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An optimal operating window for the Bunsen process in the I-S thermochemical cycle

机译:I-S热化学循环中本生过程的最佳操作窗口

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We searched for the optimal compromised operating conditions for the Bunsen reaction of IS thermochemical water splitting, considering the key concerns of the IS cycle: the liquid-liquid equilibrium (LLE) phase separation performance, the characteristics of water distribution between the sulfuric acid (SA) phase and the poly-hydroiodic acid (HI_x) phase, side reaction occurrence, and the effect on operating costs. Experimental data available from a literature survey were combined, and common trends were examined through a series of parametric studies. Based on the results, the optimal operating point and allowable operating window for the Bunsen reaction have been proposed: the optimal point is represented by 4 mol of excess iodine and 11 mol of excess water in the stoichiometry at temperature of 330 K, while the allowable window ranges over 4-6 mol for the excess iodine, 11-13 mol for the excess water, and 330-350 K for the temperature. After the Bunsen reaction and LLE phase separation, 5 mol of the excess water is distributed to the SA phase and 6-8 mol to the HI_x phase. Operating within this window makes it possible to avoid the side reaction and iodine solidification, to increase the HI concentration well above the azeotropic point in the HI_x section, and to minimize operating costs arising from excess iodine and water.
机译:考虑到IS循环的关键问题:液-液平衡(LLE)相分离性能,硫酸之间的水分布特征(SA),我们搜索了IS热化学水分解的本生反应的最佳折衷操作条件。 )相和聚氢碘酸(HI_x)相,会发生副反应,并影响运营成本。结合了文献调查获得的实验数据,并通过一系列参数研究研究了共同的趋势。根据结果​​,提出了本生反应的最佳操作点和允许的操作窗口:在330 K的温度下,化学计量中的最佳碘由4摩尔过量的碘和11摩尔过量的水表示。过量碘的窗口范围超过4-6 mol,过量水的窗口范围超过11-13 mol,温度范围超过330-350K。在本生反应和LLE相分离后,将5摩尔过量的水分配给SA相,将6-8摩尔分配给HI_x相。在该窗口内操作可以避免副反应和碘固化,可以将HI浓度大大提高到HI_x部分的共沸点之上,并可以将过量碘和水引起的运行成本降至最低。

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