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在耦合微结构系统中由全氢化二苄基甲苯制氢及使用5微米钯银膜进行纯化

Hydrogen Production from the LOHC Perhydro-Dibenzyl-Toluene and Purification Using a 5 µm PdAg-Membrane in a Coupled Microstructured System.

作者信息

Wunsch Alexander, Berg Tatjana, Pfeifer Peter

机构信息

Institute for Micro Process Engineering, Karlsruhe Institute for Technology, 76344 Eggenstein-Leopoldshafen, Germany.

出版信息

Materials (Basel). 2020 Jan 8;13(2):277. doi: 10.3390/ma13020277.

Abstract

Hydrogen bound in organic liquid hydrogen carriers (LOHC) such as dibenzyl-toluene enables simple and safe handling as well as long-term storage. This idea is particularly interesting in the context of the energy transition, where hydrogen is considered a key energy carrier. The LOHC technology serves as a storage between volatile energy and locally and timely independent consumption. Depending on the type of application, decisive specifications are placed on the hydrogen purity. In the product gas from dehydrogenation, however, concentrations of 100 to a few 1000 ppm can be found from low boiling substances, which partly originate from the production of the LOHC material, but also from the decomposition and evaporation of the LOHC molecules in the course of the enormous volume expansion due to hydrogen release. For the removal of undesired traces in the LOHC material, a pre-treatment and storage under protective gas is necessary. For purification, the use of Pd-based membranes might be useful, which makes these steps less important or even redundant. Heat supply and phase contacting of the liquid LOHC and catalyst is also crucial for the process. Within the contribution, the first results from a coupled microstructured system-consisting of a radial flow reactor unit and membrane separation unit-are shown. In a first step, the 5 µm thick PdAg-membrane was characterized and a high Sieverts exponent of 0.9 was determined, indicating adsorption/desorption driven permeation. It can be demonstrated that hydrogen is first released with high catalyst-related productivity in the reactor system and afterwards separated and purified. Within the framework of limited analytics, we found that by using a Pd-based membrane, a quality of 5.0 (99.999% purity) or higher can be achieved. Furthermore, it was found that after only 8 h, the membrane can lose up to 30% of its performance when exposed to the slightly contaminated product gas from the dehydrogenation process. However, the separation efficiency can almost completely be restored by the treatment with pure hydrogen.

摘要

结合在二苄基甲苯等有机液体氢载体(LOHC)中的氢便于简单安全地处理以及长期储存。在能源转型背景下,这一想法尤其引人关注,因为氢被视为关键的能量载体。LOHC技术可在挥发性能源与本地即时独立消费之间起到储存作用。根据应用类型,对氢纯度有决定性的规格要求。然而,在脱氢产生的产品气中,可发现低沸点物质的浓度为100至几千ppm,部分源于LOHC材料的生产,也源于在因氢释放导致的巨大体积膨胀过程中LOHC分子的分解和蒸发。为去除LOHC材料中不需要的痕量物质,需要在保护气体下进行预处理和储存。对于提纯,使用钯基膜可能会有帮助,这会使这些步骤变得不那么重要甚至多余。液体LOHC与催化剂的供热和相接触对该过程也至关重要。在本文中,展示了由径向流反应器单元和膜分离单元组成的耦合微结构系统的初步结果。第一步中,对5微米厚的钯银膜进行了表征,确定其Sieverts指数高达0.9,表明是吸附/解吸驱动的渗透。可以证明,氢首先在反应器系统中以与催化剂相关的高生产率释放,然后进行分离和提纯。在有限的分析范围内,我们发现通过使用钯基膜,可以达到5.0(纯度99.999%)或更高的质量。此外,还发现,当暴露于脱氢过程中略有污染的产品气时,仅8小时后,膜的性能就可能损失高达30%。然而,通过用纯氢处理,分离效率几乎可以完全恢复。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/2065/7014189/d358652785ba/materials-13-00277-g001.jpg

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