2022
DOI: 10.1007/s11085-022-10102-w
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Impact of Alkalis and Chlorides from Sugarcane Agriculture Residues on High Temperature Corrosion: A Review

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Cited by 6 publications
(5 citation statements)
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“…Currently, the most commonly used additive is sulfur-containing compounds. Taking liquid catalysts containing ammonium sulfate as an example, the liquid ammonium sulfate reacts with KCl in the flue gas to generate stable potassium sulfate, reducing the chlorine content in the flue gas and achieving the effect of mitigating corrosion [62]. Wang et al simulated the ash melting characteristics after the combustion of coal with high alkali metal and alkaline earth metal contents [63].…”
Section: Anticorrosion Technologymentioning
confidence: 99%
“…Currently, the most commonly used additive is sulfur-containing compounds. Taking liquid catalysts containing ammonium sulfate as an example, the liquid ammonium sulfate reacts with KCl in the flue gas to generate stable potassium sulfate, reducing the chlorine content in the flue gas and achieving the effect of mitigating corrosion [62]. Wang et al simulated the ash melting characteristics after the combustion of coal with high alkali metal and alkaline earth metal contents [63].…”
Section: Anticorrosion Technologymentioning
confidence: 99%
“…The Cl values for C75-EPL25 and C75-EBT25 are 0.020% and 0.021%, which are rather high when compared with coal at 0.005%. The presence of high Cl in both samples is thought to be one of the causes of the probe's surface condition, which still has slag and will trigger corrosion attacks [20]. Furthermore, both samples have high alkaline values, indicating that chlorine can increase the volatility of alkalis (K) in the gas phase, such as KCl.…”
Section: Probe After Ash Collectedmentioning
confidence: 99%
“…Furthermore, both samples have high alkaline values, indicating that chlorine can increase the volatility of alkalis (K) in the gas phase, such as KCl. At operating temperatures, both phases can produce deposits that condense on the pipe surface to form alkali sulfate and chloride [21].…”
Section: Probe After Ash Collectedmentioning
confidence: 99%
“…Sistemas de cogeração operando com parâmetros de vapor mais elevados (acima de 100 bar/530ºC) são encontrados no exterior e analisados nos casos 4 e 5. Apesar de ser mais eficiente, o uso de parâmetros de vapor elevados não é comum, pois o risco de problemas de corrosão em caldeiras de bagaço aumenta com a temperatura de superaquecimento do vapor [133], [134]. Demais dados de entrada, utilizados para a modelagem do sistema de referência, são listados na seção 4.1.1, tais como a quantidade de cana processada na safra (4,7 milhões TC/safra), consumo de vapor de processo (400kgvapor/TC) e PCI do bagaço de cana (6,73 MJ/kg).…”
Section: 11sistema De Cogeração De Uma Usina De Cana-de-açúcarunclassified
“…As baixas eficiências, por exemplo, para caldeiras operando a 22 bar confirmam o desperdício, sob o ponto de vista energético e exergético, de se utilizar estas caldeiras no setor sucroalcooleiro brasileiro. Embora haja um aumento na eficiência elétrica da planta, os custos e riscos de corrosão na caldeira podem aumentar com parâmetros de vapor vivo mais altos [133]. Esta é uma das razões pelas quais as modernas usinas de cana-de-açúcar ainda utilizam caldeiras de 68 bar e temperaturas de vapor superaquecido na faixa de 480ºC a 520ºC [9],…”
Section: 21desempenho Dos Sistemas De Cogeraçãounclassified