Base metal dewaxing catalyst
US-2017175011-A1 · Jun 22, 2017 · US
US10632453B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10632453-B2 |
| Application number | US-201815902211-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 22, 2018 |
| Priority date | Mar 3, 2017 |
| Publication date | Apr 28, 2020 |
| Grant date | Apr 28, 2020 |
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Methods, catalysts, and corresponding catalyst precursors are provided for performing dewaxing of diesel or distillate boiling range fractions. The dewaxing methods, catalysts, and/or catalyst precursors can allow for production of diesel boiling range fuels with improved cold flow properties at desirable yields. The catalysts and/or catalyst precursors can correspond to supported base metal catalysts and/or catalyst precursors that include at least two Group 8-10 base metals supported on the catalyst, such as a catalyst/catalyst precursor including both Ni and Co as supported metals along with a Group 6 metal (i.e., Mo and/or W). The support can correspond to a support including a zeolitic framework structure. The catalyst precursors can be formed, for example, by impregnating a support including a zeolitic framework structure with an impregnation solution that also includes a dispersion agent.
Opening claim text (preview).
The invention claimed is: 1. A catalyst precursor comprising at least two Group 8-10 base metals, at least one Group 6 metal, and a dispersion agent supported on a support comprising a zeolitic framework structure having a 10-member ring as a largest pore channel, the catalyst precursor having a molar ratio of a first Group 8-10 base metal to a second Group 8-10 base metal of 0.1 to 10, a molar ratio of the at least two Group 8-10 base metals to the at least one Group 6 metal of 0.1 to 1.0, and a molar ratio of dispersion agent to the at least two Group 8-10 base metals and the at least one Group 6 metal of 0.5 to 3.0. 2. The catalyst precursor of claim 1 , wherein the zeolitic framework structure comprises ZSM-48, ZSM-11, an MEL framework structure, an MRE framework structure, or a combination thereof. 3. The catalyst precursor of claim 2 , wherein the zeolitic framework structure comprises an MEL framework structure, the zeolitic framework structure further comprising a) a molar ratio of silica to alumina of about 35 to about 55; b) an alpha value of at least about 380; c) a total surface area of at least about 350 m 2 /g, or d) a combination thereof. 4. The catalyst precursor of claim 1 , wherein the catalyst precursor comprises about 2.0 wt % to about 30 wt % of the at least one Group 6 metal and at least two Group 8-10 base metals based on a weight of the catalyst precursor, the at least two Group 8-10 base metals optionally comprising Ni and Co, the at least one Group 6 metal optionally comprising W, Mo, or a combination thereof. 5. The catalyst precursor of claim 1 , wherein the dispersion agent comprises a compound having 2-10 carbon atoms and a carbon atom to oxygen atom ratio of about 0.6 to about 2.0. 6. The catalyst precursor of claim 1 , wherein the dispersion agent comprises a glycol, a carboxylic acid, or a combination thereof. 7. The catalyst precursor of claim 1 , wherein the dispersion agent comprises citric acid, gluconic acid, nitrilotriacetic acid, ethylene glycol, or a combination thereof. 8. The catalyst precursor of claim 1 , wherein the support further comprises an alumina binder, the alumina binder optionally having a surface area of about 150 m 2 /g or less.
containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
Lubricating oil · CPC title
Sulfiding · CPC title
Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst · CPC title
in combination with chromium, molybdenum or tungsten metal, or compounds thereof · CPC title
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