山西某地贫煤加氢增黏中铁基液体催化剂的作用机制探索

Mechanism exploration of iron-based liquid catalysts for viscosity enhancement via hydrogenation of lean coal from a region in Shanxi Province

  • 摘要: 炼焦煤作为生产焦炭的唯一原料,支撑着钢铁工业的稳定发展。然而,我国天然炼焦煤资源几近枯竭,难以支撑钢铁行业高质量发展。将储量丰富的其他煤种加氢增黏制备人工焦煤,有望解决上述问题。基于此,通过构建BMIMCl/FeCl2液体催化剂,研究其对山西某贫煤加氢增黏的影响规律,结合表征,推测催化剂的作用机制,结果表明:BMIMCl/FeCl2液体催化剂在370 ℃、氢气压力2 MPa下,可将人工焦煤黏结指数提升至65,人工焦煤收率达98.78%。催化剂历经6次循环后,人工焦煤的黏结指数仍维持在60左右,且液相回收率达99.12%。相较于原煤,人工焦煤中的脂氢增加,含氧官能团减少,黏结性大幅度提升。结合多种表征手段对加氢前后的样品进行分析,发现液体催化剂分散性好、稳定性佳,且在液相中的铁离子主要是以Fe3+的状态存在,具有更强的电负性。此外,GC-MS表明,四氢萘中氢的消耗量与人工焦煤黏结性变化呈正相关趋势。利用DFT与CDD,计算了液体催化剂中C2位点对氢自由基的吸附能力,发现咪唑环上C2位点对于氢自由基的吸附能为−1.70688 eV,低于四氢萘中α位氢自由基的解离能,证实了其是催化剂的活性中心位点。推测催化剂的作用机制为:BMIMCl/FeCl2可强化氢自由基的供给,促使煤热解自由基碎片与氢自由基结合,防止煤热解自由基碎片的过度加氢,使其碎裂成小分子碎片,从而实现煤加氢程度的精准控制。

     

    Abstract: As the only raw material for coke production, coking coal supports the stable development of the iron and steel industry. However, China’s natural coking coal resources are nearly depleted, making it difficult to support the high-quality development of the iron and steel industry. Preparing artificial coking coal by hydrogenating and viscosifying other coal species with abundant reserves is expected to solve the above problem. Based on this, a BMIMCl/FeCl2 liquid catalyst was constructed to study the effect of the BMIMCl/FeCl2 liquid catalyst on the hydrogenation and viscosity enhancement of a lean coal from Shanxi. The mechanism of the catalyst was hypothesized in conjunction with the characterization results. The results showed that the BMIMCl/FeCl2 liquid catalyst was used to increase the bonding index of artificial coking coal to 65 and the yield of artificial coking coal to 98.78% at 370 ℃ and a hydrogen pressure of 2 MPa. The bonding index of the artificial coking coal remained around 60 after six cycles of the catalyst, and the liquid phase recovery was 99.12%. Compared to raw coal, artificial coking coal has an increase in aliphatic hydrogen, a decrease in oxygen-containing functional groups, and substantial increase in bonding. The samples before and after hydrogenation were analyzed by various characterization methods. It was found that the liquid catalyst was well-dispersed and stable, and the iron ions in the liquid phase were mainly in the state of Fe3+, which had a stronger electronegativity. In addition, GC-MS analysis showed that the hydrogen consumption in tetralin had a positive correlation with the change in the bonding of artificial coking coal. Using DFT and CDD, the adsorption capacity of the C2 site for hydrogen radicals in the liquid catalyst was calculated. It was found that the adsorption energy of the C2 site on the imidazole ring for hydrogen radicals was −1.70688 eV, which was lower than the dissociation energy of the α-site hydrogen radicals in tetralin. This proved that the C2 site was the active center of the catalyst. The mechanism of the catalyst is hypothesized as follows: BMIMCl/FeCl2 enhances the supply of hydrogen radicals and induces coal pyrolysis radical fragments to combine with hydrogen radicals, preventing the over-hydrogenation of coal pyrolysis radical fragments, which would fragment into small molecular fragments, thus realizing the precise control of the degree of coal hydrogenation.

     

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