微流化床石灰石加氢反应机理和动力学研究:H2 浓度和天然石灰石的影响

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引用次数: 0

摘要

石灰石分解是水泥生产的第一步,会产生大量二氧化碳,为实现碳中和带来了巨大挑战。石灰石加氢可产生 CO 或 CH4,而不是 CO2,这可视为一种新的碳捕获方式,是一种很有前景的碳减排方法。在这项工作中,使用微流化床(MFB)反应器结合在线质谱仪,在不同的 H2 浓度下对纯 CaCO3 和几种天然石灰石样品进行了水解,以揭示石灰石氢化的机理和动力学。二氧化碳来自 CaCO3 的煅烧。CO 来自两个步骤:第一步是 CaCO3 的原位氢化,第二步是反向水气移动 (RWGS) 反应。二氧化碳在 H2 气氛中形成的活化能(Ea)低于 Ar 气氛。然而,不同浓度的 H2 对 CO2 生成的 Ea 没有明显影响。在 10%、30%、50% 和 70% 的 H2 气氛中,原位生成 CO 的 Ea 分别为 72.70 KJ/mol、54.53 KJ/mol、71.34 KJ/mol 和 60.29 KJ/mol。H2 浓度对 CO 的原位演化也没有明显影响。但是,H2 浓度会影响 RWGS 产生 CO 的 Ea。在 10%、30% 和 50%的 H2 气氛中,Ea 分别为 75.67 KJ/mol、167.59 KJ/mol 和 221.47 KJ/mol,而在 70% 的 H2 气氛中则不发生该反应。与纯 CaCO3 相比,石灰石加氢产生的 CO 更多,CO2 更少。在石灰石中,杂质元素是影响反应动力学的主要因素。过渡金属可以提高 CO2 生成速率,但对 CO 没有明显影响。高杂质石灰石的二氧化碳产率高于低杂质石灰石。过渡金属还能降低 CO2 生成和 RWGS 反应的 Ea。在 50% H2 大气中,CO2 生成的 Ea 为 88.87 KJ/mol,RWGS 生成 CO 的 Ea 为 137.60 KJ/mol。然而,在相同条件下,纯 CaCO3 的 Ea 分别为 126.91 KJ/mol 和 221.47 KJ/mol。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Study on the reaction mechanism and kinetics of limestone hydrogenation by micro fluidized bed: Effect of H2 concentration and natural limestone

Limestone decomposition is the first step in cement production, which produces a significant amount of CO2 and poses a significant challenge to achieve carbon neutrality. Hydrogenation of limestone can produce CO or CH4 instead of CO2, which can be considered as a new way of carbon capture, making it a promising method for carbon emission reduction. In this work, pure CaCO3 and several natural limestone samples were hydrolyzed under varying H2 concentration using a micro fluidized bed (MFB) reactor combined with online mass spectrometry to reveal the mechanism and kinetics of limestone hydrogenation.

The main gases produced by hydrogenation at 1 atm are CO and CO2. The CO2 comes from the calcination of CaCO3. The CO comes from 2 steps: the first step is the in-situ hydrogenation of CaCO3 and the second step is the Reverse Water Gas Shift (RWGS) reaction. The activation energy (Ea) of CO2 formation in H2 atmosphere is lower than in Ar atmosphere. However, there is no obvious effect of different H2 concentrations on the Ea of CO2 formation. The Ea of CO in situ formation is 72.70 KJ/mol, 54.53 KJ/mol, 71.34 KJ/mol and 60.29 KJ/mol in 10%, 30%, 50% and 70% H2 atmosphere, respectively. The H2 concentration also has no significant effect on the in-situ CO evolution. However, the H2 concentration can affect the Ea of CO produced by RWGS. The Ea is 75.67 KJ/mol, 167.59 KJ/mol and 221.47 KJ/mol in 10%, 30% and 50% H2 atmosphere, and this reaction doesn't occur in 70% H2 atmosphere. Compared with the pure CaCO3, the hydrogenation of limestone can produce more CO and less CO2. In limestone, impurity elements are the main factor affecting the reaction kinetics. Transition metals can increase the rate of CO2 production, but have no apparent effect on CO. The CO2 yield of high impurity limestone is higher than that of limestone with low impurities. Transition metals can also reduce the Ea of CO2 formation and the RWGS reaction. In the 50% H2 atmosphere, the Ea of CO2 formation is 88.87 KJ/mol and the Ea of CO from RWGS is 137.60 KJ/mol. However, under the same conditions, the Ea of pure CaCO3 is 126.91 KJ/mol and 221.47 KJ/mol.

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