PENGARUH AGEN GASIFIKASI BATUBARA TERHADAP PRODUK GAS YANG DIHASILKAN OLEH BATUBARA PERINGKAT RENDAH

Agus Triantoro, Adip Mustofa, Riswan Riswan

Abstract


The development of coal gasification has several disadvantages including high reaction temperature and big energy consumption, difficult purification of the gaseous products, and stringent requirements of the process equipment. It has also been pointed out to cause serious environmental pollution. In this study, the experiment was conducted by flowing nitrogen, oxygen, and , into the gasification equipment. The gasification reactor was heated to 600 oC, 700 oC and 800 oC, where dry coal had been initially fed into before the gasification process began. The flow rates of pyrolysis products were then measured and a sample was taken for further analysis by using a gas chromatograph. The analysis identified the products composition that was CO, CO2, H2, CH4, C2H4 and C2H6. The composition of synthesis gas was observed to depend on the gasification agent used. it can be summarized that there is a good correlation between gasification agent and coal used, with the quality and quantity of synthesis gas produced.


Keywords


coal gasification, synthesis gas, gasification agent

Full Text:

PDF

References


S. Suprapto, Nurhadi, Production of synthesis gas from Indonesian low rank coals using fluidized bed gasification reactor, Indonesian mining journal, 10, 10 (2007)

S. Suprapto, T. Rochman, and Y. Basyuni, Gasifikasi batubara peringkat rendah dengan pereaksi udara, Prosiding Seminar Ilmiah Hasil Penelitian dan Pengembangan Bidang Fisika Terapan, 154, Bandung, Indonesian (1995)

Caltex, The potential of coal bed methane in Indonesia, PT Caltex Pacific Indonesia, Jakarta (1998)

Nowacki, P. (ed), Coal Gasification Process. Noyes Data Corporation, New Jersey, 1981.

Rajvanshi, A.K., Biomass Gasification, Nimbkar Agricultural Institute, Maharasthra, India, 1986.

Gavalas, G.R., Coal Pyrolysis, Elsevier Scientific Publishing Company, Netherland, 1982.

Solomon, P.R., Serio, M.A., dan Suuberg, E.M., Coal Pyrolysis: Experiment, Kinetic Rates and Mechanisms. Prog. Energy Combust. Sci., (1992), 18, 133 - 220.

Solomon, P.R., Hamblen, D.G., Carangelo, R.M., Serio, M.A., General Model of Coal Devolatilization, Energy and Fuel (1987), 2, 405-422.

Cristopher Highman, Maarten Van Derburgt, Gasification, Elsevier, USA, 2008.

NEDO, 2008. Clean Coal Overview: Modeling And Simulation Technologies For Coal Gasification. Modul pelatihan Clean Coal Technology transfer project, NEDO, 1— 20 Desember 2008.

Agus Triantoro,Proses Gasifikasi Batubara Peringkat Rendah Dengan Menggunakan Katalis Nikel dan K2CO3, Thesis, Institut Teknologi Bandung, (2013).

Davies, C., Calculation in Furnace Technologi, Pergamon Press Ltd., Headington Hll Hall, Oxford, London, 1970.




DOI: http://dx.doi.org/10.20527/infotek.v14i2.304

DOI (PDF): http://dx.doi.org/10.20527/infotek.v14i2.304.g245

Article Metrics

Abstract view : 499 times
PDF - 409 times

Refbacks

  • There are currently no refbacks.


Copyright (c) 2016 INFO-TEKNIK

Creative Commons License
This work is licensed under a�Creative Commons Attribution 4.0 International License.�

joomla
statistics View My Stats

Indexed By:

Citation :

SINTA 6 mulai Vol. 19 No. 2 2018 (SK NO. 164/E/KPT/2021)

GOOGLE SCHOLAR : Sitasi = 78, H-index = 5, i10-index = 2

IPI :� Artikel = 100

IOS 3969 : Artikel = 239