Jasper
van Kampen
*ab,
Saskia
Booneveld
a,
Jurriaan
Boon
ab,
Jaap
Vente
a and
Martin
van Sint Annaland
b
aBiomass and Energy Efficiency, TNO Energy Transition, P. O. Box 15, 1755 ZG Petten, The Netherlands. E-mail: jasper.vankampen@tno.nl
bChemical Process Intensification, TU/e, P. O. Box 513, 5600 MB Eindhoven, The Netherlands. E-mail: j.v.kampen@tue.nl
First published on 2nd October 2020
Sorption enhanced dimethyl ether synthesis (SEDMES) is a novel DME production route from CO2-rich feedstocks. In situ water removal by adsorption results in high single-pass conversions, thereby circumventing the disadvantages of conventional routes, such as low carbon efficiency, energy intensive downstream separation and large recycling. The first-time demonstration of pressure swing regeneration with 80% single-pass carbon selectivity to DME allows for an enormous increase in productivity. Already a factor four increase compared to temperature swing regeneration is achieved, unlocking the potential of SEDMES as a carbon utilisation technology.
Sorption enhanced DME synthesis is validated experimentally using a 2 litre bench-scale reactor, details of which are provided in the ESI.†Fig. 1 shows a representative breakthrough experiment of sorption enhanced DME synthesis. CO2-rich syngas (CO2:CO = 2:1, stoichiometric H2), as typical for biomass-derived syngas, is fed to a previously regenerated column, at 250–275 °C and 25 bar, containing a homogeneous mixture of a CuZnAl catalyst, a γ-Al2O3 catalyst, and a 3A zeolite adsorbent, all of which are commercially available. The reactor outlet composition is measured using mass spectrometry and gas chromatography, as shown in Fig. 1. Prior to steam breakthrough, DME and unconverted CO are the primary products. After steam breakthrough, the concentration of DME drops, accompanied by the breakthrough of CO2 and methanol, indicating saturation of the adsorbent. These bench-scale test results demonstrate high performance with over 80% integral carbon selectivity towards DME when using pressure swing regeneration, without the need for a temperature swing, for the first time in the open literature. In Fig. 2 the experimental carbon distribution for SEDMES at 275 °C is shown, indicating the single-pass conversion increase from 18% for conventional synthesis (represented as the thermodynamic equilibrium) to 68%. Crucially, the experiment serves to show how a similar conversion and selectivity can be obtained with pressure swing regeneration (PSA) in comparison with previously reported experiments with a combined temperature and pressure swing regeneration (TPSA). As no time is required for heating and cooling, the adsorbent regeneration time can be reduced from 360 minutes to 60 minutes under the current conditions (Fig. 2). As a result, the DME productivity is already increased by a factor of four, with further optimisation possible.
Following the proof of feasibility of pressure swing regeneration, the cycle design of the sorption enhanced process becomes essential. The combination of the adsorption duration (ADS) and regeneration time (DES) allows optimising the trade-off for DME selectivity and productivity, which is shown in Fig. 3. Shorter adsorption times potentially result in an increased production rate. The larger reactor column requirement (m3) when the purge time does not decrease with the adsorption time, however, results in a drop in cyclic productivity (kg h−1 m−3). Considering the minimum number of columns required for any given adsorption and purge time, the productivity could be significantly boosted for shorter cycle times with the highest ADS/DES ratio (red bars in Fig. 3). The productivities reported in Fig. 3 correspond to 0.04–0.06 kg h−1 kgcat−1. This is a major improvement compared to the previously reported TPSA cycle and close to direct DME pilot plant productivity for CO to DME, which would strongly deteriorate for CO2-rich feed.13
This increase in productivity shows the impact of the demonstrated PSA regeneration on the SEDMES process performance. Benefiting from this work, optimisation of the cycle design by means of modelling and experimental validation should further unlock the potential of SEDMES as an efficient carbon utilisation technology. Followed by the techno-economic and life cycle analyses, the economic and carbon mitigating benefits of SEDMES over conventional DME synthesis technology can also now be addressed.
This work has received funding from the European Union's Horizon 2020 Research and Innovation Programme under grant agreement no. 727600.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d0cc06093c |
This journal is © The Royal Society of Chemistry 2020 |