Middle distillate hydrocracking catalyst
US-9944863-B2 · Apr 17, 2018 · US
US11400435B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11400435-B2 |
| Application number | US-201917289891-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 31, 2019 |
| Priority date | Nov 2, 2018 |
| Publication date | Aug 2, 2022 |
| Grant date | Aug 2, 2022 |
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A hydrofinishing catalyst according to the present invention includes an amorphous silica-alumina support; and a hydrogenated active metal supported on the support, and has an Al composition having a total mass (wt %) of Al and Si as a denominator and a mass (wt %) of Al as a numerator with respect to a reference line, which is a straight line passing through the center of a cross-section of the support, locations evenly spaced apart along the reference line are sequentially numbered, where composition uniformity, which is defined as UN by the Al composition at the i-th location and an average Al composition at the cross-section of the support passing through the center of the support, is 3.0 or less.
Opening claim text (preview).
The invention claimed is: 1. A hydrofinishing catalyst comprising: an amorphous silica-alumina support; and a hydrogenated active metal supported on the support, wherein composition uniformity defined as the following Expression 1 satisfies Expression 2, UN = ∑ i = 1 i = M C Al ( i ) - C Al ( ave ) M × C Al ( ave ) × 1 0 0 ( Expression 1 ) in Expression 1, UN is composition uniformity, C Al is an Al composition having a total mass (wt %) of Al and Si as a denominator and a mass (wt %) of Al as a numerator, C Al (ave) is an average Al composition on a cross section of a support passing through the center of the support, C Al (i) is an Al composition at an i-th position of positions spaced apart from each other by a predetermined interval along a reference line and sequentially numbered, the reference line being a straight line passing through the center of the cross section of the support, and M is a total number of positions at which the Al composition is measured at the reference line, and is a natural number of 20 to 500, UN≤ 3.0, and (Expression 2) The catalyst satisfies the following Expression 4 (Expression 4) Amount of Bronsted acid sites measured by adsorption of pyridine at 200° C.≥30 μmol/g. 2. The hydrofinishing catalyst of claim 1 , wherein the catalyst satisfies the following Expression 3, 5.00≤ Pv (100−500)/ Pv (10−500)*100 (Expression 3) in Expression 3, Pv(10−500) is a total volume (cm 3 /g) of pores within a size range of 10 to 500 nm per unit mass of the catalyst, and Pv(100−500) is a total volume (cm 3 /g) of pores within a size range of 100 to 500 nm per unit mass of the catalyst. 3. The hydrofinishing catalyst of claim 1 , wherein the catalyst has a strength of a Bronsted acid site satisfying the following Expression 5, Expression 6, or Expressions 5 and 6, (Expression 5) Amount of Bronsted acid sites measured by adsorption of pyridine at 300° C.≥25 μmol/g, (Expression 6) Amount of Bronsted acid sites measured by adsorption of pyridine at 400° C.≥10 μmol/g. 4. The hydrofinishing catalyst of claim 1 , wherein the active metal is one or two or more metals belonging to Groups VI to VIII. 5. The hydrofinishing catalyst of claim 4 , wherein the active metal contains Pd, Pt, or Pd and Pt. 6. The hydrofinishing catalyst of claim 4 , wherein the catalyst contains a first active metal and a second active metal, and a weight ratio of the first active metal to the second active metal is 1.0:0.1 to 1.0. 7. The hydrofinishing catalyst of claim 1 , wherein the catalyst contains 0.1 to 5 wt % of the active metal. 8. A method for producing base oil, comprising: a step of dewaxing raw oil for producing base oil in the presence of an isomerization catalyst to obtain a catalytic dewaxed oil fraction; and a step of hydrofinishing the catalytic dewaxed oil fraction using the hydrofinishing catalyst of claim 1 to produce base oil.
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