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Systems and methods for producing a crude product and compositions thereof

a crude product and crude product technology, applied in the field of systems, methods, catalysts for treating hydrocarbon feeds, can solve the problems of high tan that may contribute to the corrosion of metal components, the use of corrosion-resistant metal in existing equipment may not be desirable, and the high cost of corrosion-resistant metals

Inactive Publication Date: 2008-04-17
SHELL OIL CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent describes methods for converting hydrocarbon feeds to crude products using catalysts. The methods involve contacting the hydrocarbon feed with one or more catalysts in a fixed bed reactor to produce a total product that includes the crude product. The crude product has a specific composition and viscosity. The methods can also involve controlling contacting conditions, such as temperature, pressure, and space velocity, to optimize the conversion process. The invention also describes the use of specific catalysts and compounds of metals from columns 6-10 of the Periodic Table. Overall, the patent provides technical means for efficiently producing crude products with desired properties.

Problems solved by technology

Disadvantaged crudes with a relatively high TAN may contribute to corrosion of metal components during transporting and / or processing of the disadvantaged crudes.
The use of corrosion-resistant metal often involves significant expense, and thus, the use of corrosion-resistant metal in existing equipment may not be desirable.
The use of corrosion inhibitors may negatively affect equipment used to process the crudes and / or the quality of products produced from the crudes.
Disadvantaged crudes often contain relatively high levels of residue.
Disadvantaged crudes having such high levels of residue tend to be difficult and expensive to transport and / or process using conventional facilities.
During processing of such crudes, metal contaminants and / or compounds of metal contaminants, may deposit on a surface of the catalyst or in the void volume of the catalyst.
Such deposits may cause a decline in the activity of the catalyst.
It may be costly to regenerate the catalytic activity of a catalyst contaminated with coke.
High temperatures used during regeneration may also diminish the activity of the catalyst and / or cause the catalyst to deteriorate.
Moreover, the metals in metal salts of organic acids may cause rapid deactivation of catalysts.
Organically bound heteroatoms may, in some situations, have an adverse effect on catalysts.
Treatment facilities that process disadvantaged crudes with an oxygen content of at least 0.002 grams of oxygen per gram of disadvantaged crude may encounter problems during processing.
Organic oxygen compounds, when heated during processing, may form higher oxidation compounds (for example, ketones and / or acids formed by oxidation of alcohols, and / or acids formed by oxidation of ethers) that are difficult to remove from the treated crude and / or may corrode / contaminate equipment during processing and cause plugging in transportation lines.
Basic nitrogen compounds may have adverse effects on catalysts used in cracking processes, thus reducing the efficiency of the cracking operation.
When processing of hydrogen deficient hydrocarbons, consistent quantities of hydrogen generally need to be added, particularly if unsaturated fragments resulting from cracking processes are produced.
Hydrogen is costly to produce and / or costly to transport to treatment facilities.
Disadvantaged crudes also tend to exhibit instability during processing in conventional facilities.
Crude instability tends to result in phase separation of components during processing and / or formation of undesirable by-products (for example, hydrogen sulfide, water, and carbon dioxide).
Conventional processes often lack the ability to change a selected property in a disadvantaged crude without also significantly changing other properties in the disadvantaged crude.
For example, conventional processes often lack the ability to significantly reduce TAN in a disadvantaged crude while, at the same time, only changing by a desired amount the content of certain components (such as sulfur or metal contaminants) in the disadvantaged crude.
Adding diluent, however, generally increases costs of treating disadvantaged crudes due to the costs of diluent and / or increased costs to handle the disadvantaged crudes.
Addition of diluent to a disadvantaged crude may, in some situations, decrease stability of such crude.
In sum, disadvantaged crudes generally have undesirable properties (for example, relatively high residue content, a tendency to become unstable during treatment, and / or a tendency to consume relatively large amounts of hydrogen during treatment).
Other undesirable properties include relatively high amounts of undesirable components (for example, residue, organically bound heteroatoms, metal contaminants, metals in metal salts of organic acids, and / or organic oxygen compounds).
Such properties tend to cause problems in conventional transportation and / or treatment facilities, including increased corrosion, decreased catalyst life, process plugging, and / or increased usage of hydrogen during treatment.

Method used

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  • Systems and methods for producing a crude product and compositions thereof
  • Systems and methods for producing a crude product and compositions thereof
  • Systems and methods for producing a crude product and compositions thereof

Examples

Experimental program
Comparison scheme
Effect test

example 1

Preparation of a Catalyst Support

[0268] A support was prepared by mulling 576 grams of alumina (Criterion Catalysts and Technologies LP, Michigan City, Mich., U.S.A.) with 585 grams of water and 8 grams of glacial nitric acid for 35 minutes. The resulting mulled mixture was extruded through a 1.3 Trilobe™ die plate, dried between 90 and 125° C., and then calcined at 918° C., which resulted in 650 grams of a calcined support with a median pore diameter of 182 Å. The calcined support was placed in a Lindberg furnace. The furnace temperature was raised to 1000-1100° C. over 1.5 hours, and then held in this range for 2 hours to produce the support. The support included, per gram of support, 0.0003 grams of gamma alumina, 0.0008 grams of alpha alumina, 0.0208 grams of delta alumina, and 0.9781 grams of theta alumina, as determined by x-ray diffraction. The support had a surface area of 110 m2 / g and a total pore volume of 0.821 cm3 / g. The support had a pore size distribution with a media...

example 2

Preparation of a Vanadium Catalyst Having a Pore Size Distribution with a Median Pore Diameter of at Least 230 Å

[0270] The vanadium catalyst was prepared in the following manner. The alumina support, prepared by the method described in Example 1, was impregnated with a vanadium impregnation solution prepared by combining 7.69 grams of VOSO4 with 82 grams of deionized water. A pH of the solution was 2.27.

[0271] The alumina support (100 g) was impregnated with the vanadium impregnation solution, aged for 2 hours with occasional agitation, dried at 125° C. for several hours, and then calcined at 480° C. for 2 hours. The resulting catalyst contained 0.04 grams of vanadium, per gram of catalyst, with the balance being support. The vanadium catalyst had a pore size distribution with a median pore diameter of 350 Å, a pore volume of 0.69 cm3 / g, and a surface area of 110 m2 / g. Additionally, 66.7% of the total number of pores in the pore size distribution of the vanadium catalyst had a pore...

example 3

Preparation of a Molybdenum Catalyst Having a Pore Size Distribution with a Median Pore Diameter of at Least 230 Å

[0273] The molybdenum catalyst was prepared in the following manner. The alumina support prepared by the method described in Example 1 was impregnated with a molybdenum impregnation solution. The molybdenum impregnation solution was prepared by combining 4.26 grams of (NH4)2Mo2O7, 6.38 grams of MoO3, 1.12 grams of 30% H2O2, 0.27 grams of monoethanolamine (MEA), and 6.51 grams of deionized water to form a slurry. The slurry was heated to 65° C. until dissolution of the solids. The heated solution was cooled to room temperature. The pH of the solution was 5.36. The solution volume was adjusted to 82 mL with deionized water.

[0274] The alumina support (100 grams) was impregnated with the molybdenum impregnation solution, aged for 2 hours with occasional agitation, dried at 125° C. for several hours, and then calcined at 480° C. for 2 hours. The resulting catalyst contained ...

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Abstract

Systems and methods for producing a crude product are described herein. Systems include an upstream contacting zone and a downstream contacting zone coupled to the upstream contacting zone. The upstream contacting zone and the downstream contacting zone include one or more catalysts. Contact of a hydrocarbon feed with the one or more of the catalysts produces a hydrocarbon feed / total product mixture having a molybdenum content of at most 90% of the molybdenum of the hydrocarbon feed. Contact of the hydrocarbon feed / total product mixture in downstream with one or more downstream catalysts produces a crude product having a molybdenum content of at most 90% of the molybdenum content of the hydrocarbon feed and at most 90% of the residue content of the hydrocarbon feed. Methods of producing a crude product using said systems are described herein. Compositions of said crude product produced from said systems and methods are described herein.

Description

RELATED APPLICATION [0001] The present application claims the benefit of the filing date of U.S. Provisional patent application Ser. No. 60 / 850,109 filed Oct. 6, 2006, the disclosure of which is incorporated herein by reference.FIELD OF THE INVENTION [0002] The present invention generally relates to systems, methods, and catalysts for treating hydrocarbon feeds, and to compositions that can be produced using such systems, methods, and catalysts. More particularly, certain embodiments described herein relate to systems, methods, and catalysts for conversion of a hydrocarbon feed to a total product, wherein the total product includes a crude product that is a liquid mixture at 25° C. and 0.101 MPa and has one or more properties that are changed relative to the respective property of the hydrocarbon feed. DESCRIPTION OF RELATED ART [0003] Crudes that have one or more unsuitable properties that do not allow the crudes to be economically transported, or processed using conventional facil...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10G51/04B01J8/00B01J35/00
CPCB01J21/04C10G2300/4012B01J23/28B01J23/882B01J23/883B01J35/002B01J35/1019B01J35/1042B01J35/1061B01J35/108B01J37/0009B01J37/0203C10G45/04C10G45/08C10G47/00C10G47/10C10G47/12C10G49/04C10G65/12C10G2300/4018C10G2300/206C10G2300/208C10G2300/302C10G2300/308C10G2300/4006B01J23/22B01J35/66B01J35/635B01J35/615B01J35/647B01J35/70B01J2235/30B01J35/37B01J2235/15B01J2235/00B01J23/88C10G45/06C10G45/12C10G69/02B01J35/30
Inventor BHAN, OPINDER KISHANWELLINGTON, SCOTT LEE
Owner SHELL OIL CO
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