Process for producing diesel fuel from olefinic refinery feedstreams

Patent metadata

Field	Value
Publication number	US-10800981-B2
Application number	US-201916274735-A
Country	US
Kind code	B2
Filing date	Feb 13, 2019
Priority date	Feb 13, 2019
Publication date	Oct 13, 2020
Grant date	Oct 13, 2020

Abstract

An integrated refinery process for producing diesel fuel blending stock from olefinic heavy naphtha streams that contain gasoline and compounds with carbon numbers in the range of from 9-14 are oxidized and converted into their corresponding oxides in the presence of a homogeneous or heterogeneous catalyst, or both, and optionally an acid phase transfer agent for the liquid reactants, the product oxides having boiling points about 34° C. higher than the corresponding olefins, and as a result, in the diesel blending component boiling point range. The oxygenates produced have lubricating properties that enhance the typically poor lubricity characteristics of ultra-low sulfur diesels and reduce the need for additives to improve the lubricity of the blended diesel fuels.

First claim

The invention claimed is:

1. An integrated refinery process for producing diesel fuel blending components, the process comprising:
a. contacting an olefinic heavy naphtha hydrocarbon feedstock with a liquid oxidant and an oxidation catalyst in a reactor for a predetermined period of time that is sufficient to oxidize all or substantially all of the olefinic compounds in the feedstock to form their oxides thereby forming a reaction mixture;
b. passing the reaction mixture to an aqueous separation zone and separating an aqueous phase from a hydrocarbon reaction mixture and discharging an aqueous phase;
c. recovering and passing the hydrocarbon reaction mixture to a hydrocarbon separation zone and separating gasoline range blending components from diesel range blending components based on their respective boiling point ranges; and
d. recovering the diesel range blending components.

2. The process of claim of claim 1 in which the feedstock is derived from a catalytic cracking unit or a thermal cracking unit.

3. The process of claim 2 in which the catalytic cracking unit is a fluidized catalytic cracking (FCC) unit.

4. The process of claim 3 in which the olefinic heavy naphtha hydrocarbon feedstock includes FCC gasoline.

5. The process of claim 4 in which the FCC gasoline is a mixture of hydrocarbons comprising paraffins, aromatics, olefins and naphthenes boiling in the range from 36° to 240° C.

6. The process of claim 2 in which the thermal cracking unit is a delayed coking unit.

7. The process of claim 1 in which the liquid oxidant is in an aqueous solution and the reaction mixture includes an acid phase transfer agent.

8. The process of claim 1 in which the liquid oxidant is selected from the group consisting of hydrogen peroxide, organic peroxides, tert-butyl hydroperoxide, peroxy acids, and mixtures thereof.

9. The process of claim 1 in which the oxidation catalyst includes a metal from IUPAC Groups 4-10 of the Periodic Table.

10. The process of claim 1 in which the oxidation catalyst is an oil soluble homogeneous catalyst selected from the group consisting of sodium tungstate, molybdenum acetylacetone and molybdenum hexacarbonyl.

11. The process of claim 8 in which the reaction is conducted in a two-phase oxidation reactor.

12. The process of claim 1 in which the oxidation catalyst is a solid heterogeneous catalyst comprising a support and a metal selected from the group consisting of IUPAC Groups 4-10 of the Periodic Table.

13. The process of claim 12 in which the reaction is conducted in a three-phase reactor selected from the group consisting of fixed bed, ebullated bed, slurry bed and moving bed reactors.

14. The process of claim 9 in which the oxidation reactor is a fixed bed reactor or a continuously stirred tank reactor.

15. The process of claim 1 in which the oxides formed by the catalytic oxidation of the olefins are oxygenates.

16. The process of claim 15 in which the oxygenates formed in the reaction mixture increase the lubricity of the diesel fuel blending components.

17. The process of claim 1 in which the oxides formed by the catalytic oxidation of the olefins are epoxides of the olefins.

Assignees

• Saudi Arabian Oil Co

Inventors

• Koseoglu Omer Refa

Classifications

• C10G2400/04

  Diesel oil · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• C10G2300/301

  Boiling range · CPC title

• C10G2300/1044

  Heavy gasoline or naphtha having a boiling range of about 100 - 180 °C · CPC title

• C10G61/02 Primary

  plural serial stages only · CPC title