Abstract: . . .  storage fluid, for the purpose of supplying the energy required for a multi-effect (MED) distillation plant installed at the PSA. With this configuration, a performance ratio (kg of distillate per 2,326 kJ heat input) of 10 was obtained. With the goal of improving that value, two procedures for recovering heat in the MED unit were studied, thermal compression (which is usually used in conventional MED plants) and absorption heat pump technology, which upgrades low temperature heat with much higher second . . .
. . .  future – Seven years of experience at the Plataforma Solar de Almería (Spain), Desalination 108, pp. 51-58, 1996. [5] Gregorzewski, A. and Genthner, K., High efficiency seawater distillation with heat recovery by absorption heat pumps. Proceedings of the IDA World Congress on Desalination and Water Reuse, pp. 97-113, Abu Dhabi, November 18-24, 1995.  . . .
. . .  [4] Millow B. and Zarza E., Advanced MED solar desalination plants. Configurations, costs, future – Seven years of experience at the Plataforma Solar de Almería (Spain), Desalination 108, pp. 51-58, 1996. [5] Gregorzewski, A. and Genthner, K., High efficiency seawater distillation with heat recovery by absorption heat pumps. Proceedings of the IDA World Congress on Desalination and Water Reuse, pp. 97-113, Abu Dhabi, November 18-24, 1995.  . . .
. . .  2004. [4] Millow B. and Zarza E., Advanced MED solar desalination plants. Configurations, costs, future – Seven years of experience at the Plataforma Solar de Almería (Spain), Desalination 108, pp. 51-58, 1996. [5] Gregorzewski, A. and Genthner, K., High efficiency seawater distillation with heat recovery by absorption heat pumps. Proceedings of the IDA World Congress on Desalination and Water Reuse, pp. 97-113, Abu Dhabi, November 18-24, 1995.  . . .
. . .  Absorptivity 0.10 – 0.15 0.94 – 0.95 Weight (empty) 38 kg Operating pressure 6 bar Testing pressure 12 bar Optical efficiency 0.70 – 0.71 Thermal loss factor 3.4 W/m 2 K Thermal storage system The thermal storage system is made up of two interconnected 12-m 3 -capacity water tanks (See Fig. 5). The total volume finally chosen is based on the response time required by the gas boiler and the absorption heat pump to reach nominal operating conditions. The use of two tanks enables the solar contribution to be increased . . .
. . .  Coast researchers seek to demonstrate SWRO affordability, Desalination & Water Reuse 14(3), pp. 10-18, 2004. [4] Millow B. and Zarza E., Advanced MED solar desalination plants. Configurations, costs, future – Seven years of experience at the Plataforma Solar de Almería (Spain), Desalination 108, pp. 51-58, 1996. [5] Gregorzewski, A. and Genthner, K., High efficiency seawater distillation with heat recovery by absorption heat pumps. Proceedings of the IDA World Congress on Desalination and Water Reuse, . . .
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