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Systems, methods, and catalysts for producing a crude product

a technology of crude feed and catalysts, applied in the direction of metal/metal-oxide/metal-hydroxide catalysts, hydrocarbon oil cracking, physical/chemical process catalysts, etc., can solve the problems of high tan, high cost of corrosion-resistant metal, and inability to use corrosion-resistant metal in existing equipmen

Inactive Publication Date: 2006-10-19
SHELL OIL CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent describes a method of producing a crude product by contacting a crude feed with one or more catalysts. The catalysts used in the process have a specific pore size distribution and a specific pore volume, which helps to reduce the amount of residual micro-carbon residue (MCR) in the crude product. The MCR content of the crude product is controlled by controlling the contacting conditions. The method can also involve using a specific column of metals or compounds from columns 6-10 of the periodic Table. The resulting crude product has a reduced MCR content compared to the original crude feed. The technical effect of this patent is to provide a more efficient and effective method for producing crude products with reduced MCR content.

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 high levels of residue tend to be difficult and expensive to transport and / or process using conventional facilities.
Organically bound heteroatoms may, in some situations, have an adverse effect on catalysts used to process disadvantaged crudes.
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.
Disadvantaged crudes may have components that contribute coke and / or to thermal degradation of the disadvantaged crude.
It may be costly to regenerate the catalytic activity of a catalyst contaminated with coke and / or thermally degraded crude.
Additionally, high temperatures used during regeneration of a catalyst may also diminish the activity of the catalyst and / or cause the catalyst to deteriorate.
Problems are often encountered in conventional catalytic processing of crudes when metals in metal salts of organic acids are present.
Moreover, the metals in metal salts of organic acids may cause rapid deactivation of 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.
When processing 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).
Removal of these components, however, may cause instability in the crude, thus causing separation of the crude during transportation.
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.
The processes, systems, and catalysts described in these patents, however, have limited applicability because of many of the technical problems set forth above.
In sum, disadvantaged crudes generally have undesirable properties (for example, relatively high TAN, a tendency to become unstable during treatment, and / or a tendency to consume relatively large amounts of hydrogen during treatment).
Disadvantaged crudes may also include relatively high amounts of undesirable components (for example, components that contribute to thermal degradation, residue, organically bound heteroatoms, metal contaminants, metals in metal salts of organic acids, and / or organic oxygen compounds).
Such properties and components 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, methods, and catalysts for producing a crude product
  • Systems, methods, and catalysts for producing a crude product
  • Systems, methods, and catalysts for producing a crude product

Examples

Experimental program
Comparison scheme
Effect test

example 1

Preparation of a Catalyst Support

[0218] 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 mm die plate, heat-treated between 90° C. and about 125° C., and further heat-treated at 918° C., which resulted in 650 grams of a support with a median pore diameter of 182 Å. The heat-treated support was placed in a Lindberg furnace. The furnace temperature was raised to about 1000° C. to about 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 por...

example 2

Preparation of a Molybdenum Catalyst Containing Theta Alumina

[0220] A molybdenum catalyst was prepared in the following manner. The alumina support prepared by the method described in Example 1 was combined 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 the solids dissolved, and then cooled to room temperature. The pH of the solution was 5.36. The solution volume was adjusted to 82 mL with deionized water.

[0221] The alumina support (100 grams) was combined with the molybdenum impregnation solution, aged for 2 hours with occasional agitation, heat-treated at 125° C. for several hours, and then heat-treated at 480° C. for 2 hours. The resulting catalyst contained 0.04 grams of molybdenum per gram of catalyst, with the balance bei...

example 3

Preparation of a Molybdenum / Vanadium Catalyst Containing Theta Alumina

[0223] A molybdenum / vanadium catalyst was prepared in the following manner. The alumina support, prepared by the method described in Example 1, was impregnated with a molybdenum / vanadium impregnation solution prepared as follows. A first solution was made by combining 2.14 grams of (NH4)2Mo2O7, 3.21 grams of MoO3, 0.56 grams of 30% H2O2, 0.14 grams of MEA, and 3.28 grams of deionized water to form a slurry. The slurry was heated to 65° C. until solids dissolved, and then cooled to room temperature.

[0224] A second solution was made by combining 3.57 grams of VOSO4.xH2O (x=3 to 5) with 40 grams of deionized water. The first solution and second solution were combined and sufficient deionized water was added to bring the combined solution volume up to 82 mL to yield the molybdenum / vanadium impregnation solution. The alumina was impregnated with the molybdenum / vanadium impregnation solution, aged for 2 hours with occ...

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Abstract

Methods and systems for contacting of a crude feed with one or more catalysts to produce a total product that includes a crude product are described. The crude product is a liquid mixture at 25° C. and 0.101 MPa. The crude product may have a total content of alkali metal and alkaline-earth metal in metal salts of organic acids of at most 90% of the total content of alkali metal and alkaline-earth metal in metal salts of organic acids of the crude feed. One or more other properties of the crude product may be changed by at least 10% relative to the respective properties of the crude feed.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS [0001] This application claims priority to U.S. Provisional Application 60 / 670,147 filed on Apr. 11, 2005, herein incorporated by reference in its entirety.FIELD OF THE INVENTION [0002] The present invention generally relates to systems, methods, and catalysts for treating crude feed. More particularly, certain embodiments described herein relate to systems, methods, and catalysts for conversion of a crude 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 crude 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 facilities, are commonly referred to as “disadvantaged crudes”. [0004] Disadvantaged crudes may include acidic components that contribute to...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10G71/00
CPCC10G45/00C10G45/04C10G45/08C10G65/04C10G47/12C10G49/04C10G47/10C10G71/00
Inventor BHAN, OPINDER KISHAN
Owner SHELL OIL CO
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