US2007000808A1PendingUtilityA1
Method and catalyst for producing a crude product having selected properties
Individually held — no corporate assignee on recordPriority: Dec 19, 2003Filed: Jun 22, 2006Published: Jan 4, 2007
Est. expiryDec 19, 2023(expired)· nominal 20-yr term from priority
C10G 47/12C10G 11/02C10G 47/14C10G 45/10C10G 2300/304C10G 29/06C10G 69/00C10G 2300/1033C10G 11/08C10G 11/04C10G 45/04C10G 47/02C10G 2300/302C10G 45/08C10G 47/04C10G 2300/301C10G 2300/107C10G 47/26C10G 45/16
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Claims
Abstract
A catalyst that one or more metals from Columns 6-10 of the Periodic Table and/or one or more compounds of one or more metals from Columns 6-10 of the Periodic Table is described. The catalyst exhibits one or more bands in a range from 800 cm −1 to 900 cm −1 , as determined by Raman Spectroscopy. Methods of contacting a crude feed with hydrogen with the catalyst to produce a crude product having selected properties are also described.
Claims
exact text as granted — not AI-modified1 . A catalyst composition, comprising one or more metals from Columns 6-10 of the Periodic Table and/or one or more compounds of one or more metals from Columns 6-10 of the Periodic Table, wherein the catalyst exhibits one or more bands in a range from 800 cm −1 to 900 cm −1 , as determined by Raman Spectroscopy.
2 . The catalyst of claim 1 , wherein the catalyst has a pore size distribution with a median pore diameter of at least 180 Å.
3 . The catalyst of claim 1 , wherein the catalyst has a pore size distribution with a median pore diameter of at least 230 Å.
4 . The catalyst of claim 1 , wherein at least one of the Column 6-10 metals is molybdenum.
5 . The catalyst of claim 1 , wherein at least one of the bands is near 810 cm −1 .
6 . The catalyst of claim 1 , wherein at least one of the bands is near 835 cm −1 .
7 . The catalyst of claim 1 , wherein at least one of the bands is near 880 cm −1 .
8 . The catalyst of claim 1 , wherein the catalyst is a supported catalyst, and wherein the support comprises alumina, silica, silica-alumina, titanium oxide, zirconium oxide, magnesium oxide, or mixtures thereof.
9 . The catalyst of claim 1 , wherein the catalyst is a supported catalyst, and wherein the support comprises theta alumina, wherein a content of the theta alumina is at least 0.5 grams per gram of total catalyst.
10 . The catalyst of claim 1 , further comprising one or more elements or one or more compounds of one or more elements from Column 15 of the Periodic Table.
11 . A method of producing a crude product, comprising:
contacting a crude feed with one or more catalysts to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25° C. and 0.101 MPa, the crude feed having a residue content at least 0.1 grams of residue per gram of crude feed, at least one of the catalysts exhibits one or more bands between 800 cm −1 to 900 cm −1 , as determined by Raman Spectroscopy, and the catalyst exhibiting the bands comprising one or more metals from Columns 6-10 of the Periodic Table and/or one or more compounds of one or more metals from Columns 6-10 of the Periodic Table; and controlling contacting conditions such that the crude product has a residue content of at most 90% of the residue content of the crude feed, wherein residue content is as determined by ASTM Method D5307.
12 . The method of claim 11 , wherein the residue content of the crude feed is at most 50% of the residue content of the crude feed.
13 . The method of claim 11 , wherein the crude product has a residue content ranging from about 0.00001 grams to about 0.3 grams per gram of crude product.
14 . The method of claim 11 , wherein the crude product has a residue content ranging from about 0.0001 grams to about 0.2 grams per gram of crude product.
15 . The method of claim 11 , wherein one of the bands exhibited by the catalyst is near 810 cm −1 .
16 . The method of claim 11 , wherein one of the bands exhibited by the catalyst is near 835 cm −1 .
17 . The method of claim 11 , wherein one of the bands exhibited by the catalyst is near 880 cm −1 .
18 . The method of claim 11 , wherein the catalyst is a supported catalyst, and wherein the support comprises alumina, silica, silica-alumina, titanium oxide, zirconium oxide, magnesium oxide, or mixtures thereof.
19 . A method of producing a crude product, comprising:
contacting a crude feed with one or more catalysts to produce a total product that includes the crude product, wherein the crude product is a liquid mixture at 25° C. and 0.101 MPa, the crude feed having a TAN of at least 0.1, at least one of the catalysts exhibits one or more bands between 800 cm −1 to 900 cm −1 , as determined by Raman Spectroscopy, and the catalyst exhibiting the bands comprising one or more metals from Columns 6-10 of the Periodic Table and/or one or more compounds of one or more metals from Columns 6-10 of the Periodic Table; and controlling contacting conditions such that the crude product has a TAN of at most 90% of the TAN of the crude feed, wherein TAN is as determined by ASTM D664.
20 . The method of claim 19 , wherein the TAN of the crude feed is at least 1.
21 . The method of claim 19 , wherein the crude product has a TAN ranging from 0.001 to about 0.5.
22 . The method of claim 19 , wherein the crude product has a TAN ranging from 0.005 to about 1.
23 . The method of claim 19 , wherein one of the bands exhibited by the catalyst is near 810 cm −1 .
24 . The method of claim 19 , wherein one of the bands exhibited by the catalyst is near 835 cm −1 .
25 . The method of claim 19 , wherein one of the bands exhibited by the catalyst is near 880 cm −1 .
26 . The method of claim 19 , wherein the catalyst is a supported catalyst, and wherein the support comprises alumina, silica, silica-alumina, titanium oxide, zirconium oxide, magnesium oxide, or mixtures thereof.
27 . The method of claim 19 , wherein the crude feed has, per gram of crude feed, a total content of alkali metal and alkaline-earth metal in metal salts of organic acids of at least 0.00001 grams and the crude product has a total content of alkali metal and alkaline-earth metal in metal salts of organic acids of at most 90% of the content of alkali metal, and alkaline-earth metal, in metal salts of organic acids in the crude feed.
28 . The method of claim 27 , wherein one or more of the metals is calcium, potassium, sodium, magnesium, lithium, or combinations thereof.
29 . The method of claim 19 , wherein the crude feed has a content of Columns 5-12 metals in metal salts of organic acids, and the crude product has a content of Columns 5-12 metals in metal salts of organic acids of at most 90% of the content of Columns 5-12 metals in metal salts of organic acids of the crude feed.
30 . The method of claim 29 , wherein one or more of the metals is vanadium, molybdenum, chromium, iron, nickel, zinc, or combinations thereof.
31 . The method of claim 19 , wherein the crude feed comprises silicon, and the crude product has a content of silicon of at most 90% of the content of the silicon of the crude feed.
32 . The method of claim 19 , wherein the crude feed has a viscosity of at least 10 cSt at 37.8° C. (100° F.) and the contacting conditions are controlled such that the crude product has a viscosity at 37.8° C. of at most 90% of the viscosity of the crude feed at 37.8° C.Join the waitlist — get patent alerts
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