Abstract
This chapter describes the development of a mathematical model of a vertically stacked, forward feed (FF), low-temperature multi-effect distillation (LT-MED) plant. The model was developed by taking into consideration the same design and operational characteristics as the pilot multi-effect distillation (MED) plant at Plataforma Solar de Almería, in the southeast of Spain. The model has been validated, comparing the results of the model with the experimental data from the pilot plant.
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Abbreviations
- A :
-
Heat transfer area (m2)
- C p :
-
Specific heat (kJ/kg°C)
- M :
-
Mass flow rate (kg/s)
- M´ :
-
Mass flow rate by flashing process (kg/s)
- N :
-
Total number of effects
- NEA:
-
Non-equilibrium allowance (°C)
- PR:
-
Performance ratio
- Q :
-
Heat transfer rate (kW)
- T :
-
Temperature (°C)
- T´:
-
Temperature by flashing process (°C)
- U :
-
Overall heat transfer coefficient (kW/m2°C)
- X :
-
Salt concentration (g/kg)
- TTL:
-
Thermodynamic loss (°C)
- λ :
-
Latent heat of evaporation (kJ/kg)
- b:
-
Reject brine
- v:
-
Vapour entering, leaving (as distillate) and generated inside the evaporator or effect
- c:
-
Condenser
- cw:
-
Cooling seawater
- sw:
-
Seawater
- d:
-
Distillate
- da:
-
Distillate from the distribution system
- dr:
-
Distillate entering the mixers in the distribution system
- dm:
-
Portion of distillate distributed between the effects and the mixers
- vh:
-
Vapour consumed by preheater or distillate generated in the preheater
- gb:
-
Generated vapour by boiling
- gf:
-
Generated vapour by flashing
- f:
-
Feedwater
- fv:
-
Generated vapour by boiling and flashing
- s:
-
Heating steam in the first effect
- eff:
-
Effect
- ph:
-
Preheater
- vc:
-
Vapour in the condenser
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Palenzuela, P., Alarcón-Padilla, DC., Zaragoza, G. (2015). Steady-State Modelling of a Low-Temperature Multi-effect Distillation Plant. In: Concentrating Solar Power and Desalination Plants. Springer, Cham. https://doi.org/10.1007/978-3-319-20535-9_3
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DOI: https://doi.org/10.1007/978-3-319-20535-9_3
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