Continuous Dehydrogenation of Perhydro Benzyltoluene in a Catalytic Finned Tube Reactor

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL Industrial & Engineering Chemistry Research Pub Date : 2025-02-05 DOI:10.1021/acs.iecr.4c04254
Abelina Ellert, Michael Schmacks, Mikkel J. Braun, Luca Piccirilli, Ton V. W. Janssens, Peter Wasserscheid, Patrick Schühle
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Abstract

Storage and transport of hydrogen by charging liquid organic hydrogen carriers (LOHC) has emerged as a promising technology, as these LOHC can be handled within the existing fuel infrastructure. For the release of hydrogen from LOHC on board heavy-duty vehicles, coated reactor systems are advantageous, as the heat transfer to the catalyst is fast and efficient and the immobilized catalyst is protected from movement and abrasion in the reactor. However, the challenge is to provide a sufficient surface area for the catalytic coating, which is required to achieve high volumetric power densities. We here introduce a novel coated finned tube reactor concept for the dehydrogenation of the LOHC compound perhydro benzyltoluene (H12-BT). The reactor consists of a series of vertically arranged stainless-steel finned tubes, coated with a catalytically active layer (Pt–S/Al2O3). This results in a large catalytic surface area per reactor volume. Stable coatings have been obtained through dip-coating an Al2O3 slurry onto the finned tubes followed by impregnation with a platinum sulfite acid solution. The finned tubes are individually heated from the inside, allowing for a well-defined and manageable temperature distribution and fast responses under dynamic conditions (e.g., during vehicle start-up). The finned tube reactor exhibits plug flow reactor characteristics with increasing degrees of dehydrogenation (DoDh) in the flow direction. We have achieved a power density of more than 1 kW L–1 reaction volume at degrees of dehydrogenation above 70%. With this performance, the finned tube reactor concept shows high potential compared to state-of-the-art reactor concepts. By combining the new reactor type with a simple active carbon filter, PEM-fuel cell grade hydrogen (CO content <0.1 ppm, methane <70 ppm) was produced. This work demonstrates the finned tube reactor as an attractive concept for efficient hydrogen release from LOHC systems.

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催化翅片管反应器中过氢苄基甲苯的连续脱氢
通过充电液态有机氢载体(LOHC)来储存和运输氢气已经成为一项很有前途的技术,因为这些LOHC可以在现有的燃料基础设施中处理。对于重型车辆上LOHC的氢释放,涂层反应器系统是有利的,因为热传递到催化剂是快速和有效的,并且固定的催化剂在反应器中免受移动和磨损。然而,面临的挑战是为催化涂层提供足够的表面积,这需要实现高体积功率密度。本文介绍了一种新型涂层翅片管反应器的概念,用于LOHC化合物过氢苄基甲苯(H12-BT)的脱氢。反应器由一系列垂直排列的不锈钢翅片管组成,涂有催化活性层(Pt-S /Al2O3)。这导致每个反应器体积的催化表面积很大。通过在翅片管上浸涂Al2O3浆料,再用亚硫酸铂溶液浸渍,获得了稳定的涂层。翅片管从内部单独加热,允许在动态条件下(例如,在车辆启动期间)实现明确和可管理的温度分布和快速响应。在流动方向上,随着脱氢度(DoDh)的增加,翅片管反应器表现出塞流反应器的特性。在脱氢度超过70%的情况下,我们已经实现了超过1 kW L-1的功率密度。有了这个性能,翅片管反应器概念与最先进的反应器概念相比显示出很高的潜力。通过将新型反应器与简单的活性炭过滤器相结合,可以产生pem燃料电池级氢气(CO含量0.1 ppm,甲烷含量70 ppm)。这项工作证明了翅片管反应器作为一个有吸引力的概念,有效地从LOHC系统中释放氢。
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
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