Numerical Simulation of the Methanol Synthesis Process by Using HT-L Pulverized Coal Gasification

Yu Xin Zheng; Zhi Hua Wang; Xue Hong Wu; Yan Li Lv

doi:10.4028/www.scientific.net/AMR.1090.163

Paper Titles

Research on the Relationship between Freshness and Dielectric Spectrum of Postharvest Ling-Wu Long Jujubes
p.136

Optimization of Preparing Technology of Magnetic Carboxymethylchitosan Microspheres Molecular-Imprinted by 6-ethoxydihydrosanguinarine Using Response Surface Methodology
p.142

Simulation of Citronellal Extraction Tower Based on Aspen Plus Software
p.148

Optimization of Experimental Conditions for the Preparation of High Specific Surface Area Bamboo-Based Activated Carbon
p.154

Numerical Simulation of the Methanol Synthesis Process by Using HT-L Pulverized Coal Gasification
p.163

Identification of Solar Cell Temperature Model Using Differential Evolution Algorithm
p.167

Enhanced Absorption of Single Silicon Nanowire with Si₃N₄ Shell for Photovoltaic Applications
p.173

Immobilization of Acidic Ionic Liquid in Silica Gel for Catalytic Oxidative Desulfurization of Fuel Oils(I): Preparation and Charaterization of Catalysts
p.178

Immobilization of Acidic Ionic Liquid on Silica Gel for Catalytic Oxidative Desulfurization of Fuel Oils(II): Desulfurization
p.183

HomeAdvanced Materials ResearchAdvanced Materials Research Vol. 1090Numerical Simulation of the Methanol Synthesis...

Numerical Simulation of the Methanol Synthesis Process by Using HT-L Pulverized Coal Gasification

Abstract:

The numerical simulation of the methanol synthesis process by using HT-L pulverized coal gasification is studied in the work. Pulverized coal gasification are simulated by Aspen Plus industrial systems flower software, and the optimum condition can be gained by calculation. The pulverized coal entrained-flow gasifier adopts the minimization method of Gibbs free energy. Under the given conditions of 1500°C and carbon conversion of 99%, when coal flow volume is 3265.87 kg/h and the ratio of air and coal is 4:1, the content of effective gas is maximal, and also the content of effective gas increased with increasing of the pressure.

You might also be interested in these eBooks

Energy and Materials Research for the Future

View Preview

Info:

Periodical:

Advanced Materials Research (Volume 1090)

Pages:

163-166

DOI:

https://doi.org/10.4028/www.scientific.net/AMR.1090.163

Citation:

Cite this paper

Online since:

February 2015

Authors:

Yu Xin Zheng, Zhi Hua Wang, Xue Hong Wu*, Yan Li Lv

Keywords:

Aspen Plus Industrial Systems Flower Software, Numerical Simulation, Pulverized Coal Gasification

Export:

RIS, BibTeX

Price:

Permissions CCC:

Request Permissions

Permissions PLS:

Request Permissions

Сopyright:

Citation:

* - Corresponding Author

References

[1] Y.Q. Wu, H.G. Li , Chemical Engineering Management 1(2004): 26-27.

Google Scholar

[2] J.S. Lee, S.H. Han,H. G. Kim K.H. Lee , Y.G. Kim, Korean 17(2000)332- 336.

Google Scholar

[3] I.K. Alghurabiea, B.O. Hasanb, B. Jacksona, A. Kosminskia, P.J. Ashmana, Chemical Engineering Research and Design 91(2013) 1614–1624.

Google Scholar

[4] J. Gu, S. Wu, Y. Wu,Y. Li, J. Gao. Energy&Fuels 22(2008) 4029-4033.

Google Scholar

[5] H.Y. Park D.H. Ahn. Chemical Engineering 24(2007)24-30.

Google Scholar

[6] Y. Yun, S.W. Chung, Chemical Engineering 24(2007) 628-632.

Google Scholar

[7] F. Weiland, H. Hedman,M. Marklund, H. Wiinikka, Energy and Fuels 27 (2013) 932–941.

DOI: 10.1021/ef301803s

Google Scholar

[8] F. Weiland, H. Wiinikka, H. Hedman, M. Marklund, R. Gebart, Proceedings: The 4th Nordic Wood Biorefinery Conference, Helsinki, Finland 23–25 October, (2012).

Google Scholar

[9] N. Padban, The 4th Central European Biomass Conference in Graz, Austria (January 15–18, 2014), (2014).

Google Scholar