Next Article in Journal
Studies on Photocatalytic Degradation of Methylene Blue Using TiO2—Transition Metal Oxides Heterojunctions
Previous Article in Journal
Early Changes in Observed Eating Behaviours and Suboptimal Weight Loss in Gastric Bypass Patients: Preliminary Findings
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Abstract

Sustainable Chemistry through Catalysis and Process Intensification †

Johan Gadolin Process Chemistry Centre, Laboratory of Industrial Chemistry and Reaction Engineering, Åbo Akademi University, 20500 Turku, Finland
Presented at the International Conference EcoBalt 2023 “Chemicals & Environment”, Tallinn, Estonia, 9–11 October 2023.
Proceedings 2023, 92(1), 76; https://doi.org/10.3390/proceedings2023092076
Published: 13 December 2023
(This article belongs to the Proceedings of International Conference EcoBalt 2023 "Chemicals & Environment")
The shift away from fossil resources is revolutionizing our industrial carbon sources, and the developments in legislation demand increased overall efficiency in processes and emission abatement. Catalysis plays a key role in enabling the green transition in the chemical process industry and environmental protection. They also act as a bridge between chemical reactions and reaction mechanisms and moving from the molecular to the process scale. Besides enhancing reaction rates, increasing selectivity plays a key role, and both of these factors are tightly linked also to the process design and optimization for which modern process intensification provides good tools. The current presentation displays three examples of combining heterogeneous catalysis with process intensification for wastewater treatment and the direct conversion of CO2 recently studied by our research group. The wastewater treatment includes removing hemicelluloses from dilute biorefinery effluents with the help of catalytic aqueous-phase reforming in a continuous reactor [1,2,3,4]. The second case focuses on the removal of pharmaceuticals from communal wastewaters by combining ozonation with heterogeneous catalysis in a semi-batch reactor operating at ambient pressure [5,6,7]. In the case focusing on gas-phase processing, CO2 is converted to renewable natural gas utilizing a bi-functional catalytic material in a periodically operating continuous reactor concept [8,9,10,11,12]. Chromatography was used as the main analysis method in all of the experiments. High yields and good selectivity were obtained in all of the cases, and the next steps are related to process optimization, stability testing, and preparative studies for scale-up studies. The obtained results display significant potential for green process technology and process efficiency by combining catalyst development with process design to be able to efficiently utilize effluent streams and minimize the effects on the environment.

Funding

This research was financially supported by the Academy of Finland, Business Finland, and Tekniikan Edistämissäätiö.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

Data is available via the cited articles and from the corresponding author.

Conflicts of Interest

The author declares no conflict of interest.

References

  1. Aho, A.; Alvear, M.; Ahola, J.; Kangas, J.; Tanskanen, J.; Simakova, I.; Santos, J.; Eränen, K.; Salmi, T.; Murzin, D.Y.; et al. Aqueous phase reforming of birch and pine hemicellulose hydrolysates. Bioresour. Technol. 2022, 348, 126809. [Google Scholar] [CrossRef] [PubMed]
  2. Aho, A.; Õna, J.P.; Rosales, C.; Eränen, K.; Salmi, T.; Murzin, D.Y.; Grénman, H. Biohydrogen from dilute side streams—Influence of reaction conditions on the conversion and selectivity in aqueous phase reforming of xylitol. Biomass Bioenergy 2020, 138, 105590. [Google Scholar] [CrossRef]
  3. Alvear, M.; Aho, A.; Simakova, I.; Grénman, H.; Salmi, T.; Murzin, D.Y. Aqueous phase reforming of alcohols over a bimetallic Pt-Pd catalyst in the presence of formic acid. Chem. Eng. J. 2020, 398, 15–125541. [Google Scholar] [CrossRef]
  4. Alvear, M.; Aho, A.; Simakova, I.; Grénman, H.; Salmi, T.; Murzin, D.Y. Aqueous phase reforming of xylitol and xylose in the presence of formic acid. Catal. Sci. Technol. 2020, 10, 5245–5255. [Google Scholar] [CrossRef]
  5. Saeid, S.; Tolvanen, P.; Kumar, N.; Eränen, K.; Peltonen, J.; Peurla, M.; Mikkola, J.P.; Franz, A.; Salmi, T. Advanced oxidation process for the removal of ibuprofen from aqueous solution: A non-catalytic and catalytic ozonation study in a semi-batch reactor. Appl. Catal. B Environ. 2018, 230, 77–90. [Google Scholar] [CrossRef]
  6. Saeid, S.; Kråkström, M.; Tolvanen, P.; Kumar, N.; Eränen, K.; Mikkola, J.P.; Kronberg, L.; Eklund, P.; Peurla, M.; Aho, A.; et al. Advanced oxidation process for degradation of carbamazepine from aqueous solution: Influence of metal modified microporous, mesoporous catalysts on the ozonation process. Catalysts 2020, 10, 90. [Google Scholar] [CrossRef]
  7. Kråkström, M.; Saeid, S.; Tolvanen, P.; Salmi, T.; Kronberg, L.; Eklund, P. Catalytic ozonation of the antibiotic sulfadiazine: Reaction kinetics and transformation mechanisms. Chemosphere 2020, 247, 125853. [Google Scholar] [CrossRef] [PubMed]
  8. Wei, L.; Haije, W.; Grénman, H.; de Jong, W. Sorption enhanced catalysis for CO2 hydrogenation towards fuels and chemicals with focus on methanation. In Heterogeneous Catalysis; Elsevier: Amsterdam, The Netherlands, 2022; pp. 95–119. [Google Scholar]
  9. Wei, L.; Azad, H.; Hamza; Haije, W.; Grénman, H.; de Jong, W. Pure methane from CO2 hydrogenation using a sorption enhanced process with Catalyst/Zeolite bifunctional materials. Appl. Catal. B Environ. 2021, 297, 120399. [Google Scholar] [CrossRef]
  10. Wei, L.; Grénman, H.; Haije, W.; Kumar, N.; Aho, A.; Eränen, K.; Wei, L.; de Jong, W. Sub-nanometer ceria-promoted Ni 13X zeolite catalyst for CO2 methanation. Appl. Catal. A Gen. 2021, 612, 118012. [Google Scholar] [CrossRef]
  11. Wei, L.; Haije, W.; Kumar, N.; Peltonen, J.; Peurla, M.; de Jong, W.; Grénman, H. The influence of nickel precursors on the properties and performance of Ni impregnated zeolite 5A and 13X supported catalysts in CO2 methanation. Catal. Today 2021, 362, 35–46. [Google Scholar] [CrossRef]
  12. Wei, L.; Haije, W.; Kumar, N.; de Jong, W.; Grénman, H. Can bi-functional nickel modified 13X and 5A zeolite catalysts for CO2 methanation be improved by introducing ruthenium? Mol. Catal. A 2020, 494, 111115. [Google Scholar] [CrossRef]
Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

Share and Cite

MDPI and ACS Style

Grénman, H. Sustainable Chemistry through Catalysis and Process Intensification. Proceedings 2023, 92, 76. https://doi.org/10.3390/proceedings2023092076

AMA Style

Grénman H. Sustainable Chemistry through Catalysis and Process Intensification. Proceedings. 2023; 92(1):76. https://doi.org/10.3390/proceedings2023092076

Chicago/Turabian Style

Grénman, Henrik. 2023. "Sustainable Chemistry through Catalysis and Process Intensification" Proceedings 92, no. 1: 76. https://doi.org/10.3390/proceedings2023092076

APA Style

Grénman, H. (2023). Sustainable Chemistry through Catalysis and Process Intensification. Proceedings, 92(1), 76. https://doi.org/10.3390/proceedings2023092076

Article Metrics

Back to TopTop