12 results on '"Puello-Polo, Esneyder"'
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2. One-pot synthesis of Nb-modified Al2O3 support for NiMo hydrodesulfurization catalysts
- Author
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Puello-Polo, Esneyder, Marquez, Edgar, and Brito, J. L.
- Published
- 2018
- Full Text
- View/download PDF
3. Efecto de la modificación del soporte con níquel y la promoción con cobre en la reacción competitiva de Hidrosulfuración de Dibenzotiofeno e Hidrodesnitrogenación de Carbazol utilizando catalizadores CuMo-Ni/γ-Al2 O3.
- Author
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Montaño Herazo, Ana, Navarro Barraza, Félix, and Puello-Polo, Esneyder
- Subjects
X-ray fluorescence ,COPPER ,SURFACE area ,DESULFURIZATION ,DIBENZOTHIOPHENE - Abstract
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- Published
- 2023
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- View/download PDF
4. Enhanced hydrotreating performance of hierarchical NiMo-S/Al2O3 catalysts through ZrO2 incorporation and template-driven structural modulation.
- Author
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Puello-Polo, Esneyder, Betancourt, Paulino, and Méndez, Franklin J.
- Subjects
- *
ALUMINUM oxide , *CATALYTIC activity , *ACTIVATED carbon , *HYDROCRACKING , *DESULFURIZATION - Abstract
A dual template-assisted approach for optimizing support structures to enhance catalytic efficiency in hydrotreating reactions is presented. Catalysts synthesized using activated carbon (AC) templates exhibited significantly higher activity in both hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) compared to those prepared with starch (ST) templates. The unique porous architecture, characterized by well-distributed meso- and macropores, facilitated efficient access of bulky molecules to the active sites. On the other hand, while the reactivity in the selective opening of the naphthenic ring (SONR), which is indicative of hydrocracking functionality, was similar across all catalysts, those modified with Zr exhibited a slight improvement. The catalysts displayed bifunctional characteristics, and their performance was influenced by the amphoteric nature of the support and the specific ratios of active species on the surface. A clear correlation between catalytic activity, selectivity, and the distribution of active sites was established. • Catalysts exhibited promising HDS and HDN activities. • The selection of template agents and Zr-loading significantly influenced the catalyst's performance. • Limited hydrocracking functionality suggested a role of the amphoteric character of the Al 2 O 3 -ZrO 2 support. • Catalysts using activated carbon templates outperform those with starch templates in HDS and HDN reactions. • Unique porous structure with well-distributed meso- and macropores enhances access of bulky molecules to active sites, contributing to superior activity. [ABSTRACT FROM AUTHOR]
- Published
- 2025
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5. Síntesis y caracterización de heteropolioxometalatos tipo anderson de Ni-Mo(W) soportados sobre alúmina: Actividad de hidrodesulfuración de tiofeno
- Author
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Julio-Julio, Javier José, Puello-Polo, Esneyder, and Brito, Joaquín
- Subjects
heteropolioxometalatos tipo Anderson ,NiMo(W) ,oxidic precursor ,hidrodesulfuración ,precursor oxídicos ,Anderson type heteropolyoxometalates ,hydrodesulfurization - Abstract
Se sintetizaron heteropolioxometalatos tipo Anderson (NH4)4[NiMo6-xWxO24H6]·5H2O soportados sobre γ-Al3O2, utilizando el método de coprecipitación. Estos solidos fueron utilizados como precursores en la reacción de hidrodesulfuración (HDS) de tiofeno a 400°C. Los precursores catalíticos se caracterizaron por propiedades texturales (área específica (B.E.T) y, distribución del diámetro y volumen de poros), difracción de rayos X (DRX), espectroscopía infrarroja (FT-IR) y análisis elemental (CHON-S). Las áreas específicas estuvieron dentro del intervalo de 109 y 35 m²/g con una distribución del diámetro y volumen de poros de 8,9-9,6 nm y 0,11-0,34 cm³/g, respectivamente. El análisis por DRX mostró la presencia de NiWO4, (NH4)4[NiMo6O24H6]·5H2O y WO3. Los análisis FT-IR determinaron la obtención de la estructura tipo Anderson, debido a las distintas flexiones y estiramientos de los grupos funcionales presentes. El precursor NiMo6-O/Al fue el más activo en la HDS, con un porcentaje de conversión de 72,75% e incluso fue más activo que el catalizador comercial AERO. Los resultados de HDS revelaron que la actividad catalítica en HDS se incrementa en el orden: NiMo6-O/Al > AERO > NiMo3W3-O/Al > NiW6-O/Al. La selectividad catalítica de precursores y el catalizador comercial (AERO) estuvo dirigida hacia cis-buteno. Alumina supported (NH4)4[NiMo6-xWxO24H6]·5H2O Anderson type heteropolyoxometalates were synthesized by coprecipitation. These solids were used as precursors in the thiophene hydrodesulfurization catalytic at 400°C. The catalytic precursors were characterized by textural properties (BET specific surface area and, total pore volume and pore diameter distribution), X-ray diffraction (XRD), IR spectroscopy (FTIR) and S analysis (CHON-S). The specific surface area was between 109 and 35 m²/g with total pore volume and pore diameter distribution of 0,11-0,34 cm³/g and 8,9-9,6 nm, respectively. XRD showed the presence of NiWO4, (NH4)4[NiMo6O24H6]·5H2O and WO3. FTIR analysis can be assigned to the characteristic vibrations of Anderson-type structure, due to stretching and bending of the functional groups present. The NiMo6-O/Al precursor was the most active in the HDS, it had a conversion of 72,75% and was even more active than the AERO commercial catalyst. The results of HDS revealed that the catalytic activity increases as follows: NiMo6-O/Al > AERO > NiMo3W3-O/Al > NiW6-O/Al. The catalytic selectivity of precursors and commercial catalyst (AERO) was directed towards the cis-butene.
- Published
- 2016
6. Titanium-modified MCM-41 molecular sieves as efficient supports to increase the hydrogenation abilities of NiMoS and CoMoS catalysts.
- Author
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Méndez, Franklin J., Vargas, Roylena, Blanco, Joel, Rojas-Challa, Yahsé, Bastardo-González, Ernesto, García-Macedo, Jorge A., Puello-Polo, Esneyder, and Brito, Joaquín L.
- Subjects
MOLECULAR sieves ,FOURIER transform infrared spectroscopy ,CATALYSTS ,CATALYST supports ,HYDROGENATION ,MICELLAR solutions - Abstract
• Ti modified samples induced better-dispersed catalysts. • HDS rates improved with Ti incorporation compared with the analog Ti free catalysts. • Ti atoms acted as anchor sites, decreasing both stacking and length of the MoS 2 slabs. • The hydrogenation abilities increased when Ti atoms were incorporated. Ti modified MCM-41-supported NiMo and CoMo catalysts and their respective Ti free reference catalysts were prepared, characterized, and tested for the hydrodesulfurization reactions. The samples were synthesized by well-known procedures, such as liquid crystal templating and successive impregnation method for the supports and catalysts, respectively. Ti precursor was directly incorporated into the micellar solution before adding the silica precursor at different molar Si/Ti ratios (x = 75 and 50). Fourier transform infrared spectroscopy, solid-state
29 Si-nuclear magnetic resonance, small- and wide-angle X-ray diffraction, and nitrogen physisorption were used as characterization techniques. Four sulfided catalysts were also characterized by high-resolution transmission electron microscopy. The catalysts showed important increases in the reaction rates during both thiophene and dibenzothiophene hydrodesulfurization when the support was structurally modified with Ti-atoms. The samples supported on Ti-MCM-41(75) presented a higher activity than those supported on Ti-MCM-41(50), and they were superior to their respective Si-MCM-41-supported NiMoS and CoMoS catalysts, even NiMoTiM75 and CoMoTiM75 catalysts presented better performance compared to the conventional NiMo/Al 2 O 3 and CoMo/Al 2 O 3 catalysts in the DBT hydrodesulfurization. Ti incorporation also enhanced the selectivities to the hydrogenated products, which could be beneficial to destabilize refractory S-containing molecules. [ABSTRACT FROM AUTHOR]- Published
- 2021
- Full Text
- View/download PDF
7. Efecto de la modificación del soporte con galio y la promoción con vanadio en la hidrodesulfuración de dibenzotiofeno utilizando catalizadores NiMoV-S/Al2O3-Ga2O3.
- Author
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Romero Suarez, Jonatan E., Moreno Córdoba, German A., and Puello-Polo, Esneyder
- Abstract
The effect of support modification with nickel and promotion with copper on the competitive reaction of DBT hydrodesulfurization and carbazole hydrodesnitrogenation using NiMoV-S/Al2O3-Ga2O3 catalysts was evaluated. The catalysts were characterized by X-ray fluorescence (FRX), specific surface area (BET), Fourier-transform infrared spectroscopy (FT-IR), temperature-programmed reduction (TPR), and determination of acidic sites. FRX showed that the Mo/Ni atomic ratio was 6.2 and 5.2 for methods 1 and 2, respectively. Adsorption-desorption isotherms confirmed the formation of mesoporous materials with specific areas ranging from 124 to 272 m2/g. FTIR revealed the presence of stretches attributable to polyoxomolybdates for all catalysts and the modification of supports with gallium showed Ga-O-Ga and Ga-O-Al assignments, while unmodified alumina exhibited characteristic signals of Al-O (AlO4 and AlO6) and O=Al-OH. TPR indicated increased metal-support interaction for NiMoV-S/Al and NiMoV-S/Al-Ga-M2 related to the modification method and the presence of V. Both catalysts and support exhibited weak and very weak acidity, respectively. The catalyst obtained through method 1 was more active for DBT removal: NiMoV-S/Al-Ga-M2 < NiMo/Al < NiMoV-S/Al-Ga-M1 with global pseudo-first-order rate constants (k) of 1.86, 2.48, and 8.50 L/(h·mol·m2), respectively. [ABSTRACT FROM AUTHOR]
- Published
- 2024
- Full Text
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8. Carburos de Cobalto-Molibdeno soportados sobre carbón activado: efecto del método de síntesis, velocidad de calentamiento, tipo de precursor de cobalto y agente presulfurante en la hidrodesulfuración de tiofeno
- Author
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Puello-Polo, Esneyder, Ayala, Mónica V, and Brito, Joaquín L
- Subjects
tipo de precursor de Co ,Hydrodesulfurization ,heating rate ,presulfiding agent ,synthesis methods ,Hidrodesulfuración ,velocidad de calentamiento ,Co precursor type ,agente presulfurante ,carbón activado ,carburos de Co-Mo ,métodos de síntesis ,activated carbon ,Co-Mo carbides - Abstract
Se estudió el efecto del método de síntesis, tipo de precursor de cobalto, velocidad de calentamiento y agente presulfurante de carburos de Co-Mo soportados sobre carbón activado en la actividad catalítica de hidrodesulfuración (HDS) de tiofeno. La síntesis se llevó a cabo utilizando los métodos carbotérmico con H2 y convencional (CH4/H2 (1:4)) a 973 K y 1 o 5 K/min. Las fases carburadas se caracterizaron por área específica (B.E.T), difracción de rayos X (DRX) y espectroscopía fotoelectrónica de rayos X (XPS). Las áreas específicas estuvieron dentro de un rango de 266 y 493 m²/g relacionadas por el método de síntesis y la velocidad de calentamiento y tipo de precursor de Co, mientras que el análisis por DRX se comprobó la presencia de Co6Mo6C2 para carburos obtenido por el método carbotérmico con hidrógeno independientemente de estas variables. XPS mostró tres tipos de señales de molibdeno asignables a Moδ+ (0≤δ≤2), Mo4+ y Mo6+, y uno de Co2+ cuya abundancia estuvo influenciada por el método de síntesis y el tipo de precursor de Co. Por otro lado, XPS reveló que los carburos obtenidos a partir de precursores de sulfato de Co retienen azufre sobre su superficie como S2- y SO4(2-). Los ensayos de HDS de tiofeno mostraron que carburos obtenidos por precursores de sulfato de Co a 1K/min y el método carbotérmico con H2 fueron los de mayor actividad que los obtenidos por el método convencional cuando se activó con CS2/H2 o H2S/H2. This work studied the Effect of the presulfiding agent, type of precursor (sulfate vs. nitrate of promoter), synthesis method (conventional vs. carbothermal carbiding) and heating rate in the hydrodesulfurization of thiophene over activated carbon supported cobalt-molybdenum carbides. The synthesis was carried out using the methods conventional (CH4/H2 (1:4)) and carbothermal with H2 at 973 K and 1 or 5 K/min. The carbided phases were characterized by surface area (B.E.T), X-ray Diffraction (XRD) and X-ray photoelectron spectroscopy (XPS). The surface areas were within a rank of 266 and 493m²/g, whereas the XRD analysis verified the presence of Co6Mo6C2 for carbides obtained by carbothermal method independently of these variables. The XPS showed the presence on the surface of: Moδ+, Mo4+ and Mo6+, and Co2+ whose abundance was influenced by the synthesis method and type of precursor. On the order hand, XPS revealed that the carbides obtained by sulfate precursor retained sulfur on the surface as S2- and SO4(2-). Tests of thiophene HDS showed that carbides obtained by the carbothermal method had higher activity than those obtained by the conventional method when it was activated with CS2/H2 and inversely when used H2S/H2.
- Published
- 2014
9. NATURE OF THE ACTIVE PHASE IN HYDRODESULFURIZATION: MOLYBDENUM CARBIDE SUPPORTED ON ACTIVATED CARBON
- Author
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Puello-Polo, Esneyder, Ayala G, Mónica, and Brito, Joaquín L
- Subjects
Hydrodesulfurization ,Catalytic hydrotreating ,Presulfiding agent ,Carburo de molibdeno ,Método de síntesis ,Hidrodesulfuración ,Agente pressulfurizante ,Agente presulfurante ,Método de síntese ,Hidrotratamento catalítico ,Molybdenum carbide ,Hidrotratamiento catalítico ,Carbonetode molibdênio ,Hidrodessulfurização ,Synthesis method - Abstract
This paper studies the effect of the presulfiding agent and the synthesis method on the catalytic activity of thiophene hydrodesulfurization (HDS), using activated carbon supported molybdenum carbides. The catalytic precursor was prepared by co-impregnation of the support with the ammonium heptamolybdate solution. The conventional carbiding consists of a temperature-programmed treatment under a CH4/H2 atmosphere at 1073 K (MC), while the carbothermal method employs pure H2 at 973 K (MCH). The passivated carbides were characterized by X-ray Diffraction (XRD), surface area calculated by the Brunauer–Emmett–Teller multipoint method (BET) and X-ray Photoelectron Spectroscopy (XPS). XRD confirmed the presence of β-Mo2C for both methods of synthesis, while specific area were in the order of 400 m²/g. XPS showed the presence at the surface of Moδ+ (0 ≤ δ ≤ 2), Mo4+ and Mo6+, whose abundance was influenced by used synthesis method with greater proportion of high oxidation states in MCH. Prior to catalytic testing, the passivated carbides were presulfided in situ. HDS tests showed that regardless of the presulfiding agent (H2S o CS2), the carbides obtained by MCH had higher activity than those obtained using the conventional method. The β-Mo2C presulfiding suggests that the carbides with sulfided surfaces or carbo-sulfide mixtures could be the active phase in HDS. En este trabajo se estudió el efecto del método de síntesis y del agente presulfurante en la actividad catalítica de hidrodesulfuración (HDS) de tiofeno utilizando carburos de molibdeno soportados sobre carbón activado. El precursor catalítico fue preparado por co-impregnación del soporte con la solución de heptamolibdato de amonio. La síntesis consiste de un tratamiento a temperatura programada utilizando los Métodos Carbotérmico con H2 (MCH) y Convencional (MC) bajo una atmosfera de CH4/H2 a 973 y 1073 K, respectivamente. Los carburos pasivados se caracterizaron por difracción de rayos X (DRX), área superficial calculada por el método multipunto Brunauer-Emmett-Teller (BET) y espectroscopía fotoelectrónica de rayos X (XPS). Por DRX se comprobó la presencia de β-Mo2C para ambos métodos de síntesis, mientras que las áreas específicas estuvieron en el orden de los 400 m2/g. XPS mostró tres tipos de señales de molibdeno asignables α Moδ+ (0 ≤ δ ≤ 2), Mo4+ y Mo6+ cuya abundancia estuvo influenciada por el método de síntesis con mayor proporción de altos estados de oxidación en el MCH. Antes de los ensayos catalíticos los carburos pasivados fueron presulfurados in situ. Los ensayos de HDS evidenciaron que indistintamente del agente presulfurante (H2S o CS2), los carburos obtenidos por el MCH fueron los de mayor actividad que los sólidos obtenidos por el método convencional. Después del proceso de presulfuración los β-Mo2C fueron modificados, sugiriendo que los carburos con superficies sulfuradas o mezclas de carbosulfuros podría ser la fase activa en HDS. Neste trabalho foi estudado o efeito do método de síntese e do agente pressulfurizante na atividade catalítica de hidrodessulfurização (HDS) de tiofeno utilizando carbonetos de molibdênio suportados sobre carvão ativado. O precursor catalítico foi preparado por co-impregnação do suporte com a solução de heptamolibdato de amônio. A síntese consiste de um tratamento a temperatura programada utilizando os Métodos Carbotérmico com H2 (MCH) e Convencional (MC) sob uma atmosfera de CH4/H2 a 973 e 1073 K, respectivamente. Os carbonetos passivados foram caracterizados por difração de raios X (DRX), área superficial calculada pelo método multiponto Brunauer–Emmett–Teller (BET) e espectroscopia foto eletrônica de raios X (XPS). Por DRX foi comprovada a presença de β-Mo2C para ambos os métodos de síntese, enquanto que as áreas específicas estiveram na ordem dos 400 m2/g. XPS mostrou três tipos de sinais de molibdênio atribuíveis a Moδ+ (0 ≤ δ ≤ 2), Mo4+ e Mo6+ cuja abundância esteve influenciada pelo método de síntese com maior proporção de altos estados de oxidação no MCH. Antes dos ensaios catalíticos os carbonetos passivados foram pressulfurizados in situ. Os ensaios de HDS evidenciaram que indistintamente do agente pressulfurizante (H2S o CS2), os carbonetos obtidos pelo MCH foram os de maior atividade que os sólidos obtidos pelo método convencional. Depois do processo de pressulfurização os β-Mo2C foram modificados, sugerindo que os carbonetos com superfícies sulfuradas ou misturadas de carbosulfetos poderia ser a fase ativa em HDS.
- Published
- 2014
10. One-pot synthesis of Nb-modified Al2O3 support for NiMo hydrodesulfurization catalysts.
- Author
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Puello-Polo, Esneyder, Marquez, Edgar, and Brito, J. L.
- Abstract
The effect of Nb as a support modifier on the NiMo
6 /Al2 O3 -Nb2 O5 (x) (x = 0, 1, 4, and 8 wt% Nb) catalysts was studied. The supports were prepared by one-pot coprecipitation from soluble precursors. The XRF analysis of the catalysts showed that the contents of Mo and Ni increased slightly with the presence of Nb. Micropore area and pore volume augmented importantly with Nb content, resulting in pore diameters between 5.3 and 9.3 nm. XPS analysis showed that the presence of Nb decreases the active metal-support interaction, improving the Mo and Ni sulfidation degree. The Raman spectra of sulfided catalysts suggested an increase in the number of layers of MoS2 in the presence of Nb. Generally, the thiophene HDS activity at normal pressure of sulfided NiMo6 /Al2 O3 -Nb2 O5 (8) was greater than that of the sulfided catalysts with x = 0, 1, and 4 wt% Nb, which can be attributed to the Nb promotion that would have an effect on the type of active site (Brønsted or Lewis acidic sites), since the number of sites by CO chemisorption for sulfided NiMo6 /Al2 O3 -Nb2 O5 (x) did not show correlation with the catalytic activity. The high-pressure HDS activity of dibenzothiophene was also greater in the presence of Nb, and the hydrogenation route was preferred for the Nb-promoted solid, while the unpromoted one showed a larger yield of direct desulfurization products. The niobium-containing catalyst presented the best catalytic activity.Niobium promotion influenced the type of active site.The presence of Nb improves the sulfidation degree of Mo and Ni.Nb increases the number of Lewis acid sites related to HDS activity. [ABSTRACT FROM AUTHOR]- Published
- 2018
- Full Text
- View/download PDF
11. Effect of the structural modification by carbiding of alumina supported Anderson-type (NH4)4[NiMo6 − xWxO24H6]·5H2O on hydrodesulfurization, hydrodechlorination and selective oxidation.
- Author
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Puello-Polo, Esneyder, Diaz, Yraida, and Brito, Joaquín L.
- Subjects
- *
ANDERSON model , *DESULFURIZATION , *HYDRODECHLORINATION , *ALUMINUM oxidation , *DIBENZOTHIOPHENE - Abstract
The γ-Al 2 O 3 -supported Anderson-type complexes (NH 4 ) 4 [NiMo 6 − x W x O 24 H 6 ]·5H 2 O (x = 0, 3 or 6) were carburized with CH 4 /H 2 (1:4) mixture (denoted by NiMo 6 − x W x -C/Al). These solid compounds have been tested in a continuous flow, fixed bed reactor for thiophene hydrodesulfurization and polychlorinated biphenyls hydrodechlorination, and in (semi-) batch reactor for dibenzothiophene selective oxidation. The specific surface area and pore volume of NiMo 6 -C/Al were greater than those of NiW 6 -C/Al and NiMo 3 W 3 -C/Al. XRD results evidenced a bulk structure typical of Mo 2 C, W 2 C, WC and NiC. FT-IR verified the absence of bands corresponding to metal oxides. Generally, the catalytic activity toward a given reaction product of NiMo 6 -C/Al was greater than those of NiW 6 -C/Al and NiMo 3 W 3 -C/Al due either to its better textural properties or to a more complete transformation of the metal phases into active ones. [ABSTRACT FROM AUTHOR]
- Published
- 2017
- Full Text
- View/download PDF
12. Efecto de la modificación del soporte con níquel y la promoción con cobre en la reacción competitiva de Hidrosulfuración de Dibenzotiofeno e Hidrodesnitrogenación de Carbazol utilizando catalizadores CuMo-Ni/γ-Al2 O3.
- Author
-
Montaño Herazo, Ana, Navarro Barraza, Félix, and Puello-Polo, Esneyder
- Subjects
- *
X-ray fluorescence , *COPPER , *SURFACE area , *DESULFURIZATION , *DIBENZOTHIOPHENE - Abstract
The effect of modifying the support with Ni and promoting with Cu was evaluated in the competitive reaction of dibenzothiophene (DBT) hydrodesulfurization and carbazole hydrodenitrogenation using NiMo/γ-Al2 O3 and CuNiMo/γ-Al2 O3 catalysts. The catalysts were characterized using X-ray fluorescence (XRF), BET specific surface area, FT-IR and determination of acidic sites by titration with n-butylamine. XRF analysis showed a coincidence between nominal and experimental values with Mo/Cu= 6 and Cu/(Cu+Ni)= 0.65. The specific surface areas were ranged from 152 to 207 m² /g with pore diameters between 5.3 and 5.5 nm (mesopores). FT-IR exhibited characteristic bands of terminal and bridging Mo-O bonds associated with the Anderson-type structure, as well as Cu-O bond vibrations. CuNiMo/γ-Al2 O3 presented more acidic sites than NiMo/γ-Al2 O3 (7.1 vs. 6.48 µmol/m² ). Regardless of the catalyst, the catalytic evaluation showed a fit to the pseudo-first-order model of the Langmuir-Hinshelwood equation, with high conversion towards HDS instead of HDN, resulting in a carbazole HDN conversion below 4%. [ABSTRACT FROM AUTHOR]
- Published
- 2023
- Full Text
- View/download PDF
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