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FCC催化剂组元上轻柴油裂化反应焦炭的结构组成 被引量:13

STRUCTURE AND COMPOSITION OF COKE DEPOSITED ON COMPONENTS OF FCC CATALYST DURING GAS OIL CRACKING
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摘要 结合柱色谱层析分离、GC/MS和场解析质谱(FDMS)技术,建立了一种可萃取焦的分离检测方法,并考察了不同FCC催化剂组元轻柴油裂化反应焦炭的组成结构。结果表明,在较低反应温度下(400~460℃),Y型沸石上的焦炭含较大比例的可萃取焦,USY沸石的可萃取焦所占比例低于REY沸石的,表明USY沸石上焦炭的分子缩合度高于REY沸石;较高反应温度下(520℃),沸石上的焦炭中95%以上以高缩合度不可萃取焦状态存在。基质上的焦炭中,仅在较低的反应温度下(400℃)含有很少量可萃取焦,焦炭缩合度远高于沸石组分上的焦炭。可萃取焦以多环芳烃(3~8环结构,烷基侧链碳数不大于8)为主要组分;不可萃取焦呈无定形状态,nH/nC比在0.3~0.5之间。 An analytical method combining silica gel column chromatography separation, GC/ MS and FDMS was developed to determine the composition and structure of the soluble coke (S-coke). The characteristics of coke deposited on Y zeolites and the matrix of FCC catalyst during gas oil cracking under different reaction temperatures were investigated. The results indicate that, under lower reaction temperatures (400-460°C), most of the coke deposited on Y zeolites are soluble. Though the coke content was lower on USY zeolites, the coke substance was more condensed than those on REY zeolites. Under a higher temperature 520°C, insoluble coke (Ins-coke) appeared to be the main component of the coke. Only a little part of coke on the matrix was soluble even under a lower reaction temperature 400°C, which indicates that coke substance deposited on the matrix is more condensed than on Y zeolites. The S-coke comprised mainly methyl polyaromatic derivatives with 3-8 aromatic rings, having methyl amounts &le8. The Ins-coke was amorphous, with aromatic H/C ratio: 0.3-0.5.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2004年第5期71-77,共7页 Acta Petrolei Sinica(Petroleum Processing Section)
基金 国家重点基础研究发展规划项目资助(G2000048001)
关键词 FCC 催化剂 柴油 裂化反应 焦炭 Y型沸石 Coke Coking Column chromatography Composition Gas oils Silica gel Zeolites
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  • 1Mihinndou-Koumba P C, Cerqueira H S, Magnoux P, et al. Methylcyclohexane transformation over HFAU, HBEA, and HMFI zeolites Ⅱ Deactivation and coke formation[J]. Ind Eng Chem Res, 2001, 40: 1042-1052.
  • 2Qian K N, Tomczak D C, Rakiewicz E F, et al. Coke formation in the fluid catalytic cracking process by combined analytical techniques[J]. Energy & Fuels, 1997, 11: 596-601.
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