Estudo da incorporação de lantânio na zeólita beta na reação de tiofeno em uma corrente de cicloexano em condições de FCC

Autores

  • Vanessa Nascimento Monteiro Universidade Federal da Bahia (UFBA) Autor
  • Daniel Freire Almeida Universidade Federal da Bahia (UFBA) Autor https://orcid.org/0000-0002-1386-1753
  • Anderson Cerqueira dos Santos Silva Universidade Federal da Bahia (UFBA) Autor
  • Amanda Lienthier da Silva Universidade Federal da Bahia (UFBA) Autor
  • Zaíne Baldoino Silva Universidade Federal da Bahia (UFBA) Autor
  • Ronaldo Costa Santos Centro Universitário SENAI-CIMATEC Autor https://orcid.org/0000-0002-3972-8061
  • Luiz Antônio Magalhães Pontes Universidade Federal da Bahia (UFBA) Autor https://orcid.org/0000-0003-4158-4033

Palavras-chave:

FCC , dessulfurização, lantânio, zeólita Beta

Resumo

Strategies for desulfurization in refineries have become essential in response to increasingly stringent environmental regulations that reduce the sulfur limits in gasoline due to concerns over pollutant emissions. The Fluid Catalytic Cracking (FCC) unit plays a key role in gasoline production, making it crucial to develop technologies that maximize sulfur compound removal without compromising economic profitability. A promising approach involves the use of sulfur-reducing additives mixed with the FCC catalyst to achieve in situ reduction of these contaminants during the cracking reaction process. This study focuses on the catalytic cracking of thiophene in a cyclohexane stream using Beta zeolite (SAR 18) modified with lanthanum. The catalyst was prepared by diffusional wet impregnation, with a lanthanum content of approximately 6 wt%. Physicochemical characterizations, including XRF, XRD, structural FTIR, and N2 physisorption isotherms, were performed to compare the lanthanum catalyst (La-B) with the pure zeolite (H-B). The reaction was carried out at 500 °C using 250 mg of catalyst, with a WHSV of 3,7 h⁻¹, in a bench-scale testing unit designed for sulfur-containing molecule transformations, containing a coupled GC-FID/SCD. The sulfur content of 2 wt% (20000 ppm wt/wt) in cyclohexane was chosen to represent FCC feed conditions. Cyclohexane conversion ranged from 80-84 %mol, and thiophene conversion was 78-85 %mol. Both catalysts were selective towards cracking reactions of cyclohexane and thiophene, with a selectivity to H₂S range of 83-85 %mol. However, the lanthanum-incorporated catalyst proved more effective as a sulfur-reducing additive in gasoline, as it generated fewer condensed products and exhibited greater resistance to deactivation during both hydrocarbon and sulfur compound reactions.

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Publicado

15-11-2024

Edição

Seção

Catálise aplicada na produção de combustíveis, biocombustíveis, produtos químicos e energia.

Como Citar

NASCIMENTO MONTEIRO, Vanessa; FREIRE ALMEIDA, Daniel; CERQUEIRA DOS SANTOS SILVA, Anderson; LIENTHIER DA SILVA, Amanda; BALDOINO SILVA, Zaíne; COSTA SANTOS, Ronaldo; MAGALHÃES PONTES, Luiz Antônio. Estudo da incorporação de lantânio na zeólita beta na reação de tiofeno em uma corrente de cicloexano em condições de FCC. XIV Encontro de Catálise do Norte, Nordeste e Centro-Oeste, Brasil, 2024. Disponível em: https://submissao.sbcat.org/index.php/xivencat/article/view/89. Acesso em: 26 dez. 2024.

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