초록 ▼

The present invention provides a process for controlling the ratio of hydrogen to carbon monoxide in feed streams to reactors that convert syngas to hydrocarbon liquids. The process includes primary syngas production process for converting hydrocarbon gas to syngas comprising hydrogen and carbon mon

The present invention provides a process for controlling the ratio of hydrogen to carbon monoxide in feed streams to reactors that convert syngas to hydrocarbon liquids. The process includes primary syngas production process for converting hydrocarbon gas to syngas comprising hydrogen and carbon monoxide. The process further includes introducing a hydrogen rich stream, a carbon monoxide rich stream, or both produced by an auxiliary source to a feed stream being passed to a reactor for converting the syngas to hydrocarbon liquid, thereby adjusting the H2/CO ratio in the feed stream. Examples of reactors that may be used to convert syngas to hydrocarbon liquids are FT reactors staged in series and oxygenate producing reactors staged in series.

대표청구항 ▼

1. A process for producing hydrocarbons, comprising:(a) producing a synthesis gas stream in a syngas production process where inlet materials to the syngas production process are substantially free of carbon dioxide, and wherein the synthesis gas comprises primarily hydrogen and carbon monoxide; (b)

1. A process for producing hydrocarbons, comprising:(a) producing a synthesis gas stream in a syngas production process where inlet materials to the syngas production process are substantially free of carbon dioxide, and wherein the synthesis gas comprises primarily hydrogen and carbon monoxide; (b) forming a reactant-stream for a hydrocarbon synthesis process comprising at least a portion of the synthesis gas from step (a), wherein the ratio of hydrogen to carbon monoxide in the reactant-stream is not preferred for synthesis to hydrocarbons such that one component is a lean component; (c) providing from a feedstock which is substantially free of carbon dioxide a second stream which is rich in the lean component of the hydrocarbon synthesis process reactant-stream of step (b); (d) adding an amount of said second stream to the reactant-stream to form an adjusted reactant-stream which has a hydrogen to carbon monoxide ratio more desirable for hydrocarbon synthesis; (e) catalytically converting the adjusted reactant-stream from step (d) in a synthesis reaction to produce hydrocarbons. 2. The process according to claim 1, wherein the step (e) of catalytically converting the adjusted reactant-stream comprises Fischer-Tropsch synthesis conducted in one or more Fischer-Tropsch reactors, and wherein at least one Fischer-Tropsch reactor produces an FT gas effluent comprising un-reacted synthesis gas, and wherein the FT gas effluent is optionally subjected again to catalytic conversion conditions for Fischer-Tropsch synthesis in a Fischer-Tropsch reactor.3. The process according to claim 2 wherein the reactant-stream of step (b) comprises FT gas effluent.4. The process according to claim 2 wherein the FT gas effluent from one Fischer-Tropsch reactor is directed to a second Fischer-Tropsch reactor.5. The process according to claim 4 wherein a second reactant-stream is formed for the second Fischer-Tropsch reactor and the second reactant-stream comprises at least one of:(a) synthesis gas from the syngas production process; and (b) the FT effluent from the one Fischer-Tropsch reactors; and the process further comprises adding an amount of said second stream to said second reactant-stream to create a second adjusted reactant-stream that is more preferable for Fischer-Tropsch synthesis.6. The process according to claim 2 wherein the FT gas effluent is recycled back into the same Fischer-Tropsch reactor from which it exited.7. The process according to claim 1 further comprising the step of upgrading the hydrocarbons produced in step (e) into hydrocarbon products.8. A process for producing hydrocarbons, comprising:(a) producing a synthesis gas stream in a syngas production process where inlet materials to the syngas production process are substantially free of carbon dioxide, wherein the synthesis gas comprises primarily hydrogen and carbon monoxide; (b) dividing the synthesis gas stream from step (a) into at least a first syngas stream and a second syngas stream; (c) forming a reactant-stream for a hydrocarbon synthesis process comprising at least a portion of the synthesis gas from step (a) wherein the ratio of hydrogen to carbon monoxide in the reactant-stream is not preferred for synthesis to hydrocarbons such that one component is a lean component; (d) processing the second syngas gas stream to create a third syngas stream which is rich in the component in which the first syngas stream is lean; (e) adding an amount of the third syngas stream to the reactant-stream to form an adjusted reactant-stream which has a hydrogen to carbon monoxide ratio more desirable for hydrocarbon synthesis; and (f) catalytically converting the adjusted reactant-stream from step (e) in a synthesis reaction to produce hydrocarbons. 9. The process according to claim 8, wherein the step (d) of processing the second syngas stream comprises separating the synthesis gas into a hydrogen-rich stream and a carbon monoxide rich stream wherein one of the hydrogen-rich and carbon monoxide rich stream comprises the third syngas stream.10. The process according to claim 9, wherein the step (d) of processing the second syngas stream comprises separating with one of: a membrane separator; cryogenic separator; and pressure swing adsorber.11. The process according to claim 8, wherein the synthesis gas of step (a) is further defined by being hydrogen lean and further wherein the step (d) of processing the second syngas stream comprises a water-gas-shift reaction for reacting the second syngas stream with water, and optionally an amine-based carbon dioxide removal process, to form a hydrogen-rich stream and the hydrogen-rich stream comprises the third syngas stream.12. The process according to claim 8, wherein the step (f) of catalytically converting the adjusted reactant-stream comprises Fischer-Tropsch synthesis conducted in one or more Fischer-Tropsch reactors and wherein at least one Fischer-Tropsch reactor produces an FT gas effluent comprising un-reacted synthesis gas and wherein FT gas effluent exiting a Fischer-Tropsch reactor is optionally subjected again to catalytic conversion conditions for Fischer-Tropsch synthesis in a Fischer-Tropsch reactor.13. The process according to claim 12 wherein the reactant-stream of step (c) comprises FT gas effluent.14. The process according to claim 12 wherein the FT gas effluent from one Fischer-Tropsch reactor is directed to a second Fischer-Tropsch reactor.15. The process according to claim 12 wherein the FT gas effluent is recycled back into the same Fischer-Tropsch reactor from which it exited.16. The process according to claim 8 further comprising the step of refining the hydrocarbons produced in step (f) into hydrocarbon products.17. A process for producing hydrocarbons, comprising:(a) producing a synthesis gas stream in a catalytic partial oxidation process, wherein the synthesis gas stream comprises primarily hydrogen and carbon monoxide; (b) forming a reactant-stream for a hydrocarbon synthesis process comprising at least a portion of the synthesis gas from step (a) wherein the ratio of hydrogen to carbon monoxide in the reactant-stream is less than that preferred for synthesis to hydrocarbons and hydrogen is the lean component; (c) adding an amount of an auxiliary gas stream which is rich in hydrogen to the reactant-stream to form an adjusted reactant-stream which has a hydrogen to carbon monoxide ratio more desirable for hydrocarbon synthesis; (d) catalytically converting the adjusted reactant-stream from step (c) in a synthesis reaction to produce hydrocarbons. 18. The process according to claim 17, wherein the step (d) of catalytically converting the adjusted reactant-stream comprises Fischer-Tropsch synthesis conducted in one or more Fischer-Tropsch reactors and wherein at least one Fischer-Tropsch reactor produces an FT gas effluent comprising un-reacted synthesis gas and wherein FT gas effluent exiting a Fischer-Tropsch reactor is optionally subjected again to catalytic conversion conditions for Fischer-Tropsch synthesis in a Fischer-Tropsch reactor.19. The process according to claim 18 wherein the reactant-stream of step (b) comprises FT gas effluent.20. The process according to claim 18 wherein the FT gas effluent from one Fischer-Tropsch reactor is directed to a second Fischer-Tropsch reactor.21. The process according to claim 18 wherein the FT gas effluent is recycled back into the same Fischer-Tropsch reactor from which it exited.22. The process according to claim 17 wherein the auxiliary gas stream is derived from a least one of the following:(a) a process for converting hydrocarbons to synthesis gas; (b) a process for converting hydrocarbons to olefins; (c) a process for converting hydrocarbons to aromatics; (d) a process for catalytically dehydrogenating hydrocarbons; (e) a process for catalytically cracking hydrocarbons; (f) a process for refining petroleum; and (g) a process for converting hydrocarbons to carbon filaments. 23. The process according to claim 17 further comprising the step of upgrading the hydrocarbons produced in step (d) into hydrocarbon products.24. The process according to claim 22 further comprising subjecting the synthesis gas produced in step (a) to a water-gas-shift reaction.25. A process for operating a hydrocarbon synthesis reactor within a hydrocarbon production system, wherein the process comprises the steps of:(a) forming a reactant-stream for the hydrocarbon synthesis reactor from at least one of: (1) synthesis gas made in a process which is substantially free of carbon dioxide at the inlet; (2) effluent gas from at least one other synthesis reactor; wherein the ratio of hydrogen to carbon monoxide in the reactant-stream is not preferred for synthesis to hydrocarbons such that one component is a lean component;(b) adding an amount of a feedstock which is rich in the lean component to the reactant-stream to form an adjusted reactant-stream which has a hydrogen to carbon monoxide ratio more desirable for hydrocarbon synthesis; (c) catalytically converting the adjusted reactant-stream from step (b) in a synthesis reaction to produce hydrocarbons. 26. The process according to claim 25 wherein the reactant-stream further comprises effluent gas recycled from the hydrocarbon synthesis reactor.27. A process for operating a plurality of hydrocarbon synthesis reactors that catalytically convert synthesis gas, comprising primarily hydrogen and carbon monoxide, to hydrocarbons in a hydrocarbon synthesis production system, wherein the process comprises the steps of:(a) forming a reactant-stream for each hydrocarbon synthesis reactor from at least one of: (1) synthesis gas made in a process which is substantially free of carbon dioxide at the inlet; (2) effluent gas from at least one other synthesis reactor; wherein one reactant-stream is a deficient-stream in that the ratio of hydrogen to carbon monoxide is not preferred for hydrocarbon synthesis and one component in the deficient-stream is a lean component;(b) adding an amount of a feedstock which is rich in the lean component to the deficient-stream to form an adjusted reactant-stream which has a hydrogen to carbon monoxide ratio more desirable for hydrocarbon synthesis; and (c) catalytically converting the reactant-streams in synthesis reactions to produce hydrocarbons. 28. The process according to claim 27 wherein the reactant-streams in step (a) optionally comprise effluent gas recycled from the hydrocarbon synthesis reactor.29. The process according to claim 28, wherein the step (c) of catalytically converting the reactant-streams comprises Fischer-Tropsch synthesis reactions.30. The process according to claim 29 wherein a plurality of deficient-streams are formed and the process further comprises adding to at least a second deficient-stream an amount of a feedstock which is rich in the lean component to form adjusted reactant-streams which are more preferable for hydrocarbon synthesis.31. The process according to claim 27 wherein a plurality of deficient-streams are formed and the process further comprises adding to at least a second deficient-stream an amount of a feedstock which is rich in the lean component to form adjusted reactant-streams which are more preferable for hydrocarbon synthesis.