2020
DOI: 10.1016/j.jcou.2020.101195
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Selective CO2 hydrogenation into methanol in a supercritical flow process

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Cited by 34 publications
(41 citation statements)
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“…Understanding the cost and magnitudes of the required infrastructure is a key element for the implementation of the land-neutral methanol pathway. While hydrogenation of CO 2 to produce methanol has received significant attention in industry and academia 37 , including major R&D efforts in Brazil 38 , recent estimates of power-to-methanol processes show that they are significantly more costly than their fossil counterparts 39 , 40 . However, our proposed pathway includes important elements that can make green methanol more competitive: the size of H 2 and CO 2 storage is optimized to maximize capital utilization 41 , while the almost pure and low-cost CO 2 stream from the ethanol production process can further reduce the cost.…”
Section: Introductionmentioning
confidence: 99%
“…Understanding the cost and magnitudes of the required infrastructure is a key element for the implementation of the land-neutral methanol pathway. While hydrogenation of CO 2 to produce methanol has received significant attention in industry and academia 37 , including major R&D efforts in Brazil 38 , recent estimates of power-to-methanol processes show that they are significantly more costly than their fossil counterparts 39 , 40 . However, our proposed pathway includes important elements that can make green methanol more competitive: the size of H 2 and CO 2 storage is optimized to maximize capital utilization 41 , while the almost pure and low-cost CO 2 stream from the ethanol production process can further reduce the cost.…”
Section: Introductionmentioning
confidence: 99%
“…To couple the RWGS and FTS processes in tandem, the two processes should be carried out at the same pressure, i. e., � 20-30 bar. However, higher operational pressures will favor the CO 2 methanation pathway, [5,9] which will increase the selectivity to CH 4 and will hinder the FTS pathway. Since Ni 3 ZnC@NC was able to carry out only the RWGS pathway at atmospheric pressure, its activity was also studied at high-pressure conditions to evaluate its suitability for a RWGS/FT tandem process.…”
Section: Samplementioning
confidence: 99%
“…[2] The conversion of CO 2 in industrial processes is restricted to few examples, such as the synthesis of urea, salicylic acid, carboxylic acids, methanol, organic carbonates, and polycarbonates. [3] Considerable progress has been made towards the hydrogenation of CO 2 to C1 products (e. g., CO, CH 4 , CH 3 OH, and HCOOH), [4,5] while the hydrogenation of CO 2 into high-value C 2 + products is still challenging. In this case, the key is developing more selective catalysts that will hinder C1 byproducts.…”
Section: Introductionmentioning
confidence: 99%
“…Por sua vez, a utilização de CO 2 supercrítico (scCO 2 ) (P c = 73 bar e 31 °C) não tem sido particularmente muito estudada na conversão de CO 2 a metanol através de catálise heterogénea. Evdokimenko et al [49] e Bogdan et al [50] relataram, respetivamente, a hidrogenação de CO 2 a monóxido de carbono e a metano em condições supercríticas utilizando diferentes catalisadores. Porém, nenhum dos autores estudou a reação abaixo do ponto crítico da mistura, e por isso estes estudos não permitem esclarecer por completo o efeito benéfico das condições supercríticas na taxa de conversão e seletividade.…”
unclassified
“…Recentemente o nosso grupo descreveu um processo de fluxo em condições supercríticas utilizando o catalisador ReO x /TiO 2 (Figura 3) [50]. O uso de uma pressão elevada permitiu que este sistema convertesse uma apreciável quantidade de CO 2 quase exclusivamente em metanol.…”
unclassified