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US 11,535,515 B2Granted
Sulfur recovery within a gas processing system
AssigneeExxonMobil Upstream Research Company
InventorsPaul Scott Northrop, John Timothy Cullinane
Life of this patent
Estimating the term…
Abstract
A method for recovering sulfur within a gas processing system is described herein. The method includes contacting a natural gas stream including an acid gas with a solvent stream within a co-current contacting system to produce a sweetened natural gas stream and a rich solvent stream including an absorbed acid gas. The method also includes removing the absorbed acid gas from the rich solvent stream within a regenerator to produce a concentrated acid gas stream and a lean solvent stream. The method further includes recovering elemental sulfur from hydrogen sulfide (H2S) within the concentrated acid gas stream via a sulfur recovery unit.
Claims18
A gas processing system, comprising:
- a co-current contacting system configured to:
- contact a natural gas stream comprising an acid gas with a solvent stream to produce a sweetened natural gas stream and a rich solvent stream comprising an absorbed acid gas;
- and
- send the rich solvent stream to a regenerator;
- the regenerator configured to:
- remove the absorbed acid gas from the rich solvent stream to produce a concentrated acid gas stream and a lean solvent stream;
- and
- send the concentrated acid gas stream to a sulfur recovery unit;
- and
- the sulfur recovery unit configured to recover elemental sulfur from hydrogen sulfide (H2S) within the concentrated acid gas stream;
- and
- the co-current contacting system further comprising:
- a co-current contactor located in-line within a pipe, the co-current contactor comprising:
- an annular support ring configured to maintain the co-current contactor within the pipe;
- a plurality of radial blades configured to allow the solvent stream to flow into the co-current contactor;
- and
- a central gas entry cone configured to allow the natural gas stream to flow through a hollow section within the co-current contactor;
- wherein the co-current contactor provides for efficient incorporation of liquid droplets formed from the solvent stream into the natural gas stream such that the acid gas from the natural gas stream is absorbed by the liquid droplets;
- and
- a separation system configured to remove the liquid droplets comprising the absorbed acid gas from the natural gas stream, producing the sweetened natural gas stream and the rich solvent stream.
17 more elements
A method for recovering sulfur within a gas processing system, comprising:
- contacting a natural gas stream comprising an acid gas with a solvent stream within a co-current contacting system to produce a sweetened natural gas stream and a rich solvent stream comprising an absorbed acid gas;
- removing the absorbed acid gas from the rich solvent stream within a regenerator to produce a concentrated acid gas stream and a lean solvent stream;
- and
- recovering elemental sulfur from hydrogen sulfide (H2S) within the concentrated acid gas stream via a sulfur recovery unit;
- wherein contacting the natural gas stream comprising the acid gas with the solvent stream within the co-current contacting system comprises:
- flowing the solvent stream into a co-current contactor via an annular support ring and a plurality of radial blades extending from the annular support ring, wherein the annular support ring secures the co-current contactor in-line within a pipe;
- flowing the natural gas stream into the co-current contactor via a central gas entry cone that is supported by the plurality of radial blades, wherein a first portion of the natural gas stream flows through the central gas entry cone and a second portion of the natural gas stream flows around the central gas entry cone between the plurality of radial blades;
- contacting the natural gas stream with the solvent stream to provide for incorporation of liquid droplets formed from the solvent stream into the natural gas stream such that the acid gas from the natural gas stream is absorbed by the liquid droplets;
- and
- separating the liquid droplets comprising the absorbed acid gas from the natural gas stream within a separator, producing the sweetened natural gas stream and the rich solvent stream.
7 more elements
A gas processing system, comprising:
- a first co-current contacting system configured to:
- contact a natural gas stream comprising an acid gas with a first solvent stream to produce a first partially-sweetened natural gas stream and a first rich solvent stream comprising a first portion of absorbed acid gas;
- and
- send the first rich solvent stream to a regenerator;
- and
- wherein the first co-current contacting system comprises:
- a co-current contactor located in-line within a pipe, the co-current contactor comprising:
- an annular support ring configured to maintain the co-current contactor within the pipe;
- a plurality of radial blades configured to allow the first solvent stream to flow into the co-current contactor;
- and
- a central gas entry cone configured to allow the natural gas stream to flow through a hollow section within the co-current contactor;
- wherein the co-current contactor provides for efficient incorporation of liquid droplets formed from the first solvent stream into the natural gas stream such that the acid gas from the natural gas stream is absorbed by the liquid droplets;
- and
- a separation system configured to remove the liquid droplets comprising the absorbed acid gas from the natural gas stream, producing the first partially-sweetened natural gas stream and the first rich solvent stream;
- a second co-current contacting system configured to:
- contact the first partially-sweetened natural gas stream with a second solvent stream to produce a second partially-sweetened natural gas stream and a second rich solvent stream comprising a second portion of absorbed acid gas;
- and
- send the second rich solvent stream back into the first co-current contacting system as the first solvent stream;
- a third co-current contacting system configured to:
- contact the second partially-sweetened natural gas stream with a third solvent stream to produce a sweetened natural gas stream and a third rich solvent stream comprising a third portion of absorbed acid gas;
- and
- send the third rich solvent stream back into the second co-current contacting system as the second solvent stream;
- the regenerator configured to:
- remove the first portion of the absorbed acid gas from the first solvent stream to produce a concentrated acid gas stream and a lean solvent stream;
- send the lean solvent stream into the third co-current contacting system as the third solvent stream;
- and
- send the concentrated acid gas stream to a sulfur recovery unit;
- and
- the sulfur recovery unit configured to recover elemental sulfur from hydrogen sulfide (H2S) within the concentrated acid gas stream.
26 more elements
Dependencies are inferred from the claim text.