A subscription to JoVE is required to view this content. Sign in or start your free trial.
* These authors contributed equally
Membrane reactors enable hydrogenation in ambient conditions without direct H2 input. We can track the hydrogen production and utilization in these systems using atmospheric mass spectrometry (atm-MS) and gas chromatography mass spectrometry (GC-MS).
Industrial hydrogenation consumes ~11 Mt of fossil-derived H2 gas yearly. Our group invented a membrane reactor to bypass the need to use H2 gas for hydrogenation chemistry. The membrane reactor sources hydrogen from water and drives reactions using renewable electricity. In this reactor, a thin piece of Pd separates an electrochemical hydrogen production compartment from a chemical hydrogenation compartment. The Pd in the membrane reactor acts as (i) a hydrogen-selective membrane, (ii) a cathode, and (iii) a catalyst for hydrogenation. Herein, we report the use of atmospheric mass spectrometry (atm-MS) and gas chromatography mass spectrometry (GC-MS) to demonstrate that an applied electrochemical bias across a Pd membrane enables efficient hydrogenation without direct H2 input in a membrane reactor. With atm-MS, we measured a hydrogen permeation of 73%, which enabled the hydrogenation of propiophenone to propylbenzene with 100% selectivity, as measured by GC-MS. In contrast to conventional electrochemical hydrogenation, which is limited to low concentrations of starting material dissolved in a protic electrolyte, the physical separation of hydrogen production from utilization in the membrane reactor enables hydrogenation in any solvent or at any concentration. The use of high concentrations and a wide range of solvents is particularly important for reactor scalability and future commercialization.
Thermochemical hydrogenation reactions are used in ~20% of all chemical synthesis1. These reactions require large quantities of H2 gas, which are usually derived from fossil fuels, temperatures between 150 °C and 600 °C, and pressures up to 200 atm2. Electrochemical hydrogenation is an appealing way to bypass these requirements and to drive hydrogenation reactions using water and renewable electricity3. For conventional electrochemical hydrogenation, an unsaturated feedstock is dissolved in a protic electrolyte in an electrochemical cell. When a potential is applied to the cell, water oxidation occurs at the anode, while hydrogenation occurs at the cathode. In this reaction setup, both electrochemical water oxidation and chemical hydrogenation occur in the same reaction environment. The organic substrate is dissolved in a protic electrolyte to enable both electrochemical water splitting and hydrogenation of the feedstock. The proximity of these reactions can lead to byproduct formation and electrode fouling when the reactant is susceptible to nucleophilic attack or if the reactant concentration is too high (>0.25 M)4.
These challenges prompted our group to explore alternative ways to electrochemically drive hydrogenation reactions5,6,7. This search resulted in the use of a Pd membrane, which is conventionally used in hydrogen gas separation8. We use it as an electrode for water electrolysis on the electrochemical reactor side. This novel application of a palladium membrane enables the physical separation of the site of electrochemical water oxidation from the site of chemical hydrogenation. The resulting reactor configuration has two compartments: 1) an electrochemical compartment for hydrogen production; and 2) a chemical compartment for hydrogenation (Figure 1). Protons are generated in the electrochemical compartment by applying a potential across the Pt anode and the Pd membrane, which also serves as the cathode. These protons then migrate to the Pd membrane, where they are reduced to surface-adsorbed hydrogen atoms. The electrochemical compartment can be subdivided to include an optional cation exchange membrane to facilitate this proton migration. The surface-adsorbed hydrogen atoms permeate through the interstitial octahedral sites of the Pd fcc lattice9 and emerge on the opposite face of the membrane in the hydrogenation compartment, where they react with the unsaturated bonds of a given feedstock to form hydrogenated products7,10,11,12,13,14,15,16. The Pd in the membrane reactor, therefore, acts as (i) a hydrogen-selective membrane, (ii) a cathode, and (iii) a catalyst for hydrogenation.
Figure 1: Hydrogenation in a membrane reactor. Water oxidation at the anode produces protons, which are reduced on the palladium cathode. H permeates through the Pd membrane and reacts with propiophenone to form propylbenzene. Hydrogen evolution is a competing reaction that can occur on either side of the palladium membrane. For atmospheric mass-spectrometry, no chemical feedstock is used, necessitating H to leave the reactor in the form of H2 gas in either the electrochemical or hydrogenation compartments. Please click here to view a larger version of this figure.
The membrane reactor is assembled by sandwiching a Pd membrane between the anode and cathode compartments of an electrochemical H-cell12. Chemical-resistant O-rings are used to secure the membrane into place and ensure a leak-free seal. The electrochemical compartment of the membrane reactor contains a hydrogen-rich aqueous solution. In this study, we use 1 M H2SO4 and an anode that consists of a Pt wire enveloped in a 5 cm2 piece of platinum mesh. The anode is submerged in the electrolyte solution through a hole in the top of the electrochemical compartment. The chemical hydrogenation compartment contains a solvent and hydrogenation feedstock7,10,11,12,16,17. The hole at the top of the H-cell compartment is used for sampling. The experiments shown here use 0.01 M propiophenone in ethanol as the hydrogenation feed. However, the starting material (and concentration) can be varied to fit the experimental needs. For instance, a starting material that contains a long hydrocarbon chain and an alkyne functional group may be dissolved in pentane to improve solubility11. The applied current for the reaction can be between 5 mA/cm2 and 300 mA/cm2. All reactions are carried out under ambient temperature and pressure.
Atmospheric mass spectrometry (atm-MS) is used to measure the percent of hydrogen in the electrochemical compartment that permeates to the hydrogenation compartment11,12. This measurement is important to understand the energy inputs required for the membrane reactor, because it reveals the maximum possible hydrogen utilization (i.e., how much of the hydrogen being produced can actually be used for hydrogenation reactions). Hydrogen permeation through the Pd membrane is calculated by measuring the amount of H2 that evolves from both the electrochemical and hydrogenation compartments11,12. A permeation value of 100% means that all the hydrogen produced in the electrochemical compartment is transported through the Pd membrane to the hydrogenation compartment and then subsequently combines to form hydrogen gas. A permeation value of <100% means that hydrogen evolution occurs in the electrochemical compartment prior to permeating through the membrane. As H2 is produced from either the electrochemical or hydrogenation compartment, it enters the instrument and is ionized to H2+. The quadrupole selects fragments of m/z = +2, and the corresponding charge is measured by the detector. The plot obtained by this technique is the ionic charge over time. The ionic charge is measured for the hydrogenation compartment first, and when the signal stabilizes, the channels are changed to measure the electrochemical compartment. Hydrogen permeation is calculated by dividing the average ionic charge in the hydrogenation compartment by the total ionic charge measured in the reactor (Equation 1)11,12. To calculate hydrogen permeation, H2 from the hydrogenation and electrochemical compartments are measured separately using atm-MS.
(Eq. 1)
Gas chromatography mass spectrometry (GC-MS) is used to monitor the progress of the hydrogenation reaction12,14,15,16. To collect data for the example, the hydrogenation compartment of the reactor is filled with 0.01 M propiophenone in ethanol. By applying a potential across the Pt anode and the Pd cathode, reactive hydrogen is supplied to the hydrogenation compartment. The reactive hydrogen atoms then hydrogenate the unsaturated feedstock, and the products are quantified using GC-MS, where the sample is fragmented and ionized. By analyzing the mass of these fragments, the composition of the hydrogenation solution can be determined, and reaction rates can be calculated12,14,15,16.
1. Pd rolling
2. Pd annealing
3. Pd cleaning
4. Reactor assembly (Figure 2, left to right)
Figure 2: An image of the H-cell assembly. The electrochemical compartment contains 1 M H2SO4 electrolyte; this is where water oxidation occurs. The palladium membrane separates the two halves of the H-cell, and the gaskets provide a leak-free seal. The hydrogenation compartment contains 0.01 M propiophenone in ethanol (EtOH). Please click here to view a larger version of this figure.
5. Pd electrodeposition
6. Atm-MS reactor setup
7. Atm-MS instrument setup
8. Atm-MS software setup
9. Electrochemical hydrogenation
10. Gas chromatography-mass spectrometry
Atm-MS is used to measure the ionic current of the hydrogen that is produced in the membrane reactor. We can use these measurements to quantify how much hydrogen permeates through the Pd membrane during electrolysis. First, the hydrogen evolving from the hydrogenation compartment is measured (Figure 3, left of the dotted lines). When the signal reaches a steady state, the channel is switched to the electrochemical compartment. The H2 gas evolving from the electrochemical compartme...
The Pd membrane enables hydrogen permeation and chemical hydrogenation. The preparation of this membrane is, therefore, important to the efficacy of the membrane reactor. The Pd membrane size, crystallography, and surface are tuned to improve the experimental results. Although Pd metal can evolve hydrogen at any thickness, the Pd membranes are rolled to 25 µm. This standardization of membrane thickness ensures that the time it takes for hydrogen to permeate through the membrane is constant for all the experiments. M...
Patent applications based on the technology described in this work have been filed and published: Berlinguette, C. P.; Sherbo, R. S. "Methods and Apparatus for Performing Chemical and Electrochemical Reactions" US Patent Application No. 16964944 (PCT filed January 2019, national entry July 2020), Publication No. US20210040017A1 (published February 2021). Canadian Patent Application No. 3089508 (PCT filed January 2019, national entry July 2020), Publication No. CA3089508 (published August 2019). Priority data: US Provisional Patent Application No. 62/622,305 (filed January 2018).
We are grateful to the Canadian Natural Sciences and Engineering Research Council (RGPIN-2018-06748), the Canadian Foundation for Innovation (229288), the Canadian Institute for Advanced Research (BSE-BERL-162173), and Canada Research Chairs for financial support. This research was undertaken thanks in part to funding from the Canada First Research Excellence Fund, Quantum Materials and Future Technologies Program. We thank Ben Herring at the UBC Shared Instrument Facility for assistance with the GC-MS instrument and method development. We thank Dr. Monika Stolar for contributions to the development and editing of this manuscript. Finally, we thank the entire Berlinguette Group at the University of British Columbia for their continued support and collaboration in studying the membrane reactor.
Name | Company | Catalog Number | Comments |
Ag/AgCl Reference Electrode | BASi research products | MW-2021 | Reference electrode |
Analytical Balance | Cole-Parmer | RK-11219-03 | Instrument |
Atmospheric Mass Spectrometer | ESS CatalySys | NA | Instrument |
Bench Power Supply | Newark | 1550 | Instrument |
Conductive Copper Foil Electrical Tape | McMaster Carr | 76555A711 | Electrochemical cell assembly |
Dichloromethane | Sigma Aldrich | 270997 | Reagent |
Electric Rolling Press with Dual Micrometer | MTI Corporation | MR100A | Equipment |
Electrochemical glass H-cell | University of British Columbia glass blowing | NA | Electrochemical cell assembly |
ESS catalysis QUADSTAR | ESS CatalySys | NA | Software |
Ethanol | Sigma Aldrich | 493511 | Reagent |
Flat Rolling Mill | Pepetolls | 18700A | Equipment |
Gas Chromatography Mass Spectrometer | Agilent | NA | Instrument |
GC-MS vial | Agilent | 5067-0205 | Vial for GC-MS |
Hexanes | Sigma Aldrich | 1.0706 | Reagent |
Hydrochloric Acid | Sigma Aldrich | 258148 | Reagent |
Hydrogen peroxide solution (30% v/v) | Sigma Aldrich | H1009 | Reagent |
Isopropyl Alcohol | Sigma Aldrich | W292907 | Reagent |
Masshunter Aquisition Software | Agilent | G1617FA | Software |
Micropipette (100 µL - 1000 µL) | Gilson | F123602 | instrument |
Micropipette (20 µL - 200 µL) | Gilson | F123601 | Instrument |
Mitutoyo Digital Micrometer | Uline | H-2780 | Instrument |
Muffle Furnace | MTI Corporation | KSL-1100X | Equipment |
Nitric acid | Sigma Aldrich | 438073 | Reagent |
Nitrogen gas | Sigma Aldrich | 608661 | Reagent |
Palladium (II) Chloride | Sigma Aldrich | 520659 | Reagent |
Pd wafer bar, 1 oz, 99.95% | Silver Gold Bull. | NA | Reagent |
Platinum Auxiliary Electrode | BASi research products | MW-1032 | Anode |
Potentiostat | Metrohm | PGSTAT302N | Instrument |
Propiophenone | Sigma Aldrich | P51605 | Reagent |
Proton Exchange Membrane, Nafion 212 | Fuel cell store | NA | Electrochemical cell assembly |
Sulfuric acid | Sigma Aldrich | 258105 | Reagent |
Request permission to reuse the text or figures of this JoVE article
Request PermissionThis article has been published
Video Coming Soon
Copyright © 2025 MyJoVE Corporation. All rights reserved