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Conversion of ocean thermal energy with the 'salt cycle'

机译:随着“盐循环”的转换海洋热能

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A temperature gradient exists between the top and the depths of oceans, the "Salt Cycle" is targeted at converting this thermal energy. The phases of certain solutions (liquid - liquid or solid - liquid) separate out at lower temperatures enabling the separation of the solute. By placing the solute behind a semipermeable membrane, at a higher temperature, an osmotic pressure can be developed. The pressure released into a turbine can generate power or may be put to other uses like desalination. theright chamber is of higher concentration giving rise to osmotic pressure on that side. This osmotic pressure is released into a reaction type turbine (4). The draft tube of the turbine leads into a deep sea heat exchanger (6) where the solution getscooled and its components get separated due to lowering of solubility of the solute. The solute phase is collected and pumped by solute pump (7) back into the osmotic chamber. The remaining liquid flows back to a surface heat exchanger (I) where it getsheated to around the surface temperature. The solubility of the solute increases at higher temperature. The process continues in a closed cycle hereby named 'Salt Cycle'.As the liquid coming from the deepsea heat exchanger is not entirely free of solute, the required to flush a certain amount of residue into the down going draft tube, this will maintain an equilibrium in the concentration.
机译:在海洋的顶部和深度之间存在温度梯度,“盐循环”靶向转换该热能。在较低温度下分离出一定溶液(液 - 液或固体液体)的相位,使得溶质的分离。通过将溶质放在半透膜后面,在更高的温度下,可以开发渗透压。释放到涡轮机中的压力可以产生功率,或者可以像脱盐一样放电其他用途。 The Theright腔室具有更高的浓度,从而产生对该侧的渗透压。将该渗透压释放到反应型涡轮机(4)中。涡轮机的牵伸管引入深海热交换器(6),其中溶液静电和其部件由于溶质的溶解度降低而分离。将溶质相通过溶质泵(7)泵回渗透室。剩余的液体流回到表面热交换器(i),在那里它会在表面温度周围曝光。溶质的溶解度在较高温度下增加。该过程在特此命名为“盐循环”的过程中继续。来自Deadsea热交换器的液体不完全没有溶质,需要将一定数量的残留物冲入下来的牵伸管中,这将保持一个浓度均衡。

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