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Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam

Reformer and method for producing hydrogen and steam where steam is used for steam-assisted extraction of heavy hydrocarbons. Steam is injected into a hydrocarbon-containing reservoir. Hydrocarbons are extracted from the reservoir along with produced water. Hydrogen is produced in a catalytic steam hydrocarbon reformer. Combustion product gas from the reformer is used to generate wet steam in a once-through steam generator from produced water recycled from the reservoir. The wet steam is used for the steam-assisted extraction of heavy hydrocarbons. The reformer has a heat exchanger section where a heat exchanger is suitable for processing the produced water by once-through steam generation and is suitable for mechanical cleaning.

대표청구항 ▼

1. A hydrocarbon processing method comprising: injecting a steam-containing stream through an injection well into a hydrocarbon-containing reservoir;extracting hydrocarbons from the hydrocarbon-containing reservoir and withdrawing the hydrocarbons and recycle water through a production well, the rec

1. A hydrocarbon processing method comprising: injecting a steam-containing stream through an injection well into a hydrocarbon-containing reservoir;extracting hydrocarbons from the hydrocarbon-containing reservoir and withdrawing the hydrocarbons and recycle water through a production well, the recycle water formed from a portion of the steam-containing stream;introducing a reformer feed gas mixture into a plurality of catalyst-containing reformer tubes of a catalytic steam reformer and reacting the reformer feed gas mixture in a reforming reaction under reaction conditions effective to form a process gas comprising hydrogen;combusting a fuel with an oxidant gas in a combustion section of the reformer external to the plurality of catalyst-containing tubes under conditions effective to combust the fuel to form a combustion product gas and generate heat to supply energy for the reforming reaction;heating a first stream comprising the recycle water by indirect heat transfer with the combustion product gas thereby producing steam for the steam-containing stream from the first stream, the steam produced at a first pressure between 1 MPa (absolute) to 10 MPa (absolute) with a first steam quality less than 100% on a mass flow rate basis;conditioning process make-up water in a boiler feed water preparation system to produce boiler feed water from the process make-up water; andheating the boiler feed water by indirect heat transfer with at least one of the process gas and the combustion product gas thereby forming process steam, wherein the reformer feed gas mixture comprises the process steam. 2. The method of claim 1 wherein the boiler feed water does not comprise recycle water. 3. The method of claim 1 wherein less than 10% on a mass flow rate basis of the steam in the steam-containing stream is from the boiler feed water. 4. The method of claim 1 wherein the steam-containing stream is not formed from the boiler feed water. 5. The method of claim 1 wherein the process steam is separated from the boiler feed water in a steam drum. 6. The method of claim 1 wherein the first stream further comprises injection make-up water. 7. The method of claim 1 further comprising: heating a second stream comprising at least one of injection make-up water and the recycle water by indirect heat transfer with the process gas followed by heating the second stream by indirect heat transfer with the combustion product gas mixture thereby producing additional steam for the steam-containing stream from the second stream, the additional steam produced at the first pressure with the first steam quality or a second pressure between 1 MPa (absolute) to 10 MPa (absolute) with a second steam quality less than 100% on a mass flow rate basis. 8. The method of claim 7 wherein the process gas is shifted in one or more shift reactors prior to indirect heat exchange with the second stream. 9. The method of claim 7 wherein the first steam quality is between 50% and 85% and the second steam quality is between 50% and 85%. 10. The method of claim 1 wherein the first steam quality is between 50% and 85%. 11. The method of claim 1 further comprising removing CO2 from the process gas wherein the steam-containing stream comprises the removed CO2. 12. The method of claim 1 further comprising: condensing water in the process gas to form a condensate and a water-depleted process gas;separating the condensate from the water-depleted process gas wherein the boiler feed water comprises the condensate; andseparating the water-depleted process gas into a hydrogen product gas and a residual gas wherein the fuel comprises the residual gas. 13. The method of claim 1 further comprising: withdrawing hydrocarbon gases from the production well wherein the reformer feed gas mixture comprises the hydrocarbon gases or the fuel comprises the hydrocarbon gases. 14. The method of claim 1 further comprising: operating a gas turbine power generator to form electrical power and a gas turbine exhaust wherein the oxidant gas comprises the gas turbine exhaust. 15. The method of claim 14 further comprising: heating a third stream comprising at least one of injection make-up water and the recycle water in a heat recovery steam generator thereby producing even more additional steam for the steam-containing stream from the third stream, the even more additional steam produced at a third pressure between 1 MPa (absolute) to 10 MPa (absolute) and a third steam quality less than 100% on a mass flow rate basis, wherein a combustion oxidant for the heat recovery steam generator comprises the gas turbine exhaust. 16. The method of claim 15 wherein the third steam quality is between 50% and 85%. 17. The method of claim 1 further comprising: exhausting the combustion product gas from the reformer at a location upstream of a heat exchanger that provides the indirect heat transfer between the first stream and the combustion product gas, thereby discontinuing heating of the first stream; andcleaning the heat exchanger while continuing to form the process gas comprising hydrogen. 18. The method of claim 1 further comprising: withdrawing hydrocarbon gases from the production well wherein the reformer feed gas mixture comprises the hydrocarbon gases and the fuel comprises the hydrocarbon gases.