Solar driven DCMD: Performance evaluation and thermal energy efficiency

a b s t r a c t This paper presents the experimental results of a solar driven DCMD plant. The plant comprises four main loops. The first loop consists of the solar with a total area of 20 m2. The PV panels make up the second loop, which has a peak output of 1.48 kWpeak. The third loop in the DCMD represents three modules with a total area of 3.39 m 2 . The fourth loop is a thermal sink with a cooling water capacity of 10 3 L/h. Two heat exchangers are installed within the plant. The DCMD performance was evaluated in two modes, with the HRD (arrangement B) and without the HRD (arrangement A), during two days under various operating parameters. The permeability coefficient of the membrane was 3.27 × 10 −7 L/m 2 s Pa. The distillate per module was 3.31 L/h and 4.59 L/h for arrangements A and B, respectively. Thermal energy efficiency indicated that a fraction thermal energy was lost to the surroundings, and the balance was divided into two fractions, useful and non-useful heat. The STECmin was 2342 kW/m 3

[1]  David Loureiro,et al.  Small reverse osmosis units using PV systems for water purification in rural places , 2001 .

[2]  Runyu Ma,et al.  Analysis of a solar-powered membrane distillation system , 2005 .

[3]  A. Hafiane,et al.  Fluoride removal from aqueous solution by direct contact membrane distillation: theoretical and experimental studies , 2014, Environmental Science and Pollution Research.

[4]  Baltasar Peñate,et al.  Operational experience of a solar membrane distillation demonstration plant in Pozo Izquierdo-Gran Canaria Island (Spain) , 2012 .

[5]  Julián Blanco,et al.  Experimental evaluation of two pilot-scale membrane distillation modules used for solar desalination , 2012 .

[6]  Noreddine Ghaffour,et al.  Performance investigation of a solar-assisted direct contact membrane distillation system , 2013 .

[7]  Andrea Cipollina,et al.  A neural network-based optimizing control system for a seawater-desalination solar-powered membrane distillation unit , 2013, Comput. Chem. Eng..

[8]  Elias K. Stefanakos,et al.  Solar assisted sea water desalination: A review , 2013 .

[9]  Andrea Cipollina,et al.  تحلية مياه البحر؛ سيرورات الطاقة التقليدية والمتجددة (Seawater Desalination. Conventional and Renewable Energy Processes) , 2009 .

[10]  Menachem Elimelech,et al.  Direct contact membrane distillation with heat recovery: Thermodynamic insights from module scale modeling , 2014 .

[11]  Parimal Pal,et al.  Removal of arsenic from contaminated groundwater by solar-driven membrane distillation. , 2010, Environmental pollution.

[12]  M. Qtaishat,et al.  Desalination by solar powered membrane distillation systems , 2013 .

[13]  Matthias Rommel,et al.  Experimental investigations on solar driven stand-alone membrane distillation systems for remote areas , 2009 .

[14]  Tsung-Ching Chen,et al.  Immediate assisted solar direct contact membrane distillation in saline water desalination , 2010 .

[15]  Tzahi Y. Cath,et al.  Experimental study of desalination using direct contact membrane distillation: a new approach to flux enhancement , 2004 .

[16]  Enrico Drioli,et al.  Evaluation of energy requirements in membrane distillation , 2008 .

[17]  Stephen R Gray,et al.  Direct contact membrane distillation (DCMD): Experimental study on the commercial PTFE membrane and , 2011 .

[18]  E. Drioli,et al.  Potential of membrane distillation in seawater desalination: Thermal efficiency, sensitivity study and cost estimation , 2008 .

[19]  Sabah A. Abdul-Wahab,et al.  Performance study of the inverted absorber solar still with water depth and total dissolved solid , 2011 .

[20]  Julián Blanco,et al.  Experimental analysis of an air gap membrane distillation solar desalination pilot system , 2011 .

[21]  Zaher Al Suleimani,et al.  Desalination by solar-powered reverse osmosis in a remote area of the Sultanate of Oman , 2000 .

[22]  Kamalesh K. Sirkar,et al.  Desalination of brine and produced water by direct contact membrane distillation at high temperatures and pressures , 2012 .

[23]  Xing Yang,et al.  Performance improvement of PVDF hollow fiber-based membrane distillation process , 2011 .

[24]  Ali Kargari,et al.  Direct contact membrane distillation for seawater desalination , 2012 .

[25]  Hassan E.S. Fath,et al.  Solar desalination using humidification-dehumidification technology , 2002 .

[26]  Anthony G. Fane,et al.  The efficient use of energy in membrane distillation , 1987 .

[27]  Tzahi Y. Cath,et al.  Treatment of saline aqueous solutions using direct contact membrane distillation , 2011 .

[28]  Mohamed Khayet,et al.  Theoretical and experimental studies on desalination using the sweeping gas membrane distillation method , 2003 .

[29]  A. Hafiane,et al.  Direct contact membrane distillation: Capability to desalt raw water , 2017 .

[30]  Anthony G. Fane,et al.  Mass transfer mechanisms and transport resistances in direct contact membrane distillation process , 2006 .

[31]  Rosalam Sarbatly,et al.  Evaluation of geothermal energy in desalination by vacuum membrane distillation , 2013 .

[32]  M. Gryta Effectiveness of Water Desalination by Membrane Distillation Process , 2012, Membranes.

[33]  Toraj Mohammadi,et al.  Sea water desalination using electrodialysis , 2008 .

[34]  Hussain Al-Madani,et al.  Water desalination by solar powered electrodialysis process , 2003 .

[35]  Ali M. El-Nashar,et al.  The economic feasibility of small solar MED seawater desalination plants for remote arid areas , 2001 .

[36]  Adel O. Sharif,et al.  Experimental Investigation of Heat and Mass Transfer in Tubular Membrane Distillation Module for Desalination , 2012 .

[37]  S. T. Hsu,et al.  Seawater desalination by direct contact membrane distillation , 2002 .