Related Experiment Video
Updated: Aug 14, 2026

A Simple, Low-cost, and Robust System to Measure the Volume of Hydrogen Evolved by Chemical Reactions with Aqueous Solutions
Published on: August 17, 2016
Liquid organic hydrogen carriers for hydrogen storage: advances, challenges, and technoeconomic and sustainability
M Shahabuddin1,2, Raza Moshwan2, Md Rezaur Rahman3
1Department of Mechanical Engineering, Faculty of Engineering, University of Malaya 50603 Kuala Lumpur Malaysia shahabuddin@um.edu.my shahabuddin@iubat.edu.
Abstract:
Liquid Organic Hydrogen Carriers (LOHCs) have emerged as one of the most promising chemical-based options for hydrogen storage and transport. The review critically analysed peer-reviewed literature, primarily published recently, with emphasis on recent development, challenges and mitigating strategies. The review finds that Toluene-Methylcyclohexane (Toluene/MCH), benzyl toluenes (BT), dibenzyl toluenes (DBT), and N-ethylcarbazole (NEC) are technically advanced LOHC families with commercial applications. For hydrogenation reactions, noble metals, primarily Pt, Pd, and Ru, supported on oxide surfaces are widely used. The reaction temperature for the Toluene/MCH and NEC systems ranges from 180 to 225 °C, whereas BT and DBT require around 300 °C. For dehydrogenation, major catalyst/support systems include Pt/KIT-6 mesoporous silica, Pt/TiO2, Pt/Al2O3, Ru/Al2O3, Pt/V2O5, Pt/Y2O3, and Pt-Re/Al2O3. The dehydrogenation reaction critically suffers from a high-temperature requirement of ∼250-450 °C, due to its endothermic nature. Various types of reactors are used for the LOHC process, including fixed-bed, fluidised-bed, and Trickle/slurry-bed reactors. Significant challenges of LOHC systems include the high cost of catalysis, especially with noble catalysts; catalyst deactivation; high temperature/energy requirements, especially during dehydrogenation; carbon coking; slow reaction rates; instability under cycling; and by-product formation. From a technoeconomic perspective, the LOHC system is expensive, with a range of $2.0-7.0/kgH2 depending on the carrier and catalyst used. Therefore, LOHC technology necessitates a comprehensive, system-wide strategy rather than molecular-level advancements. One such strategy might be efficient heat utilisation in low-carbon hydrogen logistics, including integrated methods such as microwave and exhaust heat recovery. The management of carriers must align with chemical properties and logistics, while system-level techno-economic analysis (TEA) and life cycle assessment (LCA) are essential. Innovations in catalysts focus on inductively heatable structures and durability during cycles, while reactor advancements aim to improve temperature regulation and address transmission constraints.
Related Concept Videos
Reduction of Alkenes: Catalytic Hydrogenation
Metals like palladium, platinum, and nickel are commonly used in their solid forms — fine powder on an inert surface. As these catalysts remain insoluble in the reaction mixture, they are referred to as heterogeneous catalysts.
The hydrogenation process takes place on the surface of...
Biofuels
Reduction of Alkenes: Asymmetric Catalytic Hydrogenation
The metal catalyst used can be either heterogeneous or homogeneous. When hydrogenation of an alkene generates a chiral center, a pair of enantiomeric products is expected to form. However, an enantiomeric excess of one of the products can be facilitated using an enantioselective reaction or an...
Stability of Conjugated Dienes
A comparison of the enthalpies of hydrogenation of dienes reveals that conjugated dienes release less heat on hydrogenation, rendering them more stable than their nonconjugated analogs.
Reduction of Benzene to Cyclohexane: Catalytic Hydrogenation
Reduction of Alkynes to cis-Alkenes: Catalytic Hydrogenation
Like alkenes, alkynes can be reduced to alkanes in the presence of transition metal catalysts such as Pt, Pd, or Ni. The reaction involves two sequential syn additions of hydrogen via a cis-alkene intermediate.

