Fungi solubilisation of low rank coal: Performances of stirred tank, fluidised bed and packed bed reactors

2013 ◽  
Vol 106 ◽  
pp. 295-302 ◽  
Author(s):  
Bilainu O. Oboirien ◽  
Tunde V. Ojumu ◽  
Surajudeen O. Obayopo
Author(s):  
Kahar Osman ◽  
Nik Rosli Abdullah ◽  
Nor Fadzilah Othman ◽  
Mohd Norhakem Hamid ◽  
Kamariah Md Isa

Author(s):  
Kamariah Md Isa ◽  
Kahar Osman ◽  
Nik Rosli Abdullah ◽  
Nor Fadzilah Othman ◽  
Mohd Norhakem Hamid

CFD letters ◽  
2020 ◽  
Vol 12 (10) ◽  
pp. 111-127
Author(s):  
Kamariah Md Isa ◽  
Kahar Osman ◽  
Nik Rosli Abdullah ◽  
Nor Fadzilah Othman ◽  
Nurulnatisya Ahmad

Low-Rank Coal (LRC) gasification utilising Fluidised Bed Gasifier (FBG) is more efficient for LRC that has higher reactivity, moisture, tar, volatile, and ash content but lower calorific value compared to other types of coals. This work investigated the application of Computational Fluid Dynamics (CFD) in simulating LRC gasification under different temperatures which is lower (873K), normal (973K) and higher (1073K) temperature atmosphere. Besides that, the effect of LRC type and gasifying agents on the producer gas CO+H2 composition, Lower Heating Value (LHV) and Cold Gas Efficiency (CGE) were also studied using High-rank Coal (HRC) as comparison. The results obtained showed that LRC gasification using oxygen increased LHV and CGE. Lower temperature gasification using oxygen at 873 increased CO+H2, LHV and CGE for LRC compared to higher temperatures at 973K and 1073K. This prediction suggests that LRC gasification using oxygen at lower temperature increases the LRC gasification efficiency.


2007 ◽  
Vol 116 (4) ◽  
pp. 209-216 ◽  
Author(s):  
Ian Grey ◽  
Ken McDonald ◽  
Michael Fisher-White ◽  
Malisja de Vries

2016 ◽  
Vol 20 (suppl. 1) ◽  
pp. 167-181
Author(s):  
Milic Eric ◽  
Milan Stakic ◽  
Milos Banjac

An overview of the current status of low-rank coal upgrading technologies is presented in the paper, particularly with respect to drying and dewatering procedures. In order to calculate the significant parameters of the moisture removal process, a model of convective coal drying in a fluid bed, based on the two-phase (bubbling) fluidization model proposed by Kunii and Levenspiel, is developed and presented. Product-specific data (intraparticle mass transfer, gas-solid moisture equilibrium) related to the particular coal variety addressed here (Kolubara lignite) are obtained through preliminary investigations. Effective thermal conductivity of the packed bed as defined by Zehner/Bauer/Schl?nder is used to define heat transfer mechanisms occurring in the suspension phase of the fluid bed. A completely new set of experimental data obtained has been successfully used to validate the model additionally.


2018 ◽  
Author(s):  
Jayeeta Chakraborty ◽  
◽  
Robert B. Finkelman ◽  
William H. Orem ◽  
Matthew S. Varonka ◽  
...  

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