Performance of Continuous Hydrogen Production from Perhydro Benzyltoluene by Catalytic Distillation and Heat Integration Concepts with a Fuel Cell

Abstract

The benzyltoluene‐based liquid organic hydrogen carrier (LOHC) system enables the safe transport and loss‐free storage of hydrogen. At least 26% of the lower heating value of the released hydrogen, however, has to be invested in form of heat to release the stored hydrogen. The low operation temperatures of catalytic distillation (CD) can facilitate waste heat integration to reduce external heat demand. Herein, the continuous hydrogen release from perhydro benzyltoluene via CD is demonstrated. It is revealed in the experimental results that this mode of operation leads to a high hydrogen release rate and very efficient noble metal catalyst usage at exceptionally mild conditions. The hydrogen‐based productivity of platinum of 0.35 gH2 gPt−1 min−1 (0.7 kWLHV_H2 gPt−1) at a dehydrogenation temperature of only 267 °C is found to be nearly four times higher than for the conventional continuous liquid‐phase dehydrogenation at the same temperature. Furthermore, simulation results of the CD process are described. The feasibility of a fully heat‐integrated process for electricity generation from the released hydrogen via CD using waste heat from the fuel cell for the CD reboiler is demonstrated. The technical potential of coupling the H12–BT dehydrogenation by CD with high‐temperature fuel cell operation is highlighted by the simulation.

Modeling of the Continuous Dehydrogenation of Perhydro‐Dibenzyltoluene in a Cuboid Reactor

“…The cuboid reactor was compared with a cylindrical reactor to confirm the beneficial effect of the change in the cross section on the hydrogen release. The details of the cylindrical reactor setup and the experimental procedure for the cylindrical reactor can be found in Rüde et al [ 37 ] Unlike in the previous study the reactor was oriented horizontally and not vertically. We have chosen a reaction temperature of 260 °C to suppress the effect of evaporation on the comparison.…”

Perspective on Decarbonizing Long-Haul Trucks Using Onboard Dehydrogenation of Liquid Organic Hydrogen Carriers

“…There have been several studies focused on reactor designs to optimally perform the dehydrogenation reaction. − The primary objectives have been ensuring good heat transfer characteristics to power the highly endothermic reaction and managing the complex hydrodynamics as a result of the evolution of large volumes of hydrogen gas. Most literature investigations have focused on horizontal fixed-bed reactors, where evolved hydrogen moves perpendicular to the liquid flow and exits via the headspace. , They benefit from decoupling the liquid hourly space velocity (LHSV) from the gas evolution rate and do not have issues with flooding.…”