甲烷化烟气能势转换效率分析

L. Mihaescu, G. Lăzăroiu, R. Grigoriu, L. Stănescu, Mihai Dragne, G. Negreanu, I. Balcu, C. Panait
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引用次数: 1

摘要

本文的目的是建立一个数学模型,该模型包括通过甲烷化过程脱碳的现象,借助于镍/氧化铝催化剂的使用。重点放在了冲击压力和温度范围对过程的影响。为了突出co2和h2反应物压力的影响,在220-260°C的温度范围内考虑了镍催化剂NKM - 4A。数值模拟中使用的模型来源于Langmuir - Hinshelwood机制,允许CO2和O(原子氧)的解离吸附,然后形成甲烷。通过实验验证了数值模拟结果,得出氢气压力与二氧化碳压力之比的最佳范围为3 ~ 4,进一步的实验数据将该范围扩大到5。还介绍了Constanța海事大学的实验基地,该基地配备了甲烷发生器和甲烷化装置。研究(在初期阶段)只进行了纯二氧化碳的转化,氢气与二氧化碳的比例为4。它们将扩展到驱动发电机的内燃机的烟气。
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An analysis of the efficiency of flue gases energy potential conversion through methanation
The purpose of the paper targets the development of a mathematic model that encompasses the phenomena of decarbonization through methanation processes, aided by the use of a nickel / alumina catalyst. Emphasis was placed on the impact pressure and temperature ranges have on the process. A nickel catalyst, type NKM – 4A was considered in a temperature range of 220-260 °C in order to highlight the influence of the pressure of CO2and H2reactants. The model used in numerical simulations is derived from the Langmuir - Hinshelwood mechanism, admitting dissociative adsorption of CO2 and O (atomic oxygen), after which methane is formed. The numerical simulations were validated experimentally, concluding in an optimal ratio of hydrogen pressureto carbon dioxide pressure in therangefrom 3 to 4, with further experimental data extending the range up to 5. The experimental base from the Maritime University of Constanța was also presented, a base equipped with a methane generator and a methaniser. The researches (in incipient phase) performed only the conversion of pure carbon dioxide with the ratio hydrogen to carbon dioxide equal to 4. They will be extended to the flue gases of an internal combustion engine driving an electric generator.
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