Modified stoichiometric equilibrium model for sewage sludge gasification and its validation based on experiments in a downdraft gasifier

Author(s):  
R. Bijesh ◽  
P. Arun ◽  
C. Muraleedharan
Author(s):  
Pavan V Kashyap ◽  
Rose Havilah Pulla ◽  
Amit Kumar Sharma ◽  
Pankaj Kumar Sharma

2015 ◽  
Vol 36 ◽  
pp. 241-255 ◽  
Author(s):  
Le Rong ◽  
Thawatchai Maneerung ◽  
Jingwen Charmaine Ng ◽  
Koon Gee Neoh ◽  
Boon Huat Bay ◽  
...  

Proceedings ◽  
2019 ◽  
Vol 38 (1) ◽  
pp. 9
Author(s):  
Alves ◽  
Calado ◽  
Panizio ◽  
Santos ◽  
Gonçalves ◽  
...  

co-gasification experiments with mixtures in various proportions of waste wood (WW) and sewage sludge (SS) were performed in a downdraft gasifier, in order to evaluate process performance and properties of gas and chars. Addition of SS improved the energy conversion efficiency and product gas yield, and minimised the formation of tars. Char production was greater, with formation of agglomerations inside the reactor. The optimal waste mixture contained 87.5 wt.% WW and 12.5 wt.% SS, generating a product gas yield of 2.9 m3/kg waste with a calorific value of 4.8 MJ/m3, and a tar production of 4.7 g/kg waste.


2012 ◽  
Vol 27 (1) ◽  
pp. 229-236 ◽  
Author(s):  
Weerachai Arjharn ◽  
Thipsuphin Hinsui ◽  
Pansa Liplap ◽  
G. S. Vijaya Raghavan

2017 ◽  
Vol 2017 ◽  
pp. 1-14 ◽  
Author(s):  
Aïda Ben Hassen Trabelsi ◽  
Amina Ghrib ◽  
Kaouther Zaafouri ◽  
Athar Friaa ◽  
Aymen Ouerghi ◽  
...  

Solar dried sewage sludge (SS) conversion by pyrolysis and gasification processes has been performed, separately, using two laboratory-scale reactors, a fixed-bed pyrolyzer and a downdraft gasifier, to produce mainly hydrogen-rich syngas. Prior to SS conversion, solar drying has been conducted in order to reduce moisture content (up to 10%). SS characterization reveals that these biosolids could be appropriate materials for gaseous products production. The released gases from SS pyrolysis and gasification present relatively high heating values (up to 9.96 MJ/kg for pyrolysis and 8.02  9.96 MJ/kg for gasification) due to their high contents of H2 (up to 11 and 7 wt%, resp.) and CH4 (up to 17 and 5 wt%, resp.). The yields of combustible gases (H2 and CH4) show further increase with pyrolysis. Stoichiometric models of both pyrolysis and gasification reactions were determined based on the global biomass formula, CαHβOγNδSε, in order to assist in the products yields optimization.


Author(s):  
Xiao-Xu Fan ◽  
Kai Yan ◽  
Rong-Feng Sun ◽  
Li-Guo Yang ◽  
Hai-Bin Guan

AIChE Journal ◽  
2015 ◽  
Vol 61 (8) ◽  
pp. 2508-2521 ◽  
Author(s):  
Zhehan Ong ◽  
Yongpan Cheng ◽  
Thawatchai Maneerung ◽  
Zhiyi Yao ◽  
Yen Wah Tong ◽  
...  

2001 ◽  
Vol 42 (2) ◽  
pp. 157-172 ◽  
Author(s):  
Adnan Midilli ◽  
Murat Dogru ◽  
Colin R. Howarth ◽  
Mike J. Ling ◽  
Teoman Ayhan

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