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Li D, Wang X, Hou X, Sun S, Chen X, Zhang H. Synthesis of hydrophilic glyceryl monocaffeate with economical catalyst cation-exchange resin Amberlyst-35. JOURNAL OF THE SCIENCE OF FOOD AND AGRICULTURE 2023; 103:4676-4684. [PMID: 36905092 DOI: 10.1002/jsfa.12547] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/17/2022] [Revised: 02/03/2023] [Accepted: 03/10/2023] [Indexed: 06/06/2023]
Abstract
BACKGROUND Caffeic acid (CA) has anti-oxidation and anti-inflammatory. However, the poor hydrophilicity of CA limits its biological activities. In this work, hydrophilic glyceryl monocaffeate (GMC) was synthesized by esterification using different caffeoyl donors (deep eutectic solvent and solid CA). Cation-exchange resins were used as the catalysts. The effects of reaction conditions were also investigated. RESULTS The mass transfer limitation of esterification was eliminated using deep eutectic solvent. Compared with the previous catalysts (immobilized lipase Novozym 435), an economic cation-exchange resin, Amberlyst-35 (A-35), showed good catalytic performance for GMC preparation. The activation energies of GMC synthesis and CA conversion were 43.71 kJ mol-1 and 43.07 kJ mol-1 , respectively. The optimal reaction conditions were a temperature reaction of 90 °C, catalyst load of 7%, glycerol/CA molar ratio of 5:1 (mol mol-1 ), and reaction time of 24 h, which resulted in a maximum GMC yield and CA conversion of 69.75 ± 1.03% and 82.23 ± 2.02%, respectively. CONCLUSION The results of the work showed a promising alternative for the synthesis of GMC. © 2023 Society of Chemical Industry.
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Affiliation(s)
- Dami Li
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
| | - Xinying Wang
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
| | - Xuebei Hou
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
| | - Shangde Sun
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
| | - Xiaowei Chen
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
| | - Hao Zhang
- School of Food Science and Engineering, Henan University of Technology, Zhengzhou, PR China
- Henan Engineering Research Center of Oilseed Deep Processing, Henan University of Technology, Zhengzhou, PR China
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Mercado DF, Ballesteros-Rueda LM, Lizarazo-Gómez CC, Núñez-Rodríguez BE, Arenas-Calderón E, Baldovino‑Medrano VG. Synthesis and use of functionalized SiO2 nanoparticles for formulating heavy oil macroemulsions. Chem Eng Sci 2022. [DOI: 10.1016/j.ces.2022.117531] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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Sandoval-Bohórquez VS, Morales-Valencia EM, Castillo-Araiza CO, Ballesteros-Rueda LM, Baldovino-Medrano VG. Kinetic Assessment of the Dry Reforming of Methane over a Ni–La 2O 3 Catalyst. ACS Catal 2021. [DOI: 10.1021/acscatal.1c02631] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Víctor Stivenson Sandoval-Bohórquez
- Centro de Investigaciones en Catálisis (@CICAT UIS), Parque Tecnológico Guatiguará (PTG), Km. 2 vía El Refugio, Universidad Industrial de Santander, Piedecuesta (Santander) 681011, Colombia
| | - Edgar M. Morales-Valencia
- Centro de Investigaciones en Catálisis (@CICAT UIS), Parque Tecnológico Guatiguará (PTG), Km. 2 vía El Refugio, Universidad Industrial de Santander, Piedecuesta (Santander) 681011, Colombia
| | - Carlos O. Castillo-Araiza
- Laboratorio de Ingeniería de Reactores Aplicada a Sistemas Químicos y Biológicos, Departamento de Ingeniería de Procesos e Hidráulica, Universidad Autónoma Metropolitana—Iztapalapa, 09340 CDMX, Mexico
| | - Luz M. Ballesteros-Rueda
- Centro de Investigaciones en Catálisis (@CICAT UIS), Parque Tecnológico Guatiguará (PTG), Km. 2 vía El Refugio, Universidad Industrial de Santander, Piedecuesta (Santander) 681011, Colombia
| | - Víctor G. Baldovino-Medrano
- Centro de Investigaciones en Catálisis (@CICAT UIS), Parque Tecnológico Guatiguará (PTG), Km. 2 vía El Refugio, Universidad Industrial de Santander, Piedecuesta (Santander) 681011, Colombia
- Laboratorio de Ciencia de Superficies (#SurfLab-UIS), Parque Tecnológico Guatiguará (PTG), Km. 2 vía El Refugio, Universidad Industrial de Santander, Piedecuesta (Santander) 681011, Colombia
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Tatiana García‐Sánchez J, Darío Mora‐Vergara I, Molina‐Velasco DR, Antonio Henao‐Martínez J, Gabriel Baldovino‐Medrano V. Key Factors During the Milling Stage of the Seed‐assisted and Solvent‐free Synthesis of MFI and Catalytic Behavior in the Alkylation of Phenol with Tert‐butyl Alcohol. ChemCatChem 2021. [DOI: 10.1002/cctc.202100479] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
Affiliation(s)
- Julieth Tatiana García‐Sánchez
- Centro de Investigaciones en Catálisis (CICAT) Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
| | - Iván Darío Mora‐Vergara
- Centro de Investigaciones en Catálisis (CICAT) Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
| | - Daniel Ricardo Molina‐Velasco
- Laboratorio de Resonancia Magnética Nuclear Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
| | - José Antonio Henao‐Martínez
- Laboratorio de Rayos-X Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
| | - Víctor Gabriel Baldovino‐Medrano
- Centro de Investigaciones en Catálisis (CICAT) Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
- Laboratorio de Ciencia de Superficies (SurfLab) Universidad Industrial de Santander Parque Tecnológico Guatiguará km 2 vía El Refugio Universidad Industrial de Santander Piedecuesta (Santander) 681011 Colombia
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Nda-Umar UI, Ramli I, Muhamad EN, Azri N, Taufiq-Yap YH. Optimization and Characterization of Mesoporous Sulfonated Carbon Catalyst and Its Application in Modeling and Optimization of Acetin Production. Molecules 2020; 25:molecules25225221. [PMID: 33182532 PMCID: PMC7697787 DOI: 10.3390/molecules25225221] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 09/24/2020] [Revised: 10/30/2020] [Accepted: 10/31/2020] [Indexed: 11/16/2022] Open
Abstract
In this study, an optimized mesoporous sulfonated carbon (OMSC) catalyst derived from palm kernel shell biomass was developed using template carbonization and subsequent sulfonation under different temperatures and time conditions. The OMSC catalyst was characterized using acid-base titration, elemental analysis, XRD, Raman, FTIR, XPS, TPD-NH3, TGA-DTA, SEM, and N2 adsorption–desorption analysis to reveal its properties. Results proved that the OMSC catalyst is mesoporous and amorphous in structure with improved textural, acidic, and thermal properties. Both FTIR and XPS confirmed the presence of -SO3H, -OH, and -COOH functional groups on the surface of the catalyst. The OMSC catalyst was found to be efficient in catalyzing glycerol conversion to acetin via an acetylation reaction with acetic acid within a short period of 3 h. Response surface methodology (RSM), based on a two-level, three-factor, face-centered central composite design, was used to optimize the reaction conditions. The results showed that the optimized temperature, glycerol-to-acetic acid mole ratio, and catalyst load were 126 °C, 1:10.4, and 0.45 g, respectively. Under these optimum conditions, 97% glycerol conversion (GC) and selectivities of 4.9, 27.8, and 66.5% monoacetin (MA), diacetin (DA), and triacetin (TA), respectively, were achieved and found to be close to the predicted values. Statistical analysis showed that the regression model, as well as the model terms, were significant with the predicted R2 in reasonable agreement with the adjusted R2 (<0.2). The OMSC catalyst maintained excellent performance in GC for the five reaction cycles. The selectivity to TA, the most valuable product, was not stable until the fourth cycle, attributable to the leaching of the acid sites.
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Affiliation(s)
- Usman Idris Nda-Umar
- Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Department of Chemical Sciences, Federal Polytechnic, P.M.B. 55 Bida, Niger State, Nigeria
| | - Irmawati Ramli
- Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Catalysis Science and Technology Research Centre (PutraCat), Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Laboratory of Processing and Product Development, Institute of Plantation Studies, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
| | - Ernee Noryana Muhamad
- Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Catalysis Science and Technology Research Centre (PutraCat), Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
| | - Norsahida Azri
- Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Catalysis Science and Technology Research Centre (PutraCat), Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
| | - Yun Hin Taufiq-Yap
- Department of Chemistry, Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
- Catalysis Science and Technology Research Centre (PutraCat), Faculty of Science, Universiti Putra Malaysia, Serdang 43400 UPM, Selangor, Malaysia
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Abstract
Crude glycerol is the main by-product of many renewable diesel production platforms. However, the process of refining glycerol from this crude by-product stream is very expensive, and thus does not currently compete with alternative processes. The acetylation of glycerol provides an intriguing strategy to recover value-added products that are employable as fuel additives. In this work, the conversion of glycerol to acetyl derivatives was facilitated by a heterogeneous catalyst generated from the thermal hydrolysis of biosolids obtained from a municipal wastewater treatment facility. The reaction was studied using several conditions including temperature, catalyst loading, acetic acid:glycerol molar ratio, and reaction time. The data demonstrate the potential for using two distinct by-product streams to generate fuel additives that can help improve the process economics of renewable diesel production.
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