dc.contributor.author |
Saini, R |
|
dc.contributor.author |
Mahajani, SM |
|
dc.contributor.author |
Rao, DS |
|
dc.contributor.author |
Narayan, R |
|
dc.date.accessioned |
2024-07-25T04:17:08Z |
|
dc.date.available |
2024-07-25T04:17:08Z |
|
dc.date.issued |
2024 |
|
dc.identifier.citation |
International Journal Of Hydrogen Energy, 68, 2024; 823-833 |
|
dc.identifier.issn |
0360-3199 |
|
dc.identifier.uri |
http://ore.immt.res.in/handle/2018/3503 |
|
dc.description.abstract |
The co-gasification of high moisture and high volatile content low-rank lignite (LG) coal and a common waste generated from the brewed tea leaves was studied in a fluidized bed gasification unit. Multiple experiments were conducted at different temperatures, ranging from 800 degrees C to 900 degrees C, at fixed operating parameters to elucidate the catalytic thermo-chemical impact on the gasifier performance parameters. The catalytic effect of alkali and alkaline earth metals (AAEMs), especially CaO, K2O, and Na2O present in the spent tea waste (STW) sample, on the product gas composition and performance parameters during the co-gasification experiments with LG was demonstrated. Mixed blends of LG and STW showed enhancement in the overall reactivity of the steam gasification runs, compared to the LG-only feed, primarily due to the change in the surface morphology, textures, and pore structures of the solid product ash samples, as identified with the electron spectroscopy analysis. Liquid and product samples were analyzed using characterization techniques such as Fourier transform infrared (FTIR) spectroscopy, thermogravimetric analysis (TGA), X-ray diffraction (XRD), and scanning electron microscopyenergy dispersive X-ray analysis (SEM-EDX) analytical techniques, along with the proximate, ultimate, and Xray fluorescence (XRF) analysis of the gasification feed samples. An optimized blend ratio of 20 wt % of STW with LG sample enhanced the volumetric gas composition of H2 and CH4 gases from 52.03 % to 61.32 % and 3.98 %- 5.45 % (on a dry-N2-free basis) with a relatively constant CO gas composition. It showed a reduced CO2 composition from 28.64 % to 18.25 % (on a dry-N2-free basis) for the gasification temperature of 900 degrees C. Even at the lower gasification temperatures of 800 degrees C and 850 degrees C with LG + STW feed, steam gasification experiments showed relatively comparable or superior performance to gasification experiments at 900 degrees C with LG-only feed. The present study indicated a holistic way to utilize the spent tea waste generated from millions of homes and commercial establishments in various parts of the world with potential application towards synergistic gasification process with other conventional carbon-source materials. |
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dc.language |
en |
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dc.publisher |
Pergamon-Elsevier Science Ltd |
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dc.relation.isreferencedby |
SCI |
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dc.rights |
Copyright [2024]. All efforts have been made to respect the copyright to the best of our knowledge. Inadvertent omissions, if brought to our notice, stand for correction and withdrawal of document from this repository. |
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dc.subject |
Chemical Sciences |
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dc.subject |
Energy & Fuels |
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dc.title |
Co-gasification of lignite and spent tea waste for the generation of hydrogen-rich syngas in a fluidized bed gasifier |
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dc.type |
Journal Article |
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dc.affiliation.author |
CSIR IMMT, Dept Mineral Proc, Bhubaneswar 751013, Orissa, India |
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