Process for recovering ultrafine solids from a hydrocarbon liquid

• US 7,955,497 B2
• Filed: 01/21/2010
• Issued: 06/07/2011
• Est. Priority Date: 12/29/2006
• Status: Active Grant

• Current Assignee: Chevron USA Incorporated (Chevron Corp.)
• Original Assignee: Chevron USA Incorporated (Chevron Corp.)
• Inventors: Abulnaga, Baha E., Lindsay, Sara Ouzts, Guitian, Jose
• Primary Examiner(s): Griffin; Walter D
• Assistant Examiner(s): MCCAIG, BRIAN A
• Application Number:
  US12/691,422
• Publication Number:
  US 20100122938A1
• Time in Patent Office: 502 Days
• Field of Search: 208107-112, 208/146, 208/153, 208155-156, 208161-162
• US Class Current: 208/161
• CPC Class Codes: C10G 21/003 Solvent de-asphalting
• CPC Class Codes: C10G 2300/1033 Oil well production fluids
• CPC Class Codes: C10G 2300/1062 Lubricating oils
• CPC Class Codes: C10G 2300/1077 Vacuum residues
• CPC Class Codes: C10G 2300/201 Impurities
• CPC Class Codes: C10G 2300/206 Asphaltenes
• CPC Class Codes: C10G 2300/44 Solvents
• CPC Class Codes: C10G 2300/701 Use of spent catalysts
• CPC Class Codes: C10G 31/00 Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by distillation C10G7/00
• CPC Class Codes: C10G 31/10 with the aid of centrifugal force
• CPC Class Codes: C10G 67/0454 Solvent desasphalting

Abstract

A method for separating and recovering ultrafine particulate solid material from a suspension or slurry of the solid material and a hydrocarbon liquid by precipitation or flocculation of a heavy fraction of the hydrocarbon liquid with an effective amount of a precipitation or flocculation agent such that the precipitated heavy fraction encapsulates the particulate solid material. The method further comprises coking the precipitated heavy fraction and grinding the coked product to an ultrafine size.

Claims

1. A process for separating a particulate solid material from a hydrocarbon liquid comprising the following steps:

a) providing a bleed slurry comprising the hydrocarbon liquid and the solid material,

b) adding a heavy hydrocarbon liquid to the bleed slurry in an amount sufficient to increase the asphaltene content of the bleed slurry to at least 2.5 weight percent and mixing the bleed slurry in a flocculant and to form a first mixture comprising the hydrocarbon liquid, a first solvent and a flocculent containing the solid material,

c) separating the first mixture to form a second mixture and a third mixture, wherein the second mixture contains a low concentration of the flocculent and the third mixture contains a high concentration of the flocculent,

d) separating the second mixture to form a fourth mixture comprising the first solvent and the hydrocarbon liquid and a fifth mixture containing a high concentration of the flocculent,

e) combining the third mixture and the fifth mixture in a feed tank to form a final mixture comprising a high concentration of the flocculent, a low concentration of the first solvent and a low concentration of the hydrocarbon liquid,

f) drying the final mixture to form a hydrocarbon vapor mixture and a coked material wherein the hydrocarbon vapor comprises the solvent, a light fraction of the hydrocarbon liquid and entrained amounts of the solid material and wherein the coked material comprises the solid material and a heavy fraction of the hydrocarbon liquid,

g) recovering the coked material from the drying device, wherein the solid material is free of liquid hydrocarbons and comprises a catalyst and wherein the catalyst comprises a major amount of a spent catalyst and a minor amount of an active catalyst,

h) thermally shocking the coked solid material to disagglomerate and form an aqueous slurry of the coked solid material and grinding the slurry of the coked material to reduce the particle size of the coked solid material to between about 10 to 60 μ

m.

2. The process of claim 1, wherein the first solvent is an asphaltene flocculant and is selected from the group consisting of naphtha, heavy naphtha, light naptha, hexane and heptane.

3. The process of claim 1, wherein the first solvent is selected to promote the precipitation of asphaltenes.

4. The process of claim 1, wherein the step c) further comprises adding the bleed slurry to one or more mixing tanks.

5. The process of claim 4, wherein the one or more mixing tanks are connected to a means for controlling the temperature of the bleed slurry.

6. The process of claim 1, wherein the separating of the first mixture is via a first centrifuge.

7. The process of claim 6, wherein the separating of the second mixture is via a second centrifuge.

8. The process of claim 7, wherein first centrifuge is a horizontal decanter centrifuge and the second centrifuge is a vertical centrifuge.

9. The process of claim 1 wherein the flocculent of step c) is asphaltene.

10. The process of claim 1 wherein step c) further comprises mixing the bleed slurry and the first solvent for a period of time sufficient to allow the flocculent to form.

11. The process of claim 10, wherein the period of time is about 15 minutes to one hour.

12. The process of claim 1, wherein the first mixture of step c) comprises a solvent to bleed slurry mass ratio of about 3:

1 to about 1;

3.

13. The process of claim 1, wherein the first mixture is maintained at a temperature between about 60°

C. and 70°

C.

14. The process of claim 1, further comprising recovering the hydrocarbon vapor mixture from the drying device and separating the entrained amounts of the solid material, the solvent and the light fraction of the hydrocarbon liquid by means of a system of one or more condensers and one or more oil recovery columns.

15. The process of claim 1, wherein drying the final mixture is via a drying device selected from the group consisting of an indirect fired kiln, and indirect fired rotary kiln, an indirect fired dryer, an indirect fired rotary dryer, vacuum dryer and a flexicoker.

16. The process of claim 1, further comprising calcining the final mixture to a temperature between about 350°

C. to 550°

C.

17. A process for separating a particulate solid material from a hydrocarbon liquid comprising the following steps:

a) providing a bleed slurry feed comprising the hydrocarbon liquid and the solid material comprising a catalyst, wherein the mass concentration of the bleed slurry feed comprises from 15 to 40% of the solid material comprising a catalyst and wherein the bleed slurry feed is provided at a temperature between 55°

C. and 75°

C.,

b) mixing the bleed slurry feed in a flocculant for at least 15 minutes to form a first mixture comprising the hydrocarbon liquid, a first solvent and a flocculent containing the solid material,

c) separating the first mixture to recover a second mixture and a final mixture, wherein the second mixture contains a low concentration of the flocculent and the final mixture contains a high concentration of the flocculent with up to 90% of the solid material in the bleed slurry feed,

d) drying the final mixture to form a hydrocarbon vapor mixture and a coked material wherein the hydrocarbon vapor comprises the solvent, a light fraction of the hydrocarbon liquid and entrained amounts of the solid material and wherein the coked material comprises the solid material and a heavy fraction of the hydrocarbon liquid.