典型烟煤热解机理的反应动力学模拟

Molecular reaction dynamics simulation of pyrolysis mechanism of typical bituminous coal via ReaxFF

  • 摘要: 建立合理有效的烟煤大分子模型,采用基于反应力场(Reactive Force Field,ReaxFF)的分子动力学方法模拟1400-2600 K典型烟煤的热解过程,得出产物分布和中间自由基的演变历程。研究表明,随着热解温度的升高,焦炭产量先增加后降低,焦油产量的变化趋势与焦炭相反,热解气产量单调增加。煤在低温下热解主要发生一次反应,生成焦油自由基碎片和小分子气体;高温下焦油碎片的二次反应显著,生成含量较多但数量较少的焦炭及含量与数量较多的小分子气体。2000 K是一次反应向二次反应的温度转折点。在高温热解时,煤中的C与H逐渐迁移到焦炭和焦油中,而含氧官能团较为活跃,O逐渐迁移到热解气中。二次反应阶段,O最活泼,H次之,C最稳定。热解过程中最先产生的气体是H2O;NH3主要来源于二次反应;H2S在二次反应阶段被消耗转化为其他产物;H2产量最多,且随热解温度升高而增加,尤其在二次反应中大量生成,主要源于裂解产生的氢自由基碰撞和芳香结构的缩合。基于ReaxFF模拟结果得到煤热解失重活化能为39.45 kJ/mol。

     

    Abstract: A reasonable and effective macromolecular model of bituminous coal was established. The molecular dynamics method based on reactive force field (ReaxFF) was used to simulate the pyrolysis process of typical bituminous coal in the range of 1400-2600 K. The distribution of products and evolution of intermediate radicals were analyzed. Calculation results showed that with increase of pyrolysis temperature, yield of char firstly increased and then decreased, while the trend in tar production was opposite. Yield of pyrolysis gas increased monotonously with increasing temperature. The pyrolysis of coal at low temperature mainly experienced primary reaction with formation of tar free radical fragments and small molecular gases. At high temperature, the secondary reaction of tar fragments was remarkable, and char with more content but less quantity and small molecular gas with more content and quantity were produced. The temperature turning point from the primary reaction to the second one was 2000 K. Under the high temperature pyrolysis conditions, C and H in coal gradually migrated into char and tar, while oxygen-containing functional groups were more active, resulting in migration of O to pyrolysis gases. In the secondary reaction stage, comparing chemical properties of the three elements C, H and O, O was the most active, H was the second, and C was the most stable. H2O was firstly released during pyrolysis. NH3 mainly came from secondary reactions during which H2S was consumed and converted into other products. Yield of H2 was the highest, and increased with increasing pyrolysis temperature. A large amount of H2 was generated in secondary reactions, which was mainly from collision of hydrogen radicals generated from pyrolysis and condensation of aromatic structures. Based on ReaxFF simulation results, the weightless activation energy of coal pyrolysis was 39.45 kJ/mol.

     

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