Solvent-assisted delayed coking process

• US 8,894,841 B2
• Filed: 06/11/2012
• Issued: 11/25/2014
• Est. Priority Date: 07/29/2011
• Status: Active Grant

• Current Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Original Assignee: Saudi Arabian Oil Company (Government of Saudi Arabia)
• Inventors: Koseoglu, Omer Refa
• Primary Examiner(s): Boyer, Randy
• Assistant Examiner(s): VALENCIA, JUAN C
• Application Number:
  US13/493,635
• Publication Number:
  US 20130026069A1
• Time in Patent Office: 897 Days
• Field of Search: 208390-391, 208/87
• US Class Current: 208/87
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: C10B 57/045 containing mineral oils, bitumen, tar or the like or mixtures thereof
• CPC Class Codes: C10G 9/005 Coking (in order to produce liquid products mainly)

Abstract

An improved process for the delayed coking of a heavy residual hydrocarbon feedstock to reduce the coking induction period and to enhance the coking process relative to the processes of the prior art is achieved by mixing a sufficient volume of a paraffinic solvent having the formula C_nH_2n+2, where n=3 to 8 with the heavy feedstock to disturb the equilibrium of asphaltenes in the solution of maltenes in order to flocculate substantially all of the solid asphaltenes particles to thereby increase the yield and quality of valuable liquid products and minimize undesirable cracking reactions that result in high molecular weight polymers and the formation of coke.

Claims

1. A delayed coking process for use in a delayed coking unit that includes at least one drum, the coking unit producing a delayed coking unit product stream and a coke product that is retained in the drum, the coking unit product stream being introduced into a coking product stream fractionator to produce at least a bottoms fraction, an intermediate fraction and a light naphtha fraction, the process comprising:

a. analyzing a sample of fresh heavy hydrocarbon feedstock containing asphaltenes that is to be subjected to the delayed coking process to determine the paraffinic solvent-to-asphaltenes ratio required to flocculate substantially all of the asphaltenes in the feedstock;

b. introducing the fresh heavy hydrocarbon feedstock containing asphaltenes for preheating into the lower portion of the coking product stream fractionator;

c. discharging the bottoms fraction that includes the preheated fresh hydrocarbon feedstock from the fractionator as a coking unit combined feedstream;

d. introducing a paraffinic solvent having the formula C_nH_2n+2, where n can be from 3 to 8 or a combined paraffinic and olefinic solvent, the latter having the formula C_nH_2n, where n can be from 3 to 8, into the coking unit combined feedstream with a sufficient ratio of solvent-to-feedstream to solvent-flocculate substantially all of the asphaltenes in the coking unit combined feedstream, the solvent being introduced after the discharge of the coking unit combined feedstream from the coking product fractionator and prior to passing the combined coking unit feedstream to the delayed coking drum;

e. introducing the coking unit combined feedstream which contains asphaltenes into the coking unit furnace for heating to a predetermined coking temperature; and

f. passing the heated combined feedstream containing solvent-flocculated asphaltenes and paraffinic solvent to the delayed coking drum to produce the delayed coking product stream having an increased portion of liquids and depositing a reduced amount of coke on the interior of the drum, as compared to the amount of coke deposited in the absence of the addition of the paraffinic solvent to the same heavy hydrocarbon feedstock.

2. The process of claim 1 in which the ratio of solvent-to-feedstream is from 0.1:

1 to 10;

1 by volume.

3. The delayed coking process of claim 1, wherein the paraffinic solvent has an initial boiling point of up to 80°

C.

4. The delayed coking process of claim 1, wherein at least a portion of a light naphtha fraction having a boiling point less than 80°

C. and substantially free of aromatic compounds recovered from the coking product fractionator is introduced into the coking unit combined feedstream.

5. The delayed coking process of claim 4, wherein the light naphtha stream withdrawn from the fractionator and introduced into the coking unit combined feedstream includes a mixture of alkanes and alkenes.

6. The delayed coking process of claim 4, wherein a light gas oil is recovered from the fractionator as a separate stream with the light naphtha stream.

7. The delayed coking process of claim 1, wherein the paraffinic or combined paraffinic olefinic solvent is introduced into the coking unit combined feedstream in a solvent mixing zone intermediate the coking product fractionator and the coking unit furnace.

8. The delayed coking process of claim 1, wherein the paraffinic or combined paraffinic olefinic solvent is introduced into the coking unit combined feedstream in a solvent mixing zone intermediate the coking unit furnace and the coking drum.

9. The delayed coking process of claim 1, wherein the paraffinic or combined paraffinic olefinic solvent is injected into the coking unit combined feedstream prior to the coking drum.

10. The delayed coking process of claim 1, wherein step (d) includes heating the coking unit combined feedstream to a temperature in the range of from 480°

C. to 530°

C. at a pressure in the range of from 1 to 20 bars.

11. The delayed coking process of claim 10, wherein the pressure is in the range of from 1 to 10 bars.

12. The delayed coking process of claim 10, wherein the pressure is in the range of from 1 to 7 bars.

13. The delayed coking process of claim 1, wherein the heavy hydrocarbon feedstock is an unrefined hydrocarbon source selected from the group consisting of crude oil, bitumen, tar sands, shale oils, coal liquefaction liquids, and combinations thereof.

14. The delayed coking process of claim 1, wherein the heavy hydrocarbon feedstock is derived from a refined hydrocarbon source selected from the group consisting of atmospheric residue, vacuum residue, visbreaker products, fluid catalytic cracking products or by-products, and combinations thereof.

15. The delayed coking process of claim 1, wherein the heavy hydrocarbon feedstock is a mixture having a boiling point between 36°

C. and 2000°

C.

16. The delayed coking process of claim 1 in which the coking unit includes two drums and the process is operated in swing mode.

17. The delayed coking process of claim 1, where in the coking cycle is reduced by at least 30%.

18. A delayed coking process for use in a delayed coking unit that includes at least one drum, the coking unit producing a delayed coking product stream and a coke product that is retained in the drum, the coking product stream being introduced into a coking product stream fractionator to produce at least a bottoms fraction, an intermediate fraction and a light naphtha fraction, the process comprising:

a. analyzing a sample of fresh heavy hydrocarbon feedstock containing asphaltenes that is to be subjected to the delayed coking process to determine the paraffinic solvent-to-asphaltenes ratio required to flocculate substantially all of the asphaltenes;

b. introducing the fresh heavy hydrocarbon feedstock containing asphaltenes for preheating into the lower portion of the coking product fractionator;

c. discharging the bottoms fraction that includes the preheated fresh hydrocarbon feedstock from the fractionator as a coking unit combined feedstream;

d. introducing the coking unit combined feedstream into the coking unit furnace for heating to a predetermined coking temperature;

e. mixing a paraffinic solvent having the formula C_nH_2n+2, where n=3 to 8, with the furnace-heated coking unit combined feedstream in a ratio of solvent-to-feedstream of from 0.1;

1 to 10;

1 by volume to form solvent-flocculated asphaltenes in the furnace heated coking unit combined feedstream;

f. passing the furnace-heated coking unit combined feedstream containing the solvent-flocculated asphaltenes and paraffinic solvent to the delayed coking drum to produce the delayed coking unit product stream having an increased portion of liquids and depositing a reduced amount of coke on the interior of the drum, as compared to the amount of coke deposited in the absence of the addition of the paraffinic solvent to the same heavy hydrocarbon feedstock.

19. The delayed coking process of claim 18, wherein the mixing of paraffinic solvent and the furnace-heated coking unit combined feedstream occurs in a mixing zone.

20. The delayed coking process of claim 18, wherein the paraffinic solvent is injected directly into the furnace-heated coking unit combined feedstream.