Conversion Characteristics of Aromatic Hydrocarbons in Simulated Gaseous Atmospheres in Reducing Section of Two-Stage Entrained-Flow Coal Gasifier in Air- and 02/C02-
Conversion Characteristics of Aromatic Hydrocarbons in Simulated Gaseous Atmospheres in Reducing Section of Two-Stage Entrained-Flow Coal Gasifier in Air- and 02/C02-
复制标题
两级气流床煤气化炉还原段模拟气态芳烃在空气-和02/CO2-中的转化特性
DOI:
10.1021/ef301658d
复制
发表时间:
2013
期刊:
影响因子:
5.3
通讯作者:
et al.
中科院分区:
文献类型:
--
作者:
Yasuhiro SAKURAI;et al.
Conversion of refractory aromatic hydrocarbons was studied with an atmospheric flow reactor that simulated the reducing section of a two-stage entrained-flow coal gasifier in air-blown and O2/CO2-blown (CO2recycling) modes at temperatures of 1100–1400 °C. Mixed vapors of benzene and naphthalene (7/3 on a carbon basis) were fed into the reactor at total concentration in a range from 3.7 to 37 g·Nm–3together with a CO–CO2–H2–H2O mixture in the O2/CO2-blown mode or CO–CO2–H2–H2O–N2mixture in the air-blown mode. Soot was the major fate of the aromatics at the inlet benzene/naphthalene concentration of 35–37 g·Nm–3, and its yield was not influenced significantly either by the mode of gasification or temperature at 1200–1400 °C. The contribution of gas-phase reforming to the conversion of the aromatics became more important as their inlet concentration decreased. At the inlet concentration of 3.7–7.5 g·Nm–3, the O2/CO2-blown mode was clearly more effective in reducing the soot yield than the air-blown mode and increasing the gas yield. It was explained on the basis of a detailed chemical kinetic model that the increased partial pressure of CO2induced a higher concentration of key active species such as hydroxyl radicals that initiated the oxidative decomposition of the aromatics.