2020
DOI: 10.1016/j.joei.2020.03.009
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Effect of high silicon-aluminum coal ashes on sintering and fusion characteristics of a potassium-rich biomass ash

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Cited by 33 publications
(8 citation statements)
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“…Comparing the mineral composition of raw coal, roof rock, and mixed pyrolysis semicoke, it was found that after pyrolysis, orthoclase, pyrite, and kaolinite disappeared, and sanidine, pyrrhotite, and albite appeared. With the increase of temperature, orthoclase changes its crystal structure into sanidine with lower degree of order 24–26 . In the UCG pyrolysis process, kaolinite loses water to form metakaolinite.…”
Section: Resultsmentioning
confidence: 99%
“…Comparing the mineral composition of raw coal, roof rock, and mixed pyrolysis semicoke, it was found that after pyrolysis, orthoclase, pyrite, and kaolinite disappeared, and sanidine, pyrrhotite, and albite appeared. With the increase of temperature, orthoclase changes its crystal structure into sanidine with lower degree of order 24–26 . In the UCG pyrolysis process, kaolinite loses water to form metakaolinite.…”
Section: Resultsmentioning
confidence: 99%
“…An AFT analyzer (Keli Co., Ltd., Hebi, China) was used to test AFT under an oxidation atmosphere in accordance with the ASTM D1857 standard [45]. According to the ash cone, four characteristic temperatures (DT, softening temperature (ST), hemispherical temperature (HT), and flow temperature (FT)) were identified.…”
Section: Ash Fusion Temperature Testmentioning
confidence: 99%
“…To maintain continuous liquid slagging in industrial gasification operations, the gasifier operating temperature is typically about 100–150 °C above the flow temperature (FT) of the feedstock. For coal with high ash melting temperatures, such as high-silica–aluminum coals, the existence of a large number of refractory materials in ash slag at high temperatures can cause poor ash slag fluidity. Furthermore, as a result of the complexity and variability of coal types, for some coal with a lower ash melting temperature, although the operating temperature is about 100 °C above the FT, its viscosity is still higher and shows poor fluidity, which makes it difficult to match the liquid slagging requirements of an entrained-flow gasifier. Therefore, in an actual industrial operation process, coal blending or adding flux is commonly adopted to achieve the regulation of coal ash slag fluidity, which is in essence to realize the regulation of coal ash fluidity by altering the ash chemical composition of the feed coal. Because the transportation cost of coal blending is high and difficult to control, the addition of flux is the optimal scheme to regulate the fluidity of coal ash slag.…”
Section: Introductionmentioning
confidence: 99%