This paper presents the development of an advanced adsorption desalination system (ADS) with heat and mass recovery. By means of internal heat and mass recovery, this adsorption desalination system (ADS), offers a significantly higher performance ratio compared to the conventional systems. After vapor desorption, the pressure difference in the hot bed is first transmitted to the cold bed using mass recovery. Then, the heat from the hot bed is transferred into the cold bed and, eventually, to the condenser and evaporator, by means of the cold water. Numerical simulations for this system are compared to a verified experimental model, and then developed to study the effect of the operating parameters. The level of SDWP or specific daily water production for this ADS was found to be 13.48 m^3/ton of silica gel/day at a hot water temperature of 92.5 (°C) and a cold water temperature of 30 (°C). Consequently, in these operating conditions, the SDWP of the advanced ADS was found to be 153% more than the conventional ADS. Also, at the same temperature conditions, the performance ratio of the ADS with heat and mass recovery was 35% higher than the ADS without heat and mass recovery.

本文介绍了具有热量和质量回收功能的高级吸附脱盐系统（ADS）的开发。通过内部热量和质量回收，该吸附脱盐系统（ADS）与常规系统相比，性能比明显提高。蒸气解吸后，首先通过质量回收将热床中的压力差传输到冷床中。然后，来自热床的热量通过冷水传递到冷床，并最终传递到冷凝器和蒸发器。将该系统的数值模拟与经过验证的实验模型进行比较，然后进行研究以研究运行参数的影响。发现该ADS的SDWP或特定的每日产水量为92.的热水温度为13.48 m ^ 3 /吨硅胶/天。5（°C）和30（°C）的冷水温度。因此，在这些操作条件下，发现高级ADS的SDWP比常规ADS高153％。同样，在相同温度条件下，具有热和质量回收率的ADS的性能比比没有热和质量回收率的ADS高35％。