微波辅助催化加热提高页岩甲烷裂解产氢效率

K. Yan, Q. Yuan, Xiangyu Jie, Xiaoqiang Li, J. Horita, Jacob Stephens
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摘要

在美国,蒸汽甲烷重整(SMR)技术以天然气为主要原料,产生约95%的氢气(H2)。虽然氢气是清洁的,但通过SMR制氢的过程却不是,因为它排放的二氧化碳(CO2)是氢气的10倍左右。二氧化碳必须被捕获并封存在水库或含水层系统中,这是非常昂贵的。一种革命性的方法是利用储层中丰富的未开采碳氢化合物,直接从储层中生成和提取氢气。这种方法不涉及天然气的生产、运输或精炼。同时,如果产生二氧化碳,将同时被封存在储层中,而不会产生到地面。因此,这种方法具有潜在的低成本和环境友好性。在本文中,我们建议使用微波辅助催化加热来提高页岩气储层中甲烷向氢的转化。为了验证这一概念,我们进行了一系列实验,在微波反应器中裂解流经页岩岩石样本和粉末的甲烷流。以碳化硅(SiC)作为微波受体,页岩样品的温度可快速达到700℃以上。在实验温度为500°和600°时,Fe和Fe3O4催化剂的甲烷转化率分别达到40.5%和100%。有趣的是,与加热样品中相同重量百分比的SiO2相比,页岩的存在有利于甲烷在相对较低的温度下裂解。页岩中碳酸盐的热分解作用也有利于提高页岩的渗透率。研究了不同页岩比重比和甲烷流量的影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Microwave-Assisted Catalytic Heating for Enhanced Clean Hydrogen Generation from Methane Cracking in Shale Rocks
Steam methane reforming (SMR) technology generates about 95% hydrogen (H2) in the United States using natural gas as a main feedstock. While hydrogen is clean, the process of hydrogen generation via SMR is not, as it emits about 10 times more carbon dioxide (CO2) than hydrogen. The CO2 has to be captured and sequestrated in reservoirs or aquifer systems, which is costly. A revolutionary approach is to generate and extract hydrogen directly from petroleum reservoirs by taking advantage of the abundant unrecovered hydrocarbons in reservoirs. This approach does not involve natural gas production, transportation, or refinery. Meanwhile, the CO2, if generated, will be sequestrated simultaneously in reservoirs without being produced to surface. This approach is therefore potentially low cost and environmentally friendly. In this paper, we propose to use microwave-assisted catalytic heating to enhance methane conversion to hydrogen within shale gas reservoirs. To validate this concept, we conducted a series of experiments to crack methane streams flowing through shale rock samples and powders in a microwave reactor. With silicon carbide (SiC) as the microwave receptor, the temperature of shale samples can quickly reach to above 700 °. The methane conversion efficiency is up to 40.5% and 100% in the presence of Fe and Fe3O4 catalysts at the measured temperature of 500° and 600 °, respectively. Interestingly, the presence of shale is favorable for methane cracking at a relatively lower temperature compared to the case with the same weight percentage of SiO2 in heated samples. The thermal decomposition of carbonate in shale rocks also benefits the improvement of permeability of shale. The influences of different shale weight ratios and methane flow rates are also investigated.
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