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                  <mods:namePart>Santos, Ronaldo C.</mods:namePart>
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                  <mods:namePart>Silva, Anderson Cerqueira dos Santos</mods:namePart>
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                  <mods:namePart>Lam, Yiu Lan</mods:namePart>
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                  <mods:namePart>Ferreira, Jose Marcos Moreira</mods:namePart>
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                  <mods:namePart>Ballesteros-Plata, Daniel</mods:namePart>
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                  <mods:namePart>Rodríguez-Castellón, Enrique</mods:namePart>
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               <mods:name>
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                  <mods:namePart>Martínez Arribas, Agustin</mods:namePart>
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               <mods:name>
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                  <mods:namePart>Pontes, Luiz A. M.</mods:namePart>
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                  <mods:dateAccessioned encoding="iso8601">2025-09-26T09:22:44Z</mods:dateAccessioned>
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               <mods:identifier type="citation">R. C. Santos, D. F. Almeida, A. C. dos S. Silva, et al. “ Modulation of the Acidity of HY, HBETA, and HZSM-5 Zeolites by Lanthanum Incorporation for Selective Gasoline Desulfurization in the FCC Riser.” ChemCatChem 17, no. 21 (2025): e00888. https://doi.org/10.1002/cctc.202500888</mods:identifier>
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               <mods:identifier type="doi">10.1002/cctc.202500888</mods:identifier>
               <mods:abstract>This study evaluates the incorporation of lanthanum into zeolites&#xd;
Y, Beta, and ZSM-5 to promote the desulfurization of a gasoline&#xd;
stream directly in the riser of a fluid catalytic cracking (FCC) process.&#xd;
The catalysts were prepared using wet impregnation and&#xd;
characterized by X-ray diffraction (XRD) (crystallinity and phase&#xd;
integrity), XRF (La content and Si/Al ratio), X-ray photoelectron&#xd;
spectroscopy (XPS), solid state nuclear magnetic resonance&#xd;
(NMR) of 29Si and 27Al, N2 adsorption, high-resolution transmission&#xd;
electron microscopy (HRTEM), temperature-programmed&#xd;
desorption of ammonia (TPD-NH3), Fourier-transform infrared&#xd;
spectroscopy (FTIR), and pyridine chemisorbed FTIR (FTIR-Py).&#xd;
Catalytic tests were conducted in a tubular reactor, using a mixture&#xd;
of cyclohexane and thiophene (20000 ppm) at 773 K and&#xd;
1.3 atm. Catalytic activity was assessed in a fixed-bed reactor&#xd;
using a cyclohexane/thiophene feed, and product selectivities&#xd;
were quantified by gas chromatography with flame ionization&#xd;
and sulfur chemiluminescence detectors. The addition of lanthanum&#xd;
altered the acidity of the catalysts, reducing the total&#xd;
density of acid sites while increasing the strength of Lewis acid&#xd;
sites. The protonated zeolites, particularly HY, facilitated sulfur&#xd;
removal, achieving a 91% selectivity for H2S through secondary&#xd;
hydrogen transfer reactions. In contrast, the lanthanum-modified&#xd;
zeolites enhanced thiophene alkylation and condensation reactions,&#xd;
as evidenced by the selectivity observed in La/BEA and&#xd;
La/ZSM-5, which reached 15%. The results indicated that incorporating&#xd;
lanthanum changes the desulfurization profile, making&#xd;
the catalysts more selective for forming higher molecular weight&#xd;
sulfur compounds, thereby shifting the products toward the FCC&#xd;
diesel range.</mods:abstract>
               <mods:language>
                  <mods:languageTerm authority="rfc3066">eng</mods:languageTerm>
               </mods:language>
               <mods:accessCondition type="useAndReproduction">Atribución 4.0 Internacional</mods:accessCondition>
               <mods:subject>
                  <mods:topic>Catálisis heterogénea</mods:topic>
               </mods:subject>
               <mods:subject>
                  <mods:topic>Petróleo - Refino</mods:topic>
               </mods:subject>
               <mods:subject>
                  <mods:topic>Industria petroquímica</mods:topic>
               </mods:subject>
               <mods:subject>
                  <mods:topic>Materiales porosos</mods:topic>
               </mods:subject>
               <mods:subject>
                  <mods:topic>Zeolitas</mods:topic>
               </mods:subject>
               <mods:titleInfo>
                  <mods:title>Modulation of the Acidity of HY, HBETA, and HZSM-5 Zeolites by Lanthanum Incorporation for Selective Gasoline Desulfurization in the FCCRiser</mods:title>
               </mods:titleInfo>
               <mods:genre>journal article</mods:genre>
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