# US 2014/0197072 A1 · Oil upgrading within combustion exhaust

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- Number: US 2014/0197072 A1
- Document ID: US20140197072A1
- Status: Published application
- Kind: A1
- Application number: 14/149,190
- Filed: 2014-01-07
- Published: 2014-07-17
- Earliest claimed: 2013-01-14
- Assignees: ConocoPhillips Company
- Applicants: Conocophillips Company
- Inventors: David William LARKIN
- Web page: https://patentgrep.com/patent/US20140197072A1

## CPC

- C10G 9/38: produced by partial combustion of the material to be cracked or by combustion of another hydrocarbon
- Y02P 30/40: Ethylene production
- C10G: CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION (cracking to hydrogen or synthesis gas C01B; cracking or pyrolysis of hydrocarbon gases to individual hydrocarbons or mixtures thereof of definite or specified constitution C07C; cracking to cokes C10B); RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

## Abstract

Methods and systems relate to upgrading hydrocarbons, such as bitumen, by contacting the bitumen with flue gas of oxy-combustion. Quenching a mixture formed of the bitumen and the flue gas controls conversion of the bitumen. Limited size and amount of equipment needed enables employing such upgrading at production fields to facilitate making the bitumen transportable by pipeline without relying on diluents.

## Claims

### Claim 1

A method of upgrading hydrocarbons, comprising:
combusting oxygen and fuel inside a vessel to generate flue gas;
introducing the hydrocarbons into the vessel and in contact with the flue gas to cause thermal cracking of the hydrocarbons;
quenching a mixture of the hydrocarbons and the flue gas to control conversion of the hydrocarbons; and
separating the mixture into an aqueous stream, a gaseous stream and a products stream containing the hydrocarbons that have been upgraded.

### Claim 2 (depends on 1)

The method according to claim 1, wherein the quenching includes introducing water into the mixture for vaporization.

### Claim 3 (depends on 1)

The method according to claim 1, wherein the flue gas contains hydrogen and steam to limit coking and olefin formation.

### Claim 4 (depends on 1)

The method according to claim 1, further comprising separating the oxygen from air prior to supplying the oxygen to the vessel.

### Claim 5 (depends on 1)

The method according to claim 1, further comprising cooling the flue gas prior to introducing the hydrocarbons into the vessel.

### Claim 6 (depends on 1)

The method according to claim 1, further comprising cooling the flue gas with water prior to introducing the hydrocarbons into the vessel.

### Claim 7 (depends on 1)

The method according to claim 1, further comprising cooling the flue gas by passing a portion of the flue gas through a heat exchanger before being recycled and combined with a remainder of the flue gas prior to introducing the hydrocarbons into the vessel.

### Claim 8 (depends on 1)

The method according to claim 1, wherein the vessel is located in a production field to provide the upgrading remote from a refinery.

### Claim 9 (depends on 1)

The method according to claim 1, further comprising transporting the products stream by pipeline to a refinery for additional processing.

### Claim 10 (depends on 1)

The method according to claim 1, wherein the hydrocarbons include bitumen and the products stream meets pipeline specifications without relying on diluents.

### Claim 11 (depends on 1)

The method according to claim 1, wherein the hydrocarbons when introduced into the vessel have an American Petroleum Institute (API) gravity less than 15° and the products stream has an API gravity greater than 19°.

### Claim 12 (depends on 1)

The method according to claim 1, further comprising withdrawing solid coke material with the aqueous stream from the products stream.

### Claim 13

A system for upgrading hydrocarbons, comprising:
a vessel coupled to receive oxygen and fuel for combustion inside the vessel to generate flue gas, wherein the vessel includes a first inlet to introduce the hydrocarbons into the vessel and in contact with the flue gas for thermal cracking of the hydrocarbons and a second inlet to introduce a coolant for controlling conversion of the hydrocarbons by quenching a mixture of the hydrocarbons and the flue gas; and
a separator coupled to receive the mixture for splitting into an aqueous output, a gaseous output and a product output containing the hydrocarbons that have been upgraded.

### Claim 14 (depends on 13)

The system according to claim 13, wherein the coolant is water introduced into the mixture for vaporization.

### Claim 15 (depends on 13)

The system according to claim 13, wherein the flue gas contains hydrogen and steam to limit coking and olefin formation.

### Claim 16 (depends on 13)

The system according to claim 13, further comprising a third inlet into the vessel disposed to introduce a fluid for cooling the flue gas ahead of the first inlet for introducing the hydrocarbons into the vessel.

### Claim 17 (depends on 13)

The system according to claim 13, further comprising a third inlet into the vessel disposed to introduce water for cooling the flue gas ahead of the first inlet for introducing the hydrocarbons into the vessel.

### Claim 18 (depends on 13)

The system according to claim 13, further comprising a recycle loop off of the vessel and including a heat exchanger for cooling at least some of the flue gas ahead of the first inlet for introducing the hydrocarbons into the vessel.

### Claim 19 (depends on 13)

The system according to claim 13, further comprising an air separation unit coupled to supply the oxygen to the vessel.

### Claim 20 (depends on 13)

The system according to claim 13, wherein the vessel is located in a production field to provide the upgrading remote from a refinery.
