A5028021740- Thermochemical Biomass Conversion Processes
- Catalysts for Methane Reforming
- Catalytic Processes in Materials Science
- Extraction and Separation Processes
- Granular flow and fluidized beds
- Recycling and Waste Management Techniques
- Advancements in Battery Materials
- Cyclone Separators and Fluid Dynamics
- Catalysis and Hydrodesulfurization Studies
- Minerals Flotation and Separation Techniques
- Iron and Steelmaking Processes
- Fluid Dynamics and Mixing
- Coal and Its By-products
- Combustion and flame dynamics
- Chemical Looping and Thermochemical Processes
- Fire dynamics and safety research
- Petroleum Processing and Analysis
- Neurological Disorders and Treatments
- Fluid Dynamics and Heat Transfer
- Air Quality and Health Impacts
- Ionic liquids properties and applications
- Coal Properties and Utilization
- Mineral Processing and Grinding
- Regional Economic and Spatial Analysis
- Urban Transport and Accessibility
Ningbo University of Technology
2022-2024
Ningbo University
2024
Tianjin University
2023-2024
East China University of Science and Technology
2020-2024
Xi'an Jiaotong University
2024
Institute of Coal Chemistry
2017-2019
University of Chinese Academy of Sciences
2017-2018
Northwest University
2015
The catalytic hydrogasification of char to synthetic natural gas was carried out in a pressurized fixed-bed reactor over Cu–Ni–Ca composite catalysts. effect the Cu–Ni ratio, loading, reaction temperature on methane yield, and formation rate investigated. characterization these catalysts by X-ray diffraction showed that alloy formed with suitable ratio during hydrogasification. Experiment results indicated 1:1 favored for alloy, which presented highest activity. Methane yield...
In this work, a systematic study has been conducted to optimize the process conditions and evaluate kinetic parameters for hydrodesulfurization of coal tar. Experiments were performed in trickle-bed hydrogenation unit at temperatures, hydrogen pressures, liquid hourly space velocities 643–683 K, 9.6–13.6 MPa, 0.3–0.5 h–1, respectively. Hydrogen oil volume ratio was maintained constant 1,200 LN/L all cases. Optimization investigated using Box-Behnken experimental design by response surface...
Download This Paper Open PDF in Browser Add to My Library Share: Permalink Using these links will ensure access this page indefinitely Copy URL DOI