Shizhe Liu
Shizhe Liu has a total of 31 co-authors. Here are the top co-authors by number of shared publications:
Chunyi Li
3 shared publicationsBin Gao
1 shared publicationBin Hao
Tangshan College
1 shared publicationChaohe Yang
1 shared publicationChenjie Zhu
1 shared publication- Chunyan Tu
Key Laboratory of Coal Science and Technology of Ministry of Education and Shanxi Province, Taiyuan University of Technology, Taiyuan 030024, China
1 shared publication
Latest Publications
- 1 January 2020
- Published by Elsevier in Catalysis Communications
- Vol. 133
La-doped Zr-Beta zeolite as efficient catalyst for reduction of cyclohexanone to cyclohexanol via the MPV process
- 1 January 2020
- Published by Elsevier in Catalysis Communications
- Vol. 133
La-doped Zr-Beta zeolite as efficient catalyst for reduction of cyclohexanone to cyclohexanol via the MPV process
- 1 January 2016
- Published by Elsevier in Journal of Energy Chemistry
- Vol. 25 (1) , 85-92
Effects of Cs-substitution and partial reduction on catalytic performance of Keggin-type phosphomolybdic polyoxometalates for selective oxidation of isobutane
- 1 January 2016
- Published by Elsevier in Journal of Energy Chemistry
- Vol. 25 (1) , 85-92
Effects of Cs-substitution and partial reduction on catalytic performance of Keggin-type phosphomolybdic polyoxometalates for selective oxidation of isobutane
- 1 May 2013
- Published by Elsevier in Journal of Catalysis
- Vol. 301, 93-102
Selective conversion of glycerol to acrolein over supported nickel sulfate catalysts
- 1 May 2013
- Published by Elsevier in Journal of Catalysis
- Vol. 301, 93-102
Selective conversion of glycerol to acrolein over supported nickel sulfate catalysts
- 4 July 2011
- Published by Trans Tech Publications, Ltd. in Advanced Materials Research
- Vol. 284-286, 1358-1361
Preparation of Porous Catalyst Support with Gangue of Bauxite Tailing
Porous catalyst support was prepared using gangue of bauxite tailing which was a solid waste material. It was found that the mass ratio of gangue of bauxite and knar clay was 4: 1. The masses of cellulose and water were individually 1 wt% and 25 wt% of the total mass of gangue of bauxite tailing and knar clay. The pore forming agent M was optimum among the selected pore forming agents. The pore forming agent M didn’t residue in support after sintering so that the support wasn’t polluted. The appropriate addition of the pore forming agent M was 4%, and the catalyst support with the porosity of 41.3% was preparated. The appropriate sintering temperature and holding time were 1250 °C and 2.0 h, respectively. Mullite and quartz were the main mineral phase of the porous catalyst support and the catalyst support have good chemical stability and heat-resisting property.
- 4 July 2011
- Published by Trans Tech Publications, Ltd. in Advanced Materials Research
- Vol. 284-286, 1358-1361
Preparation of Porous Catalyst Support with Gangue of Bauxite Tailing
Porous catalyst support was prepared using gangue of bauxite tailing which was a solid waste material. It was found that the mass ratio of gangue of bauxite and knar clay was 4: 1. The masses of cellulose and water were individually 1 wt% and 25 wt% of the total mass of gangue of bauxite tailing and knar clay. The pore forming agent M was optimum among the selected pore forming agents. The pore forming agent M didn’t residue in support after sintering so that the support wasn’t polluted. The appropriate addition of the pore forming agent M was 4%, and the catalyst support with the porosity of 41.3% was preparated. The appropriate sintering temperature and holding time were 1250 °C and 2.0 h, respectively. Mullite and quartz were the main mineral phase of the porous catalyst support and the catalyst support have good chemical stability and heat-resisting property.