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    Feasibility analysis of a CO2 recycling plant for the decarbonization of formate and dihydroxyacetone production

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    Identificadores
    URI: http://hdl.handle.net/10902/23797
    DOI: 10.1039/d1gc01042e
    ISSN: 1463-9262
    ISSN: 1463-9270
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    Autoría
    Rumayor Villamil, MartaAutoridad Unican; Domínguez Ramos, AntonioAutoridad Unican; Irabien Gulías, ÁngelAutoridad Unican
    Fecha
    2021-07-07
    Derechos
    © Royal Society of Chemistry
    Publicado en
    Green Chemistry, 2021, 23(13), 4840-4851
    Editorial
    Royal Society of Chemistry
    Enlace a la publicación
    https://doi.org/10.1039/d1gc01042e
    Palabras clave
    Decarbonization
    Carbon footprint
    Carbon recycling plant
    Carbon dioxide utilization
    Environmental assessment
    Techno-economic assessment
    Resumen/Abstract
    Renewable-driven CO2 recycling plants (CO2RPs) to produce chemicals have a certain role to play in the decarbonization of the economy. In recent years, significant progress has been made in the decarbonization of chemicals such as formate/formic acid (HCOO-/HCOOH) by CO2 electrochemical reduction (CO2ER). The traditional approach consists of the cathodic CO2ER coupled to the anodic oxygen evolution reaction (OER). Current trends consist of alternative anodic processes, such as glycerol (GLY) electro-oxidation (EOG), as a powerful alternative to the OER because it can noticeably lower the cell voltage. Also, this recent alternative leads to the formation of products in the anode with more economic value than O2, for example, the fine chemical dihydroxyacetone (DHA). Until now factors other than just the energy savings in the ER cell have been neglected. But these factors, such as the anodic market size, the downstream separation energy demand, etc., have to be contemplated in the whole decarbonization picture. In the present study, we analyze the environmental and economic benefits of the integrated production of HCOO- and DHA by a renewable-driven CO2RP in which the traditional OER is substituted by the EOG alternative. Life Cycle Thinking was used to support the decision-making. HCOO- and DHA fossil routes as well as the traditional decarbonization OER scheme (that decarbonized the amount of HCOO-) were used for benchmarking. The integrated production in the proposed CO2RP is highly limited by the small market size of DHA compared to that of HCOO- and also by the high energy requirements in the DHA purification step. Anodic DHA concentration over 1.5 wt% is compulsory in short-mid-term developments to achieve a positive decarbonization scenario wherein the integrated production of DHA and HCOO- is compared with the traditional route. A noticeable reduction in the market price of DHA would be possible with appropriate anode developments. In addition, we evaluate the influence of the renewable electricity market forecast in the economic figures of DHA and HCOO- produced by the co-electrolysis technology.
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    UNIVERSIDAD DE CANTABRIA

    Repositorio realizado por la Biblioteca Universitaria utilizando DSpace software
    Contacto | Sugerencias
    Metadatos sujetos a:licencia de Creative Commons Reconocimiento 4.0 España