Upgrading of light cycle oil via coupled hydrogenation and ring-opening over NiW/Al2O3-USY catalysts

Upgrading of light cycle oil via coupled hydrogenation and ring-opening over NiW/Al2O3-USY catalysts
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NiW/Al2O3-USY 催化剂耦合加氢开环升级轻循环油

DOI:
10.1016/j.cattod.2010.04.018
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发表时间:
2010-12
期刊:
影响因子:
5.3
通讯作者:
--
中科院分区:
化学2区
文献类型:
--
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通过水热和酸处理,制备了一系列不同酸度和孔径的超稳定Y (USY)沸石样品。在USY沸石和Al2O3的混合载体上维持NiW硫化物催化剂。以四氢化萘为模型化合物,在连续固定床反应器上研究了催化偶联加氢和开环性能。在所研究的反应条件下[T=613K, P=4.0MPa, LHSV=2.0h−1,H2/油(v/v)=500],所有催化剂均表现出较高的四氢萘转化率。产物收率和选择性主要取决于沸石的性质(即酸度)。沸石的酸度是影响四氢化萘开环选择性的关键因素。对于中等酸度的USY沸石,在c10产率为98.2%的条件下,最高十六烷开环产率为39.1wt%。使用流体催化裂化轻循环油原料,催化剂的活性高于商用催化剂,在柴油收率为97.6wt%的情况下,十六烷数增加了14个单位。由于开环反应的第一步是加氢反应,因此催化剂必须具有较高的加氢活性。使用本文提供的支撑,ws2slab在催化剂上的平均层数高达2.7。
A series of ultrastable Y (USY) zeolite samples with different acidities and pore sizes are prepared via hydrothermal and acid treatments. NiW sulfide catalysts are maintained on a mixed support of USY zeolite and Al2O3. The catalytic coupled hydrogenation and ring-opening performance are studied on a continuous fixed-bed reactor using tetralin as the model compound. All catalysts show high tetralin conversions under the reaction conditions studied [T=613K, P=4.0MPa, LHSV=2.0h−1, H2/oil (v/v)=500]. Product yields and selectivity are mainly determined by the zeolite property (i.e., acidity). A medium to strong zeolite acidity is the key factor in the ring-opening selectivity of tetralin. A maximum high cetane ring-opening product yield of 39.1wt% is obtained at a C10yield of 98.2wt% for a USY zeolite with medium acidity. Using an fluid catalytic cracking light cycle oil feedstock, the activity of the catalyst is higher than that of commercial catalysts, giving a 14-unit cetane number increase at a diesel yield of 97.6wt%. Because the first step of the ring-opening reaction is hydrogenation, the catalyst must have high hydrogenation activity. The WS2slabs have a high average layer number of 2.7 on the catalyst using the support presented here.
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