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二氧化碳-氮气混合气体在微粉硅胶中生成水合物的 实验研究

  • 刘军 ,
  • 梁德青
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  • 1. 中国科学院广州能源研究所,广州 510640;
    2. 中国科学院天然气水合物重点实验室,广州 510640;
    3. 广东省新能源和可再生能源研究开发与应用重点实验室,广州 510640;
    4. 中国科学院大学,北京 100049
刘军(1991-),男,博士研究生,主要从事天然气水合物动力学研究。梁德青(1970-),男,研究员,博士生导师,主要从事天然气水合物研究。

收稿日期: 2019-03-20

  修回日期: 2019-05-06

  网络出版日期: 2019-08-29

基金资助

国家自然科学基金项目(51706230,51376182)

Investigation on CO2/N2 Mixed Gas Hydrate Formation in a Silica Gel Bed

  • LIU Jun ,
  • LIANG De-qing
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  • 1. Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, China;
    2. CAS Key Laboratory of Gas Hydrate, Guangzhou 510640, China;
    3. Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development, Guangzhou 510640, China;
    4. University of Chinese Academy of Sciences, Beijing 100049, China

Received date: 2019-03-20

  Revised date: 2019-05-06

  Online published: 2019-08-29

摘要

空气中CO2含量的增加导致了全球气候变暖问题。气体水合物能够有效分离出电厂尾气中的CO2,对改善环境具有重要意义。考察了微粉硅胶(silica gel)中80mol% N2与20mol% CO2混合气体水合物形成特性,选取压力范围为6.0 ~ 8.0 MPa,温度范围为 -20 ~ -5℃。研究发现,N2与CO2混合气进入反应釜后,直接生成水合物,诱导时间小于1 min。压力越高、温度越低,生成水合物的相对气体消耗量越大,最大的相对气体消耗量为0.115 (mol/mol),水的转化率最大为77.02mol%,前30 min水合物生成速率与压力无关。水合物气体消耗量越大,反应釜中剩余N2组分的含量越大,最大为90.95mol%。水合物生成驱动力越低,水合物中CO2 组分越高。在6.0 MPa、-5℃下,水合物中CO2组分最大为65.70mol%。

本文引用格式

刘军 , 梁德青 . 二氧化碳-氮气混合气体在微粉硅胶中生成水合物的 实验研究[J]. 新能源进展, 2019 , 7(4) : 309 -317 . DOI: 10.3969/j.issn.2095-560X.2019.04.003

Abstract

The increase of carbon dioxide content in the air leads to global climate problems. Gas hydrate can effectively separate carbon dioxide from power plant flue gas, which is of great significance to improve the environment. In this work, the CO2/N2 mixed gas hydrate formation in silica gel bed was studied under pressure and temperature ranges of (6.0 - 8.0 MPa) and (-20 - -5oC), respectively. Results showed that the mixed gas hydrate formed immediately when the flue gas was pressurized into the reactor, and the induction time was less than 1 min. The normalized gas consumption was larger at higher pressure or lower temperature. The largest normalized gas consumption was 0.115 (mol/mol), and the highest water conversion was 77.02mol%. Pressure had no effect on the normalized rate of gas consumed for the first 30 min. The gas proportion of N2 in equilibrium gas increased with the final gas consumption increase. The highest gas proportion of N2 in equilibrium gas was 90.95mol%. CO2 proportion in the hydrate was higher at lower hydrate formation driving force. The highest CO2 proportion in the hydrate was 65.70mol% at 6.0 MPa and -5oC.

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