ECOCAT · Improving the economic feasibility of the biorefinery through catalysis engineering: enhancing the catalyst performance and optimizing valuable product yields
Horizon 2020 — Marie Skłodowska-Curie Actions
- Duration
- 2018-01-15 → 2020-01-14
- EU contribution
- €183,455
- Participants
- 1
- Scheme
- MSCA-IF-EF-ST
Lines connect the coordinator with its partners.
Results in brief
Improving the economic feasibility of the biorefinery through catalysis engineering: enhancing the catalyst performance and optimizing valuable product yields
The growing energy demand globally, in combination with environmental concerns and concerns with the dependency on finite fossil energy resources and energy security, has spurred research into alternative energy resources. Lignocellulose is a non-edible, abundant and low-cost form of biomass that can be converted to a liquid renewable energy carrier (bio-oil) via a process known as fast pyrolysis. Bio-oil is a complex mixture of oxygenates derived from biomass and has some unfavourable properties that make its conversion to transportation biofuels very challenging. By incorporating a solid catalyst in the fast pyrolysis process, the biomass-derived products can be partially deoxygenated and a bio-oil with more favourable properties can be produced that can be upgraded to transportation fuels. The disadvantage of using a catalyst is the formation of byproducts such as coke, water and permanent gases. In addition, the need to periodically replace the catalyst has a significant impact on the economics of the process and the cost of the products. The aim of ECOCAT was to improve on the economics of catalytic fast pyrolysis by reducing catalyst-related operating costs. This can be achieved by the development of a more active catalyst with superior selectivity towards key valuable products. The most commonly used catalyst for catalytic fast pyrolysis is the ZSM-5 zeolite, a catalyst with a unique microporous structure that is very effective for the production of valuable monoaromatic hydrocarbons and for the minimisation of solid byproducts (coke). However, the microporous structure of ZSM-5 may not be optimal for the conversion of the large biomass-derived compounds that are formed during. As such, adding a degree of mesoporosity in the ZSM-5 may be beneficial for the cracking of the large compounds into smaller intermediates, which can then diffuse through the micropores to be converted to valuable deoxygenated products. In ECOCAT, ZSM-5 zeolites with varying degrees of added mesoporosity were synthesised. The mesoporous ZSM-5 zeolites were both more active and more selective than microporous ZSM-5 and gave consistently higher yields of desirable products.
Data: CORDIS, © European Union
Project objective
Catalytic pyrolysis of biomass is a process for the conversion of lignocellulosic biomass to a liquid product that has potential to be utilized as a fuel, a source of renewable chemicals and as an alternative to crude oil for upgrading to transportation fuels. ZSM-5 zeolite is the most studied catalyst for this process due to its acidity and shape-selectivity, which favour the conversion of biomass oxygenates to valuable aromatic hydrocarbons and limit the formation of coke. Among the shortcomings of the ZSM-5 zeolite is the small size of its pores; these small pores do not allow the large molecules in the pyrolysis vapours to access the active acid sites. Secondly, its sensitivity to biomass metals leads to poisoning and deterioration of its selectivity. Coupled with the high cost of the ZSM-5, the later leads to significant operating costs that arise from the necessity to replace the deactivated catalyst with fresh material at high rates.The objective of this proposal is to investigate and improve on the economics of the process by reduction of catalyst-related operating costs and optimization of catalyst selectivity towards desirable products. This is going to be achieved through utilization of microporous zeolites modified with mesoporosity. Mixed results have been reported with such zeolites in the past. To address this, a suitable experimental procedure will be developed for the systematic study of mesoporosity through assessment of multiple aspects of catalyst performance, such as activity, selectivity, coke suppression and deoxygenation. Increased activity and selectivity is expected to result from increased accessibility of larger molecules to the zeolite acid sites. In order to address the short lifetime of the catalyst, the mechanism of poisoning from biomass metals will also be studied and modification of the catalyst, tentatively with implementation of materials more reactive to biomass metals, will be investigated in order to extend its lifetime.
Original text from CORDIS.
Participants
- ASTON UNIVERSITY · BirminghamCoordinatorUnited Kingdom
Links
Data: CORDIS, © European Union
