2022 4th International Conference on Applied Chemistry and Industrial Catalysis(ACIC 2022)
Keynote Speakers

——Keynote Speeches 1——

姜克隽  研究员  国家发展与改革委员会能源研究所   

Jiang Kejun  Researcher  Energy Research Institute, NDRC

Research focus: Energy System Analysis

3.pngKejun Jiang’s research focus is energy, climate change mitigation and air pollution prevention policy assessment by using IPAC modeling, to support national five year plans, and long-term planning. He began his research in ERI from 1990, and led the development of Integrated Policy Assessment Model for China(IPAC). IPAC modeling team is now a leading research team on China’s 2050 energy transition studies by providing benchmark research results. Major research focus includes energy and emission scenarios, energy policy, energy system,. energy market analysis, and climate change, local environment policies and international negotiation. He also was authors of IPCC for Special Report on Emission Scenario from 1997, and Working Group III Third Assessment Report, leader author for IPCC WGIII AR4 Chapter 3, and leader author for GEO-4 Chapter 2, CLA in WGIII of IPCC AR5, LA for IPCC AR5 Synthesis Report, CLA of IPCC Special Report on 1.5℃ Warning, Vice Co-Chair of GEO6. From 2010, he is author for UNEP Emission Gaps. Now he is lead author of IPCC AR6 WGIII. He also joined international research collaboration projects such as EMF, FP6, FP7 and H2020 research projects. He is member of Scientific Panel of UNEP CCAC, and Scientific Committee of IAMC. He got his Ph.D in Social Engineering Department of Tokyo Institute of Technology.

——Keynote Speeches 2——

魏贤勇  教授/博导/“高层次人才”学术带头人


Xianyong Wei Professor/PhD advisor/ Leading expert of “High-level Talent Plan” of Xinjiang University

Xinjiang University/China University of Mining and Technology

Research focus: efficient utilization of heavy carbon resources


Prof. Wei has chaired two key projects and four general projects funded National Natural Science Foundation of China, two projects of the national “973 Plan” and the national “863 Plan”. He is now chairing another two key projects of NSFC.

Prof. Wei has published over 400 papers on SCI-indexed journals. He is also an owner of one international patent, 20 national patents and two utility models. His works has been cited above 8000 times.

Prof. Wei is a leading expert of professional coal processing technologies in the national “Thousand Talents Program”, an excellent postgraduate supervisor of Jiangsu province, a high-level talent of “High-caliber Talent Training Program” of Jiangsu province, an outstanding talent for innovative coal industry technologies, an excellent chemical professional of China, and an winner of the Lu Jiaxi Excellent Student Supervisor Award. Prof. Wei is a government-funded researcher and has made it to the list of highly-cited scholars in China from 2014 to 2018. 


——Keynote Speakers of Past Sessions——

水恒福  教授/博导/现任安徽工业大学党委常委、副校长

Hengfu Shui Professor/ PhD supervisor/ Vice President & Standing Committee Member of CPC Committee of Anhui University of Technology.

Research focus: Coal clean conversion and utilization



Study on Catalytic Thermal Dissolution of lignite and Hydro-liquefaction of Its Thermal Dissolution Soluble Fraction For Potential Jet Fuel

Keyworlds: Xilinguole lignite; Catalytic thermal dissolution; Hydrogenation liquefaction; Catalyst; Jet fuel


The effects of different catalysts on the catalytic thermal dissolution (TD) properties of Xilinguole (XLGL) lignite were studied. The structure of thermal dissolution soluble fractions (TDSFs) was analyzed and characterized. The results suggest that the catalytic activity of the four catalysts used is in order of BF3/SBA-15FeS+SSO42-/ZrO2=Fe2O3. At 360, the TD yield of BF3/SBA-15 was the highest, and the TD yields of CMNO, 1-MN+10%CH3OH and 1-MN were 39.5%, 59.6% and 28.6%, which were higher of 17.1%, 17.4% and 12.7% than those without catalyst respectively. The results suggest that the catalyst can improve TD activity of lignite. 

The TDSF obtained with 1-MN+10%CH3OH and BF3/SBA-15 catalytic TD at 360gave the highest yield of liquefied oil (CHS) as 33.1% after catalytic hydrogenation under Ni-Mo-S/Al2O3 with cyclohexane as solvent at 360. This is because the aromatic condensation degree of this TDSF is lower and the aliphatic hydrocarbon content is higher, which is beneficial for the hydro-liquefaction of TDSF. CHSs obtained by liquefaction of TDSF from the catalytic TD of lignite in 1-MN were dominated by 1~2 ring aromatic compounds. The content of saturated cycloalkanes in CHS obtained by liquefaction of TDSF at 320was 6.12%, which was slightly higher than that of 5.07% in CHS obtained by liquefaction of TDSF at 360.

The hydroliquefaction activity of three catalysts used were in the order Ni-Mo-S/Al2O3>Ni/ZSM-5>Cu-Ni/Al2O3. In the presence of catalyst Ni-Mo-S/Al2O3 and tetrahydronaphthalene as hydrogen donor solvent, the yield of CHS increased gradually with the increase of the liquefaction temperature from 280 to 400, and the maximum was 60.4% obtained at 400. The content of saturated cycloalkanes in CHS decreased with the increase of liquefaction temperature, and the maximal content of saturated cycloalkanes in CHS was 13.5% obtained at 280, suggesting that low temperature hydrogenation is favorable to saturate hydrogenation of aromatics. Therefore the hydro-liquefaction of TDSF at low temperature can be used to produce the potential jet fuel.