CoordenaÃÃo de AperfeiÃoamento de NÃvel Superior / This work presents two new prototypes of a circular desalinator operation in a solar cooker for indirect heating. The first prototype, called Type A, produces desalinated water from brackish water deposited in the pan solar cooker. In the second prototype, the Type B, the brackish water pan is used only as a means of transfering heat to the first tray tower desalination. These prototypes were fabricated and tested in LESGN (Solar Energy Laboratory and Natural Gas). Its structure consists of stainless steel plates, trays with circular and inclined downwards (with circular trays to facilitate the flow of condensed water) and "pipes" (that harvest desalinated water and take out the stages and side rails, harvesting the water that condenses the side walls). The desalting tower was formed by a set of trays to facilitate the handling and operation. The experiments were conducted between 7.00am and 5.00pm and the maximum number of stages was three. Experiments with 2 and 3 stages confirmed the heat recovery process, in other words, the repeated use of the heat stored in the desalinated water in a lower stage by stage above. The experimental results showed that the maximum production were daily for the Type A, 4.72 L with 3 stages, and the desalinator Type B 3.50 L also with 3 stages. It was found that the efficiency of desalination type A was greater than that of Type B, which explains why Type B has a further resistance to heat transfer. On the other hand, Type B prototype allows continued operation of the desalination tower, not requiring the dismantling after each emptying process of the water in the pan / Este trabalho apresenta dois novos protÃtipos de um dessalinizador circular para operaÃÃo em um fogÃo solar de aquecimento indireto. O primeiro protÃtipo, denominado Tipo A, produz Ãgua dessalinizada a partir da Ãgua salobra depositada na panela do fogÃo solar. No segundo protÃtipo, o Tipo B, a Ãgua salobra da panela à usada apenas como meio de transferÃncia de calor para a primeira bandeja da torre de dessalinizaÃÃo. Estes protÃtipos foram fabricados e testados no LESGN (LaboratÃrio de Energia Solar e GÃs Natural). Sua estrutura à formada por chapas de aÃo inoxidÃvel com bandejas circulares e inclinadas para baixo, com bandejas circulares para facilitar o escoamento da Ãgua condensada, âcachimbosâ, que colhem a Ãgua dessalinizada e levam para fora dos estÃgios e calhas laterais, que colhem a Ãgua que condensa pelas paredes laterais. A torre de dessalinizaÃÃo foi formada por um conjunto de bandejas para facilitar o manuseio e operaÃÃo. Os experimentos foram realizados entre 7 e 17 hs e o nÃmero mÃximo de estÃgios foi trÃs. Os experimentos com 2 e 3 estÃgios confirmaram o processo de recuperaÃÃo de calor, ou seja, a utilizaÃÃo repetida do calor armazenado na Ãgua dessalinizada em um estÃgio inferior pelo estÃgio superior. Os resultados experimentais mostraram que as mÃximas produÃÃes diÃrias foram, para o Tipo A, de 4,72 L com 3 estÃgios, e para o dessalinizador Tipo B, 3,50 L com 3 estÃgios. Verificou-se que a eficiÃncia do dessalinizador Tipo A era superior ao do Tipo B, o que se explica por o Tipo B ter uma resistÃncia a transferÃncia de calor a mais. Por outro lado, o protÃtipo Tipo B permite uma operaÃÃo continuada da torre de dessalinizaÃÃo, nÃo sendo necessÃrio a sua desmontagem apÃs cada esvaziamento da Ãgua na panela.

CoordenaÃÃo de AperfeiÃoamento de Pessoal de NÃvel Superior / This dissertation presents the experimental result of a system to absorb solar energy to heat up a desalination tower with heat recovery mechanism and a change made in the heated water distribution at the heat storage tank. The system to absorb solar energy consists of solar thermal flat plate collectors for high temperatures and it responsible for the conversion of solar radiation in thermal energy to heat up the water to be desalinated. The change made in the storage tank consists of the installation of a stainless steel pipe with holes equally spaced and arrangement to allow a better distribution of the hot water from the solar collectors in the heat storage tank. The desalination unit has two components: two high temperatures solar collectors and a desalination tower with six stages. In its operation, water is heated in the solar collectors and moves by natural convection to the storage tank, to the bottom of the tower. In the tank, the water transfers heat to the salty water in the first stage of the tower. This heated water transfer heat by evaporation, convection and radiation to the second stage and part of its energy is lost to the ambient. The condensed vapor on the walls of the stages flows down by gravity to be collected in a reservoir installed under the desalination tower. The heat received by the second stage is used to heat up the ater in this stage and the process is repeated in all stages. The performance of the desalination unit was satisfactory. The temperature in the storage tank reached values near 85ÂC and the water temperatures at the outlet of the solar collector were near 100ÂC. The daily production was 31 liters of desalinated water and the GOR-value (gain output ratio) was 1,54