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甲烷气氛下铁基催化剂对低阶煤温和液化的影响

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针对煤直接液化的高温高压苛刻反应条件和高昂的氢气成本问题,通过降低煤液化反应温度、压力和更换供氢气氛等方法来优化工艺过程.选用四种铁基催化剂研究低阶煤在甲烷气氛下温和液化的反应特性,研究结果表明:神华黑山长焰煤HS在温度350 ℃、初始压力3 MPa的甲烷气氛下液化产物为轻质气体、液化油和沥青质;以FeSO4为催化剂时沥青质的产率最高达到8.03%,并将煤液化的转化率提升了 6.10%;以FeS为催化剂时油气产率提升了3.48%;助剂硫元素的加入对煤液化反应总转化率的提升有着重要作用;Fe粉、Fe+S和FeS催化剂的加入有助于提升煤液化油中单环芳烃的含量.
Effect of iron-based catalyst on mild liquefaction of low rank coal in methane atmosphere
Aiming at the high temperature and high pressure reaction conditions and high hydrogen cost of direct coal liquefaction,the process was optimized by reducing the temperature and pressure of coal liquefaction reaction and improving the hydrogen supply atmosphere.Four kinds of iron-based catalysts were used to study the reaction characteristics of mild liquefaction of low-rank coal under methane atmosphere.The results show that the liquefaction products of Shenhua Heishan long flame coal HS are light gas,liquefied oil and asphaltene under methane atmosphere of 350 ℃ and initial pressure of 3 MPa.When FeSO4 is used as catalyst,the yield of asphaltene reaches the highest 8.03%,and the conversion rate of coal liquefaction increases by 6.10%.When FeS was used as catalyst,the oil and gas yield increased by 3.48%.The addition of sulfur element plays an important role in the improvement of the total conversion of coal liquefaction reaction.The addition of Fe powder,Fe+S and FeS catalysts is helpful to increase the content of single cyclic aromatic hydrocarbons in coal liquefaction oil.

low-rank coaliron-based catalystmild liquefactionmethane

马桂林、周亚笑、吴诗勇、李超、黄峰、白金锋、徐静

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辽宁科技大学化学工程学院辽宁省煤化工专业技术创新平台,辽宁鞍山 114051

低阶煤 铁基催化剂 温和液化 甲烷

辽宁省兴辽英才计划科技创新领军人才项目

XLYC2002063

2024

煤炭加工与综合利用
中国煤炭加工利用协会

煤炭加工与综合利用

影响因子:0.496
ISSN:1005-8397
年,卷(期):2024.(3)
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