Demetallization of hydrocarbons

Patent metadata

Field	Value
Publication number	US-10752842-B2
Application number	US-201615579495-A
Country	US
Kind code	B2
Filing date	Jun 30, 2016
Priority date	Jul 2, 2015
Publication date	Aug 25, 2020
Grant date	Aug 25, 2020

Abstract

The present disclosure refers to a process and a process plant for extraction of metals from a hydrocarbon mixture obtained from a gasification or pyrolysis process, comprising the steps of combining said hydrocarbon mixture with an aqueous acid forming a mixture, mixing said mixture, separating said mixture in a contaminated aqueous phase and a purified hydrocarbon phase, with the associated benefit of said aqueous acid being able to release metals bound in such gasification and pyrolysis processes.

First claim

The invention claimed is:

1. A process for producing a hydrotreated hydrocarbon from a hydrocarbon mixture obtained from a gasification or pyrolysis process or from an oxygenate mixture of biological origin, said hydrocarbon mixture having an acidity number above 1.5 mg KOH/g, comprising the steps of:
a. combining said hydrocarbon mixture with an aqueous acid forming a mixture,
b. mixing said mixture,
c. separating said mixture in a contaminated aqueous phase and a purified hydrocarbon phase,
d. combining said purified hydrocarbon phase with a gas rich in hydrogen forming a hydroprocessing stream, and
e. directing said hydroprocessing stream to a hydroprocessing step forming a hydrotreated hydrocarbon,
wherein the process does not comprise a step of addition of an aqueous liquid comprising elements other than C, H, O, N and S in a concentration above 0.1% such that neither the aqueous acid, nor any other aqueous additive, would comprise other elements than C, H, O, N or S above 0.1%.

2. The process according to claim 1 , in which the hydrocarbon mixture comprises from 0.5% to 10% oxygen.

3. The process according to claim 1 according to which the aqueous acid is taken from strong mineral acids or organic acids.

4. The process according to claim 1 , according to which concentration of the aqueous acid is from 1% to 30%.

5. The process according to claim 1 , according to which hydrocarbon mixture is combined with acid in a ratio from 20:1 to 1:2.

6. The process according to claim 1 , according to which step b is carried out at a temperature from 20° C. to 150° C.

7. The process according to claim 1 , according to which the hydrocarbon mixture has an acid number lower than 150 mg KOH/g.

8. The process according to claim 1 , in which said hydroprocessing step (e) involves contacting the hydroprocessing stream with one or more catalytically active materials being active in one or more a reactions taken from the group of hydrogenation of heteratomic hydrocarbons, hydrogenation of diolefins and hydrogenation of metallic heteratomic hydrocarbons, wherein each of said one or more catalytically active materials may be present in the one or more reactors, wherein any sequence of said one or more materials may be used and wherein pressure, temperature and space velocity are selected such that the catalytically active materials are active for the appropriate reactions.

9. The process according to claim 1 , in which an amount of said hydrotreated hydrocarbon is withdrawn and recycled as a recycle stream to a position upstream the point of withdrawal, in a hydrocarbon mixture:recycle stream ratio from 1:½ to 1:3.

10. The process according to claim 1 , further comprising a hydrocracking step (f) after said hydroprocessing step (e), optionally comprising a further hydrotreatment step and a separation step (g) after said hydrocracking step (f) providing a vapour product and one or more liquid hydrocarbon products, wherein the hydrocracking step (f) is operated at a temperature between 330° C. and 420° C., a pressure between 1.5 MPa and 20 MPa, a liquid hourly space velocity between 0.2 hr-1 and 5 hr-1, and a hydrogen to hydrocarbon ratio between 100 and 2000 Nm3/m3.

11. A process according to claim 1 , further comprising a step upstream step (a) of gasifying a carbonaceous material, forming a said hydrocarbon having an acid number above 1.5 mg KOH/g.

12. A process according to claim 11 , further comprising a step of transporting an intermediate from one geographical location to another, wherein said intermediate is either said hydrocarbon having an acid number above 1.5 mg KOH/g or said hydrotreated hydrocarbon.

13. The process according to claim 1 , wherein said hydrocarbon mixture has an acidity number above 2 mg KOH/g.

14. The process according to claim 1 , wherein said hydrocarbon mixture has an acidity number above 4 mg KOH/g.

15. A process plant for production of a purified hydrocarbon from a tar feedstock comprising:
a. an acid wash reactor having one or more inlets in fluid communication with a tar feedstock inlet and with a acid inlet and having an outlet,
b. a means for phase separation having an inlet, a aqueous phase outlet, and a purified hydrocarbon phase outlet,
c. a gasifier or pyrolysis section having a solid carbonaceous fuel inlet, a water inlet and optionally an oxidant inlet, a synthesis gas outlet and a tar outlet,
wherein the outlet of said acid wash reactor is in fluid communication with the inlet of said means for phase separation, and
wherein said tar outlet is in fluid communication with said tar feedstock inlet.

16. The process plant according to claim 15 , further comprising d. a gas cleaning section receiving a gas comprising CO, H2 and SO2, having an inlet, a desulfurized synthesis gas outlet and a sulfuric gas outlet e. a sulfuric acid production section having a sulfur source inlet and a sulfuric acid outlet, wherein said sulfuric gas outlet is in fluid communication with said sulfur source inlet, said sulfuric acid outlet is in fluid communication with said acid inlet and said tar outlet is in fluid communication with said tar feedstock inlet.

17. The process plant according to claim 16 wherein said means for phase separation is taken from the group comprising centrifuges, electrostatic separators, gravity separators.

18. The process plant according to claim 15 , comprising a section for hydrotreatment, having an inlet and an outlet, with the inlet of said section for hydrotreatment being in fluid connection with the outlet of said purified hydrocarbon phase outlet.

19. The process plant according to claim 18 comprising a section for hydrocracking, having an inlet and an outlet, with the inlet of said section for hydrocracking being in fluid connection with the outlet of said outlet of the section for hydrotreatment.

Assignees

• Haldor Topsoe As

Inventors

• Egeberg Rasmus Gottschalck
• Hidalgo Vivas Angelica
• Enevoldsen Søren Selde

Classifications

• C10C1/20

  Refining by chemical means {inorganic or organic compounds}(obtaining hydrocarbon oils C10G) · CPC title

• C10J3/00

  Production of combustible gases containing carbon monoxide from solid carbonaceous fuels (destructive distillation processes C10B) · CPC title

• C10B53/00

  Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form (wet carbonising of peat C10F) · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G17/06

  using acids derived from sulfur or acid sludge thereof · CPC title