New cognition on coke degradation regions and quantificational control by potassium and sodium in alkali enriched model for BF
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摘要: 堿金屬對高爐內焦炭的破壞大多通過研究堿金屬碳酸鹽對焦炭氣化反應的影響,從而得出鉀、鈉破壞性相近,在控制堿金屬入爐時也基本不對二者進行區分;但高爐調研表明在堿金屬富集明顯加劇的區域堿金屬碳酸鹽已分解且焦炭中鉀含量均大于鈉.本文通過熱力學計算得知在堿富集區域堿金屬主要以單質蒸氣而非碳酸鹽或氧化物形式存在,據此設計了模擬此區域有無CO2時鉀、鈉單質蒸氣在焦炭上的自主吸附和破壞實驗,結合原子吸收光譜法、X射線衍射法和掃描電鏡-能譜分析發現鉀蒸氣和焦炭中灰分大量結合形成鉀霞石后體積膨脹、裂紋擴展導致堿金屬富集區域鉀在焦炭上的吸附和破壞能力均遠大于鈉,因此建議盡量采用低灰分焦炭并嚴格控制入爐鉀負荷.進一步研究體系中不同鉀蒸氣含量對氣化反應的影響規律,得出當鉀蒸氣與焦炭的氣固質量比率超過3%后焦炭反應性陡升.依據堿金屬富集區域鉀、鈉在焦炭上的不同吸附和破壞性,建立了鉀、鈉各自入爐上限及總量上限的量化控制模型.Abstract: The effects of potassium and sodium on coke degradation are commonly thought to be similar by studying the influence of alkali carbonates on coke gasification, and the amounts of potassium and sodium into the blast furnace (BF) are controlled without considering the differences. But BF investigations indicate that alkali carbonates have decomposed and in coke the potassium content is always larger than the sodium content, where the enrichment of alkali metals is obviously aggravated. In this article it is found by thermodynamic calculations that alkali metals exist as simple substance vapors instead of carbonates or oxides in the alkali enriched regions. Based on that, experiments for testing the autonomic absorption and damage of potassium and sodium vapors on coke with or without carbon dioxide were designed to simulate the alkali enriched regions. Atomic absorption spectrometry (AAS), X-ray diffraction (XRD) and scanning electron microscope-energy dispersive spectrometry (SEM-EDS) analysis reveal that the absorbance and damage of potassium vapor on coke are much larger than those of sodium vapor because of easy combination with ash in coke to form kaliophilite, which induces volume expansion and crack propagation. So it is proposed that the ash content in coke should be low and potassium into BF should be strictly controlled. Coke gasification tests with different contents of potassium vapor show a steep ascent in coke reaction index (CRI) when the mass ratio of potassium vapor to coke in the gas-solid system is above 3%. According to the different absorption and damage effects of potassium and sodium on coke, quantificational control models are constructed for determining the upper limits of potassium and sodium as well as the total amount into BF.
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Key words:
- blast furnaces /
- alkali metals /
- vapor /
- coke /
- ash /
- degradation
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