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SULFITE OXIDATION UNDER FLUE GAS DESULFURIZATION CONDITIONS: ENHANCED OXYGEN ABSORPTION CATALYZED BY TRANSITION METALS.

机译:烟气脱硫条件下的亚硫酸盐氧化:过渡金属催化的增氧吸收。

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摘要

The sulfite oxidation reaction was studied by measuring the rate of oxygen absorption across an unbroken interface into 1 liter of unsparged, agitated sulfite (10 mM) and catalyst (0.01 to 100 mM) solution at pH 4-6 and 50(DEGREES)C. At catalyst concentrations enabling enhanced absorption all the incoming oxygen was consumed in a thin interfacial reaction zone and the bulk solution oxygen concentration was zero. Multivalent Fe, Mn, Co, Cu and Cr ions were potent catalysts under these conditions, univalent Ni was inactive. At 10 mM these catalysts gave pseudo-first order (in oxygen) rate constants of 8.6, 43, 4.7, 95 and 11 s('-1), respectively. However, values for Cu and Cr are uncertain because of long transient times. Dry catalyst added in its upper valence state (ferric, cupric, chromic) produced high initial rates that fell in one to six hours to steady state while catalyst added in its lower state (ferrous, manganous, cobaltous) showed no high rates and reached steady state in less than one minute. Ferric and ferrous eventually resulted in the same rate so the catalytically active agent was probably some ferric species--possibly FeOOH--but was solubility-limited at a total Fe concentration of about 0.01 mM at pH 5 resulting in an enhancement factor of 2.4 at all higher concentrations. The iron ions probably cycle, being reduced during initiation and re-oxidized in the reaction zone. Fe was a much stronger catalyst than Mn or Co but its rate was limited by ferric solubility. Thiosulfate (0.05-1 mM) had a stronger inhibiting effect and efficiency on Mn than on Fe. EDTA was an effective inhibitor for Fe at equal or greater concentrations. A generalized free radical mechanism is proposed to model the initiation, termination and inhibition of radical chain reactions. Rates for Fe and Co increase with pH from 4 to 5, perhaps due to an effect upon the catalytic regeneration reaction, while Mn was unchanged. Strong positive Mn-Fe synergisms were found to cause absorption rates of up to five times those expected.
机译:通过测量pH值为4-6和50(DEGREES)C跨1升未喷射,搅拌的亚硫酸盐(10 mM)和催化剂(0.01至100 mM)溶液的不间断界面的氧气吸收率来研究亚硫酸盐的氧化反应。在能够提高吸收率的催化剂浓度下,所有进入的氧气都在一个薄的界面反应区中被消耗掉,并且本体溶液中的氧气浓度为零。在这些条件下,多价铁,锰,钴,铜和铬离子是有效的催化剂,单价镍是惰性的。在10 mM时,这些催化剂的假一阶(在氧气中)速率常数分别为8.6、43、4.7、95和11 s('-1)。但是,由于过渡时间长,因此Cu和Cr的值不确定。以较高价态(铁,铜,铬)添加的干催化剂产生高的初始速率,在1-6小时内降至稳态,而以较低价态(铁,锰,钴)添加的催化剂则没有高速率并达到稳定不到一分钟的状态。铁和亚铁最终产生的速率相同,因此催化活性剂可能是某些铁物种-可能是FeOOH-但在pH 5时总Fe浓度约为0.01 mM时溶解度受到限制,导致增强因子为2.4。所有更高的浓度。铁离子可能循环,在引发过程中被还原并在反应区中被再次氧化。铁是一种比锰或钴强得多的催化剂,但其速度受到铁溶解度的限制。硫代硫酸盐(0.05-1 mM)对锰的抑制作用和效率强于对铁的抑制作用。 EDTA是相等或更高浓度的铁的有效抑制剂。提出了一种通用的自由基机制来模拟自由基链反应的引发,终止和抑制。 Fe和Co的比率随pH从4增加到5而增加,可能是由于对催化再生反应的影响,而Mn则保持不变。发现强的正Mn-Fe协同作用可导致吸收率高达预期的五倍。

著录项

  • 作者

    ULRICH, RICHARD KEVIN.;

  • 作者单位

    The University of Texas at Austin.;

  • 授予单位 The University of Texas at Austin.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 1983
  • 页码 191 p.
  • 总页数 191
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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