초록 ▼

Provided is a catalyst for hydrocracking a paraffinic hydrocarbon which provides satisfactorily high cracking activity and middle fraction yield as well as the low pour point of the fuel base material (the middle fraction) all together. The catalyst of the present invention comprises a USY zeolite d

Provided is a catalyst for hydrocracking a paraffinic hydrocarbon which provides satisfactorily high cracking activity and middle fraction yield as well as the low pour point of the fuel base material (the middle fraction) all together. The catalyst of the present invention comprises a USY zeolite derived from NaY used as the raw material and having a peak intensity of 30 or lower, appearing on the 111 surface upon X-ray diffraction, and a noble metal of Group VIII of the periodic table.

대표청구항 ▼

1. A catalyst for hydrocracking a paraffinic hydrocarbon, comprising a USY zeolite derived from NaY used as a raw material and having a peak intensity of not more than 30, appearing on a 111 surface upon X-ray diffraction, and a noble metal of Group VIII of the Periodic Table. 2. The catalyst accord

1. A catalyst for hydrocracking a paraffinic hydrocarbon, comprising a USY zeolite derived from NaY used as a raw material and having a peak intensity of not more than 30, appearing on a 111 surface upon X-ray diffraction, and a noble metal of Group VIII of the Periodic Table. 2. The catalyst according to claim 1, wherein an average particle size of the USY zeolite is not more than 1.0 μm. 3. The catalyst according to claim 1, further comprising an amorphous solid acid. 4. The catalyst according to claim 3, wherein the amorphous solid acid is at least one selected from the group consisting of silica-alumina, silica-zirconia, and alumina-boria. 5. The catalyst according to claim 3, wherein a mass ratio of the amorphous solid acid to the USY zeolite is at least one and not more than 60. 6. The catalyst according to claim 1, wherein a content of the USY zeolite is from 0.1 to 15 percent by mass. 7. The catalyst according to claim 1, wherein a silica-alumina molar ratio of the USY zeolite is in a range of 20 to 140. 8. The catalyst according to claim 1, wherein the NaY has a peak intensity of from 20 to 25. 9. A process for producing a fuel base material, comprising hydrocracking a paraffinic hydrocarbon using a catalyst comprising a USY zeolite derived from NaY used as a raw material and having a peak intensity of not more than 30, appearing on a 111 surface upon X-ray diffraction, and a noble metal of Group VIII of the Periodic Table.