Shailesh Pathak

ORCID: 0000-0002-3781-6041
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About
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Research Areas
  • Chemical Looping and Thermochemical Processes
  • Catalysis and Hydrodesulfurization Studies
  • Industrial Gas Emission Control
  • Catalytic Processes in Materials Science
  • Catalysis for Biomass Conversion
  • Carbon Dioxide Capture Technologies
  • Catalysts for Methane Reforming
  • Biofuel production and bioconversion
  • Ionic liquids properties and applications
  • Thermochemical Biomass Conversion Processes
  • Catalysis and Oxidation Reactions
  • Agricultural and Food Sciences
  • Carbon dioxide utilization in catalysis
  • Water Governance and Infrastructure
  • Indian Economic and Social Development
  • CO2 Reduction Techniques and Catalysts
  • Architecture and Computational Design
  • Thermodynamic properties of mixtures
  • Fiber-reinforced polymer composites
  • Optical Systems and Laser Technology
  • Thermal and Kinetic Analysis
  • Agricultural risk and resilience
  • Glass properties and applications
  • Linguistics and Cultural Studies
  • Bee Products Chemical Analysis

University of California, Santa Barbara
2024

Indian Institute of Technology Delhi
2019-2023

University of Louisville
2023

Indian Institute of Technology Roorkee
2015-2019

Raja Ramanna Centre for Advanced Technology
2013

Methane pyrolysis at 950 °C and 1 atm was investigated on iron containing catalysts derived from a magnetite (Fe3O4) ore in semibatch fluidized bed reactor. The particulates (∼10–50 μm) were observed to undergo reduction fragmentation approximately 100 nm iron–iron carbide 100% methane as the reactor heated high gas flow rates. After prereduction, rate decreased weight hourly space velocity (WHSV) of 3.5 h–1, activity increase maximum conversion 90% (turnover frequency ∼ 0.3 s–1). At...

10.1021/acs.energyfuels.4c01484 article EN cc-by-nc-nd Energy & Fuels 2024-07-09

In present work, experiments for gas-phase acetic acid hydrogenation were conducted over SiO2–Al2O3 supported platinum–tin (Pt–Sn) catalysts. These experimental data used to model the kinetics of reaction based on two-site Langmuir–Hinshelwood–Hougen–Watson kinetic model. Kinetic parameters determined, and excellent matches found between calculated results data. order get a better insight into effect process conversion selectivity spontaneity reaction, thermodynamic was developed. Based...

10.1021/acs.energyfuels.9b04070 article EN Energy & Fuels 2020-02-13

Myrica esculenta is a plant of significant ethnobotanical and medicinal interest. This review synthesizes the current knowledge regarding its traditional uses, phytochemical composition, therapeutic potential. Historically, has been employed in indigenous medicine for various ailments, including digestive disorders, respiratory issues, skin diseases. The plant’s benefits are largely attributed to diverse array bioactive compounds, such as flavonoids, phenolic acids, essential oils. Recent...

10.21590/jddhs.01.03.07 article EN 2024-09-25

Understanding tailored CO3O4 spinel with Fe3+ doping is challenging due to the surface state characterization of bifunctional catalysts higher cation diversity. Doping secondary metal creates a double structure (a hybrid normal and inverted spinels), enhancing catalytic properties by generating more active oxygen vacancies. Cobalt-rich (FeCo2O4) iron-rich (CoFe2O4) are synthesized using wet impregnation method, supported over oxidized SiC (pretreated SiC) for improved metal-support...

10.26434/chemrxiv-2023-n273j preprint EN cc-by 2023-07-28

Understanding the characterization of a tailored Co3O4 spinel with Fe3+ doping poses challenge due to surface state complexity in bifunctional catalysts higher cation diversity. Doping secondary metal results double structure (a hybrid normal and inverted spinels). This enhances catalytic properties by generating more active oxygen vacancies. The cobalt-rich (FeCo2O4) iron-rich (CoFe2O4) are synthesized using wet impregnation method, supported over oxidized SiC (SiC-Pretrt) for an improved...

10.1021/acs.jpclett.3c02119 article EN The Journal of Physical Chemistry Letters 2023-12-26

The comprehensive kinetics of simultaneous CO consumption in a Fischer–Tropsch and water–gas shift reaction network was systematically investigated over supported FeCo 2 O 4 spinel catalyst.

10.1039/d2se01282k article EN Sustainable Energy & Fuels 2022-12-03
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