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The present invention relates a process and apparatus that recovers a helium rich stream from a mixed gas having low concentrations of helium therein. More specifically, the invention relates to an integrated process and apparatus for treating a mixed feed gas from an operating process that produces

The present invention relates a process and apparatus that recovers a helium rich stream from a mixed gas having low concentrations of helium therein. More specifically, the invention relates to an integrated process and apparatus for treating a mixed feed gas from an operating process that produces a liquid product from natural gas containing helium, such as processes that produce ammonia, methanol, or liquid hydrocarbons.

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1. An integrated process for recovery of a helium rich stream and a hydrogen rich stream from a feed stream containing 10-80 volume percent hydrogen, 0.1-5.0 volume percent helium, and the balance being higher boiling components, comprising: (a) routing the pressurized feed stream to a cryogenic sep

1. An integrated process for recovery of a helium rich stream and a hydrogen rich stream from a feed stream containing 10-80 volume percent hydrogen, 0.1-5.0 volume percent helium, and the balance being higher boiling components, comprising: (a) routing the pressurized feed stream to a cryogenic separation unit wherein the majority of the higher boiling components are separated and removed from the feed stream;(b) heating a stream containing helium removed from the cryogenic separation unit and routing the heated stream to at least one hydrogen transport membrane where the heated stream is separated into a hydrogen rich permeate stream, and a retentate stream depleted of hydrogen;(c) routing the retentate stream depleted of hydrogen to at least one oxidation unit and reacting it with an oxidant to remove substantially all the remaining hydrogen in the retentate to produce a helium containing stream, wherein the helium concentration ranges from about 5-40 volume percent and the balance being higher boiling components;(d) routing the helium containing stream to a phase separator and sequentially a dryer wherein most of the water is removed; and(e) routing the dried helium containing stream to the same or a different cryogenic separation unit where the majority of remaining higher-boiling components are removed and a helium rich product stream having about 80% or higher helium content by volume is obtained. 2. The integrated process of claim 1, wherein the feed stream composition comprises by volume 10-80% hydrogen, 0.1-5% helium, 10-90% one or more higher boiling components from the group comprising methane or other hydrocarbons, nitrogen, argon, carbon monoxide and impurities. 3. The integrated process of claim 1, wherein the feed stream is cooled in a cryogenic separation unit against an outlet stream containing predominantly higher boiling components and a separate product stream containing predominantly hydrogen and helium. 4. The integrated process of claim 1, wherein the heated feed stream is at a temperature in the range of about 250-1000° C. 5. The integrated process of claim 1, wherein the hydrogen rich permeate stream is recovered by utilizing a sweep stream to produce a mixture of hydrogen and sweep gas. 6. The integrated process of claim 5, wherein the hydrogen rich permeate stream is recovered by utilizing steam as a sweep stream at pressure and then cooling a steam-hydrogen mixture to condense water and recover hydrogen at a pressure higher than its partial pressure in the retentate stream. 7. The integrated process of claim 5, wherein the sweep stream is nitrogen or other inert gases. 8. The integrated process of claim 1, wherein the hydrogen transport membrane is a two-stage membrane, wherein the hydrogen permeate is recovered at 15-25 psia in the first stage and in the second stage additional hydrogen permeate is recovered under vacuum or by utilizing a sweep stream. 9. The integrated process of claim 1, wherein the retentate stream depleted of hydrogen exiting the hydrogen transport membrane is cooled to 30 to 100° C. prior to routing to the oxidation unit. 10. The integrated process of claim 1, wherein the oxidant is selected from the group consisting of air, oxygen-enriched air, and oxygen. 11. The integrated process of claim 1, wherein the oxidation unit is a catalytic oxidation unit to enhance reaction between hydrogen and oxidant. 12. The integrated process of claim 1, wherein intercoolers and phase separators are employed where two or more catalytic oxidation units are employed to reduce the temperature of effluent from each oxidation unit and to remove condensed water in the helium containing stream. 13. The integrated process of claim 1, wherein the helium rich product stream is further compressed and sent to a helium refinery for further purification and/or liquefaction. 14. The integrated process of claim 1, further comprising compressing the feed stream prior to routing to the cryogenic separation unit. 15. The integrated process of claim 1, further comprising recovering the hydrogen rich permeate stream. 16. The integrated process of claim 1, further comprising compressing a portion of dried helium containing stream and recycling said portion by combining said portion with the hydrogen retenate upstream of the oxidation unit. 17. The integrated process for recovery of a helium rich stream from a feed stream containing 10-80 volume percent of hydrogen, 0.1-5.0 volume percent helium, and the balance being higher boiling components, comprising: (a) routing the pressurized feed stream to a cryogenic separation unit wherein the majority of the higher boiling components are separated and removed from the feed stream;(b) heating the feed stream removed from the cryogenic separation unit and routing the heated feed stream to at least one hydrogen transport membrane where the feed stream is separated into a hydrogen rich permeate stream, and a retentate stream depleted of hydrogen;(c) routing the retentate stream depleted of hydrogen to at least one oxidation unit to remove substantially all the hydrogen remaining in the retentate to produce a helium containing stream, wherein the helium concentration ranges from about 5-40 volume percent and the balance being higher boiling components;(d) routing the helium containing stream to a phase separator and sequentially a dryer wherein most of the water is removed; and(e) further processing the helium containing stream of step (d) in one or more polymeric membrane stages, wherein the permeate is recovered as helium rich product stream having about 80% or higher helium content by volume. 18. The integrated process of claim 17, where the helium containing stream in step (e) is processed in a first polymeric membrane stage where the helium containing stream is separated into a first retentate stream and a first permeate stream having at least about 30% helium content. 19. The integrated process of 19, where the permeate stream having at least about 30% helium content is further separated in a third polymeric membrane stage into a third retentate stream which can be recycled to the first polymeric membrane and a third permeate stream recovered as helium rich product having about 80% or higher helium content by volume. 20. The integrated process of claim 19, wherein the third permeate stream recovered as helium rich product having about 80% or higher helium content by volume is further compressed to a pressure compatible with the downstream delivery point. 21. The integrated process of claim 19, wherein the downstream delivery point is either a storage tank or a helium refinery. 22. The integrated process of claim 17, wherein the third permeate stream recovered as helium rich product contains less than about 1% methane and balance being other higher boiling components. 23. The integrated process of claim 1, wherein the feed stream is generated as a by-product in a process that uses natural gas to produce a liquid product, such as ammonia, methanol, or higher hydrocarbons. 24. The integrated process of claim 17, wherein the helium-rich product stream having at least 80% helium content by volume is further processed to produce a purified helium product stream containing at least 98% helium content by volume. 25. The integrated process of claim 17, wherein the helium-rich product stream is further routed through a pressure swing adsorption apparatus for final purification.