Integrated process for coal chemical demineralization and spent caustic regeneration- A pilot scale study
Indian coal washing plants face tremendous pressure in maintaining clean coal yield and handling the rejects. Conventional coal washing plants generate clean coal with 15–18% ash content and 35–50% yield by several physical beneficiation techniques. Handling and disposal of the rest of 50% reject is...
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Veröffentlicht in: | Journal of cleaner production 2021-12, Vol.327, p.129497, Article 129497 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | Indian coal washing plants face tremendous pressure in maintaining clean coal yield and handling the rejects. Conventional coal washing plants generate clean coal with 15–18% ash content and 35–50% yield by several physical beneficiation techniques. Handling and disposal of the rest of 50% reject is an environmental concern and hence, alternate processes for utilization of high-ash washery rejects are of high importance. In this work, the chemical demineralization process is explored at a pilot scale to produce the low ash clean coal from different washery rejects. 44.6%–67.8% demineralization is achieved with the single-stage alkali-acid leaching process and 68.4%–78.3% by multi-stage leaching at optimum operating conditions. However, the economics of the process depends on the regeneration of the spent alkali solution. Therefore, a two-step methodology for spent-alkali regeneration is developed. In the first step, carbonation of spent-alkali with CO2 separates almost >95% of the silica and alumina impurities. In the second step, 89.2% caustic soda is recovered by causticization using quick lime.
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•Coal washery generates ∼50% as high-ash rejects.•44.6%–67.8% demineralization is achieved with single-stage alkali-acid leaching process.•68.4%–78.3% demineralization is achieved by multi-stage leaching.•Two-step methodology for 89.2% caustic-soda recovery from spent-alkali.•>95% of the silica and alumina impurities removed and generates high-purity CaCO3. |
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ISSN: | 0959-6526 1879-1786 |
DOI: | 10.1016/j.jclepro.2021.129497 |