Department of Chemical and Environmental Engineering, Yale University, New Haven, Connecticut 06520-8286, United States.
Environ Sci Technol. 2015 May 5;49(9):5820-7. doi: 10.1021/es506347j. Epub 2015 Apr 14.
We present a hybrid osmotic heat engine (OHE) system that uses draw solutions with an organic solvent for enhanced thermal separation efficiency. The hybrid OHE system produces sustainable energy by combining pressure-retarded osmosis (PRO) as a power generation stage and membrane distillation (MD) utilizing low-grade heat as a separation stage. While previous OHE systems employed aqueous electrolyte draw solutions, using methanol as a solvent is advantageous because methanol is highly volatile and has a lower heat capacity and enthalpy of vaporization than water. Hence, the thermal separation efficiency of a draw solution with methanol would be higher than that of an aqueous draw solution. In this study, we evaluated the performance of LiCl-methanol as a potential draw solution for a PRO-MD hybrid OHE system. The membrane transport properties as well as performance with LiCl-methanol draw solution were evaluated using thin-film composite (TFC) PRO membranes and compared to the results obtained with a LiCl-water draw solution. Experimental PRO methanol flux and maximum projected power density of 47.1 L m(-2) h(-1) and 72.1 W m(-2), respectively, were achieved with a 3 M LiCl-methanol draw solution. The overall efficiency of the hybrid OHE system was modeled by coupling the mass and energy flows between the thermal separation (MD) and power generation (PRO) stages under conditions with and without heat recovery. The modeling results demonstrate higher OHE energy efficiency with the LiCl-methanol draw solution compared to that with the LiCl-water draw solution under practical operating conditions (i.e., heat recovery<90%). We discuss the implications of the results for converting low-grade heat to power.
我们提出了一种混合渗透压热机(OHE)系统,该系统使用有机溶剂作为汲取剂,以提高热分离效率。该混合 OHE 系统通过将压力延迟渗透(PRO)作为发电阶段和利用低品位热能的膜蒸馏(MD)作为分离阶段相结合,产生可持续能源。虽然以前的 OHE 系统使用水电解质汲取剂,但使用甲醇作为溶剂具有优势,因为甲醇具有高挥发性,且其热容和蒸发热比水低。因此,甲醇汲取剂的热分离效率将高于水电解质汲取剂。在这项研究中,我们评估了 LiCl-甲醇作为 PRO-MD 混合 OHE 系统潜在汲取剂的性能。使用薄膜复合(TFC)PRO 膜评估了膜传输特性以及 LiCl-甲醇汲取剂的性能,并与 LiCl-水汲取剂的结果进行了比较。使用 3 M LiCl-甲醇汲取剂,实现了 47.1 L m(-2) h(-1)的 PRO 甲醇通量和 72.1 W m(-2)的最大预估功率密度。在有和没有热回收的情况下,通过对热分离(MD)和发电(PRO)阶段之间的质量和能量流进行耦合,对混合 OHE 系统的整体效率进行了建模。建模结果表明,在实际操作条件下(即热回收<90%),与 LiCl-水汲取剂相比,LiCl-甲醇汲取剂具有更高的 OHE 能量效率。我们讨论了将低品位热能转化为电能的结果的意义。