Page 2 - Water-energy_2020
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F. Calise, et al.                                                        Energy Conversion and Management 220 (2020) 113043

           Nomenclature                                       η el    electrical efficiency
                        2
           A      area, (m )                                  Subscripts and superscripts
           AF     annuity factor, (–)
           C      cost, (€)                                   a       Ambient
          c       specific Heat [J/kg/K]                       AH      auxiliary heater
           CPVT   concentrating PhotoVoltaic Thermal solar collectors  ap  Aperture
                  concentration ratio                         back    back surface
          C PVT
                                 2
           I b    beam radiation [W/m ]                       cell    photovoltaic cell
                                 2
                  total radiation [W/m ]                      cool    Cooling
           I tot
                                                2
          h c     convective heat transfer coefficient [W/m /K]  conc   Concentrator
                  fluid specific Enthalpy [J/kg]                conv    Convective
          h f
          ṁ f    fluid mass flow rate [kg/s]                   dhw     domestic hot water
           P ̇    electric power, (kW)                        el      Electric
                                           2
          r       area specific thermal resistance [m K/W]      f      Fluid
           T      temperature, (°C or K)                      heat    Heating
           v      voltage, (V)                                in      Inlet
                          3
           V      volume, (m )                                ins     Insulation
           E      energy, (kWh)                               MED     multi effect distillation
           I      current, (A)                                mp      max power
           J      capital cost, (€)                           N       Number
                                   3
           j      specific cost-price, (€/m )                  net     Net
           M      maintenance, (€/year)                       oc      open-circuit
           NOCT   nominal operating cell temp, (°C)           out     Outlet
           PI     profit index, (–)                            ref     reference conditions
                                                              rec     Receiver
           Greek symbols                                      RO      reverse osmosis
                                                              sky     referred to sky
          α       Absorptance                                 sub     Substrate
                  Emittance                                   th      Thermal
          ε R
          ε       heat transfer effectiveness                  TK      Tank
           Δ      Difference                                   th      Thermal
           ρ PVT  PVT Reflectance                              top     top surface
          σ       Stephan-Botzmann constant                   u       Unit
           η th   thermal efficiency
           Solar energy is considered one of the most promising renewable  Thermal and/or Mechanical Vapor Compression (TVC, MVC), Reverse
         energy sources [2], available almost all over the world with different  Osmosis, (RO), and Electrodialysis (ED). Some of these technologies
         intensities. It can be used as an energy input of polygeneration plants,  (MSF, MED, TVC) use thermal energy to convert seawater into fresh-
         including solar thermal collectors and photovoltaic (PV) panels. In fact,  water. Other technologies (RO, ED) are driven by electricity. Therefore,
         in solar-powered polygeneration plants, different solar technologies can  desalination units can also be easily coupled to a plurality of renewable
         be included for the direct conversion of the solar irradiation into heat  energy sources and/or energy cascades. In MED systems, seawater is
         available at different temperatures, according to the adopted solar  desalinated by a series of heating and evaporation processes, until
         thermal technology. For example, in case of low or medium tempera-  freshwater is produced [7]. This technique is quite flexible in both
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         ture levels, the produced heat is employed in solar heating and cooling  operating temperature and capacity range (also higher than 20.000 m /
         (SHC) systems and/or domestic hot water (DHW) applications [3]. SHC  day of freshwater). This makes this technology especially attractive for
         technology, converting the solar irradiation into space heating and  small-medium scale communities in remote zones such as islands. RO is
         cooling, is particularly interesting in summer, when the cooling energy  an electrically-driven desalination technology. In RO, fresh water,
         demand is often simultaneous to the availability of solar radiation. PV  under high pressure, passes through semi-permeable membranes,
         panels are used for the direct electric energy production and they are  leaving behind the high-concentrated brine solution. More than 50% of
         commonly coupled with electric vapour compression chillers. Hybrid  the worldwide installed desalination plants are based on RO technology
         PV-Thermal (PVT) collectors [4,5] for combined heat and power pro-  due to its simplicity and relatively low energy cost and energy con-
         duction are nowadays one of the most interesting applications for the  sumption [8]. As mentioned before, desalination technologies are also
         simultaneous production of useful thermal and electrical energy. In case  often coupled with renewable energy sources and a number of theo-
         of low-temperature heat (residential applications), thermal energy is  retical and experimental studies are available in this field. However,
         usually exploited for domestic hot water (DHW) preparation or space  there is no consensus regarding the most profitable desalination tech-
         heating purposes. In addition, due to the lower PVT operating tem-  nology, since this selection also depends on a number of additional
         perature - with respect to PV panels - the power production occurs at  external parameters. Therefore, one of the aims of this work is the
         higher electrical efficiencies. In solar trigeneration plants, PVT solar  comparative analysis of different desalination technologies, depending
         collectors can be combined with single-stage Lithium Bromide / Water  on different system layout configurations. In particular, in this work,
         (LiBr/H 2 O) absorption chillers for the production of cooling, heating,  the most promising thermal and electrical desalination technologies
         DHW and electric energy [6].                         (MED and RO, respectively) are analysed considering different poly-
           For freshwater production, several desalination techniques are  generation plants. Here, when the MED process is included into the
         available: Multi Stage Flash (MSF), Multi Effect Distillation (MED),  plant, solar thermal collectors are implemented, while electricity

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