Rong Xing

ORCID: 0000-0002-9452-8855
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About
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Research Areas
  • Mesoporous Materials and Catalysis
  • Advanced battery technologies research
  • Crystallization and Solubility Studies
  • Advanced Photocatalysis Techniques
  • Chemical and Physical Properties in Aqueous Solutions
  • Advancements in Battery Materials
  • Catalytic Processes in Materials Science
  • Analytical Chemistry and Chromatography
  • Covalent Organic Framework Applications
  • Catalysis and Hydrodesulfurization Studies
  • Electrocatalysts for Energy Conversion
  • Supercapacitor Materials and Fabrication
  • Advanced Battery Materials and Technologies
  • Chemical Synthesis and Reactions
  • Catalysis and Oxidation Reactions
  • Catalysis for Biomass Conversion
  • Nanomaterials for catalytic reactions
  • Fuel Cells and Related Materials
  • Advanced Battery Technologies Research
  • Zeolite Catalysis and Synthesis
  • Oxidative Organic Chemistry Reactions
  • Conducting polymers and applications
  • Membrane Separation and Gas Transport
  • Advanced biosensing and bioanalysis techniques
  • Copper-based nanomaterials and applications

East China University of Science and Technology
2025

Hunan Agricultural University
2017-2024

Shandong University
2019-2024

Yancheng Teachers University
2015-2024

State Grid Corporation of China (China)
2024

Affiliated Hospital of Chengde Medical College
2024

Shanghai University of Medicine and Health Sciences
2024

Beihang University
2023

Beijing Academy of Artificial Intelligence
2023

Clariant (United States)
2016-2023

In this paper we present a new process to produce furfural and co-products of formic acetic acids from waste aqueous hemicellulose solutions using continuous two zone biphasic reactor. We estimate approach uses 67% 80% less energy than the current industrial processes furfural. An economic analysis indicates that can be produced with at 366 US$ per metric ton which is 25% selling price in U.S. market today. This assumes plant capacity 78 kiloton year furfural, 12 acid 44 (processing 160 hour...

10.1039/c1ee01022k article EN Energy & Environmental Science 2011-01-01

In this paper we report a novel four-step process for the production of jet and diesel fuel range alkanes from hemicellulose extracts derived northeastern hardwood trees. The extract is representative byproduct that could be produced by wood-processing industries such as biomass boilers or pulp mills in U.S. tested study contained mainly xylose oligomers (21.2 g/l after acid hydrolysis) well 0.31 glucose, 0.91 arabinose, 0.2 lactic acid, 2.39 acetic formic other minor products. first step an...

10.1039/c0gc00263a article EN Green Chemistry 2010-01-01

Abstract Novel solid acid catalysts have been prepared from F u d an U niversity (FDU)‐type mesoporous polymers with the Ia and P6mm mesostructures through a carefully controlled sulfonation procedure. Various techniques adopted to characterize throughout their structures, porosity, acidity as well information related sulfonic groups. The group‐functionalized mesopolymers prove be efficient heterogeneous in reactions such liquid‐phase Beckmann rearrangement of cyclohexanone oxime...

10.1002/adfm.200600784 article EN Advanced Functional Materials 2007-08-15

We demonstrate how hemicellulose-derived C5 sugars can be converted into a high-quality petroleum refinery feedstock by four-step catalytic process. The substitute consists of normal, branched and cyclic alkanes up to 31 carbons in length is similar composition feedstocks produced today from crude oil. This process tuned adjust the size liquid alkanes. In first step furfural acid-catalyzed dehydration sugar streams biphasic reactor. second aldol condensation with acetone THF solvent using...

10.1039/c2ee23316a article EN Energy & Environmental Science 2012-11-09

Abstract We have developed a kinetic model for aqueous‐phase production of levulinic acid from glucose using homogeneous catalyst. The proposed shows good fit with experimental data collected in this study batch reactor. was also fitted to steady‐state obtained plug flow reactor (PFR) and continuously stirred tank (CSTR). consists four key steps: (1) dehydration form 5‐hydroxymethylfurfural (HMF); (2) reversion/degradation reactions produce humins (highly polymerized insoluble carbonaceous...

10.1002/cssc.201100717 article EN ChemSusChem 2012-06-13
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