CO water-gas-shift reaction character over Cu-Zn catalyst
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摘要: 通過考察不同條件下燒結對Cu-Zn和Fe-Cr催化劑變換反應性能的影響,并結合催化劑的化學吸附表征手段,探討了用Cu-Zn系催化劑替代Fe-Cr系催化劑作為高變催化劑的可行性.活性評價結果表明,從初期活性來看,Cu-Zn系催化劑不僅在低變溫度,而且在高變溫度下也優于Fe-Cr系催化劑;從催化劑的燒結特性來看,Cu-Zn系催化劑雖然在450℃的高溫燒結條件下于初期階段燒結明顯,但500h之后逐漸趨于穩定,穩定后的活性仍優于Fe-Cr系催化劑.活性評價結果與CO化學吸附量測試結果相吻合.據此提出了不使用Fe-Cr系催化劑,在高、低溫變換過程均使用Cu-Zn系催化劑的CO變換工藝,可將入口體積分數10%的CO去除到1%以下.Abstract: The effect of sintering on the performance of two kinds of catalysts was analyzed under various conditions,and chemisorption characterization of catalysts was carried out to investigate the feasibility of substituting Cu-Zn catalyst for Fe-Cr catalyst in high temperature CO water-gas shift process (HTS).Results of activity evaluation experiments show that as a fresh catalyst,Cu-Zn catalyst has a higher activity than Fe-Cr catalyst,not only in the temperature range of low temperature shift (LTS),but also in the temperature range of HTS.On the other hand,sintering of Cu-Zn catalyst is obvious in the beginning stage at a relative high temperature of 450℃,but gets steady after 500 h,and in the steady stage the activity of Cu-Zn catalyst is still higher than that of Fe-Cr catalyst.The results of activity evaluation accord with those of CO chemical sorption.A CO water-gas shift process with substituting Cu-Zn catalyst for Fe-Cr catalyst was suggested in both HTS and LTS processes,in which the CO content could be removed to below 1% from the inlet content of 10%.
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Key words:
- fuel cells /
- Cu-Zn catalyst /
- Fe-Cr catalyst /
- sintering
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