, consists of a 1 kWe Stirling engine coupled with a single effect thermal desalination plant for the simultaneous production of electricity and >150 L/day of fresh water. The prototype was able to work in two different operation modes: batch operation and continuous operation. In the former, the evaporator tank is initially filled with the salt water up to its maximum and the evaporation process ends as the salt water level reaches the top of the coil. In the latter, concentrate is continuously extracted and salt water is fed inside the evaporator tank in order to maintain brine salinity almost constant. In a previous work authors investigated the plant performance in batch operation mode finding a good agreement with the predicted results. In this work, plant performance is evaluated in continuous operation and compared to the batch operation mode. In both cases, fresh water production reached a maximum of about 7 L/h in the best operating conditions. However, despite the higher complexity of the plant, performance is worse in the continuous operation mode due to the negative effect of the continuous seawater flow. Indeed, the lower the salt content of the treated water, the lower the fresh water production due to process limits which will be extensively discussed in the paper. More precisely, the plant's average productivities were about 1.3 L/kWh and 1.16 L/kWh of thermal energy input in batch and continuous operation modes respectively. In any case, the apparatus exhibited a very good response to varying thermal power input thus confirming the opportunity to feed the desalination plant also with different forms of waste heat. Hence the proposed solution, studied for a coupling with a 1 kWe Stirling engine, can be easily applied also to the other micro-CHP technologies. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:646 / 657
页数:12
相关论文
共 45 条
  • [1] Comparative performance evaluation of conventional multi-effect evaporation desalination processes
    Al-Mutaz, Ibrahim S.
    Wazeer, Irfan
    [J]. APPLIED THERMAL ENGINEERING, 2014, 73 (01) : 1194 - 1203
  • [2] Evaporation rate as a function of water salinity
    Al-Shammiri, M
    [J]. DESALINATION, 2002, 150 (02) : 189 - 203
  • [3] Reprint of "Desalination using low grade heat in the process industry: Challenges and perspectives"
    Ammar, Yasmine
    Li, Hanning
    Walsh, Conor
    Thornley, Patricia
    Sharifi, Vida
    Roskilly, Anthony P.
    [J]. APPLIED THERMAL ENGINEERING, 2013, 53 (02) : 234 - 245
  • [4] A review on the applicability of integrated/hybrid membrane processes in water treatment and desalination plants
    Ang, Wei Lun
    Mohammad, Abdul Wahab
    Hilal, Nidal
    Leo, Choe Peng
    [J]. DESALINATION, 2015, 363 : 2 - 18
  • [5] Load sharing with a local thermal network fed by a microcogenerator: Thermo-economic optimization by means of dynamic simulations
    Angrisani, Giovanni
    Canelli, Michele
    Rosato, Antonio
    Roselli, Carlo
    Sasso, Maurizio
    Sibilio, Sergio
    [J]. APPLIED THERMAL ENGINEERING, 2014, 71 (02) : 628 - 635
  • [6] [Anonymous], 2015, MATLAB
  • [7] Water distillation: a prototype to determine flow rate gains temperature and salt concentration changes in pressurised system
    Armenta-Deu, C
    [J]. RENEWABLE ENERGY, 2004, 29 (09) : 1557 - 1568
  • [8] Effects of temperature and salt concentration on distilled water production
    Armenta-Deu, C
    [J]. RENEWABLE ENERGY, 2002, 25 (02) : 281 - 292
  • [9] Bartolini C.M., 2012, 15 INT STIRL ENG C D
  • [10] Simulation of hybrid renewable microgeneration systems for variable electricity prices
    Brandoni, C.
    Renzi, M.
    Caresana, F.
    Polonara, F.
    [J]. APPLIED THERMAL ENGINEERING, 2014, 71 (02) : 667 - 676