Method for producing a crude product with reduced tan

Abstract

Contacting a crude feed with one or more catalysts to produce a total product that includes the crude product is described. The crude feed has a TAN of at least 1. At least one of the catalysts includes 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. Contacting conditions are controlled contacting such that the crude product has a TAN from about 0.001 to about 0.5.

Description

PRIORITY [0001] This application claims priority to U.S. patent application Ser. No. 11 / 014,335 entitled “SYSTEMS, METHODS, AND CATALYSTS FOR PRODUCING A CRUDE PRODUCT” filed on Dec. 16, 2004 which claims priority to U.S. Provisional Patent Application No. 60 / 531,506 filed on Dec. 19, 2003 and to U.S. Provisional Patent Application No. 60 / 618,681 filed on Oct. 14, 2004FIELD OF THE INVENTION [0002] The present invention generally relates to systems, methods, and catalysts for treating crude feed, 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 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 m...

AI Technical Summary

Benefits of technology

[0023] In some embodiments, the invention describes 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 1, at least one of the catalysts 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 from about 0.001 to about 0.5, wherein TAN is as determined by ASTM D664.

[0024] In some embodiments, the invention describes a catalyst composition comprising one or more metals from Column 5 of the Periodic Table and/or one or more compounds of one or more metals from Column 5 of the Periodic Table, wherein the catalyst exhibits one or more bands in a range from 650 cm−1 to 1000 cm−1, as determined by Raman Spectroscopy.

[0025] In some embodiments, the invention describes 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, at least one of the catalysts exhibits one or more bands in a range from 650 cm−1 to 1000 cm−1, as determined by Raman Spectroscopy, and the catalyst exhibiting the bands comprising one or more metals from Column 5 of the Periodic Table and/or one or more compounds of one or more metals from Column 5 of the Periodic Table; and controlling contacting conditions such that an atomic hydrogen/carbon (H/C) of the crude product is between 80% and 120% of the atomic H/C of the crude feed.

[0026] In some embodiments, the invention describes a catalyst composition, comprising one or more metals from Columns 6-10 of

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.

Such 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.

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.

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 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 TAN, 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.

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