Multi-stage membrane separation process
View Patent ↗The invention concerns a process for the removal of gaseous acidic contaminants, especially carbon dioxide and/or hydrogen sulphide, in two or more stages from a gaseous hydrocarbonaceous feedstream ( 1 ) comprising hydrocarbons and said acidic contaminants, using one or more membranes in each separation stages. The gaseous hydrocarbonaceous feedstream is especially a natural gas stream. The process is especially suitable for feedstreams comprising very high amounts of acidic contaminants, especially carbon dioxide, e.g. more than 25 vol. %, or even more than 45 vol. %. In a first stage ( 2 ) a pure or almost pure stream of acidic contaminants is separated from the feedstream, the acidic contaminants ( 4 ) stream suitably containing less than 5 vol % of hydrocarbons. The remaining stream ( 3 ) comprises the hydrocarbons and still a certain amount of gaseous acidic contaminants. In a second stage ( 5 ) a pure or almost pure stream of hydrocarbons ( 8 ) is separated from the remaining stream, where after the then remaining stream ( 6 ) is combined with the feed for the first stage ( 1 ), the hydrocarbon stream suitably containing less than 5 vol % of acidic contaminants.
1. A process for the removal of gaseous acidic contaminants from a gaseous hydrocarbonaceous feedstream comprising such gaseous acidic contaminants, the process comprising:
1) providing the hydrocarbonaceous feedstream at a pressure between 30 and 120 bara,
2) contacting the hydrocarbonaceous feedstream with a membrane to obtain a hydrocarbon rich retentate and an acidic contaminants rich permeate,
3) contacting the hydrocarbon rich retentate obtained in step 2) with a second membrane to obtain a hydrocarbon rich retentate and an acidic contaminants rich permeate,
4) compressing the acidic contaminants rich permeate obtained in step 3) up till a pressure between 30 and 120 bara, and
5) mixing the compressed permeate obtained in step 4) with the feedstream of step 1)
further comprising obtaining the hydrocarbonaceous feedstream from a gaseous feed comprising hydrocarbons and acidic contaminants by contacting the gaseous feed with a membrane to obtain the hydrocarboneous feedstream and an acidic contaminants rich permeate.
2. The process according to claim 1 , in which the feedstream has a temperature between −20 and 100° C.
3. The process according to claim 1 , in which the acidic contaminants comprise one or more compounds selected from carbon dioxide and hydrogen sulphide.
4. The process according to claim 3 , in which the feedstream comprises carbon dioxide in an amount between 10 and 95 vol % based on the total feedstream, and in which the feedstream comprises hydrogen sulphide in an amount between 0 and 45 vol % based on the total feedstream.
5. The process according to claim 3 , in which the feedstream comprises hydrocarbons in an amount between 5 and 90 vol % based on the feedstream.
6. The process according to claim 1 , in which the permeate obtained in step 2) has a pressure between 1 and 30 bara.
7. The process according to claim 1 , in which the permeate in step 2) has an acidic contaminants content of >90 vol % based on the total retentate stream.
8. The process according to claim 1 , in which the retentate in step 2) has a hydrocarbons content of between 40 and 80 vol % based on the total retentate stream.
9. The process according to claim 1 , in which the permeate in step 3) has a pressure between 1 and 20 bara.
10. The process according to claim 1 , in which the permeate in step 3) has an acidic contaminants content of between 40 and 90 vol % based on the total retentate stream.
11. The process according to claim 1 , in which the retentate in step 3) has a hydrocarbons content of more than 90 vol %, based on the retentate.
12. A process for the removal of gaseous acidic contaminants from a gaseous hydrocarbonaceous feedstream comprising such gaseous acidic contaminants, the process comprising;
1) providing the hydrocarbonaceous feedstream at a pressure between 30 and 120 bara,
2) contacting the hydrocarbonaceous feedstream with a membrane to obtain a hydrocarbon rich retentate and an acidic contaminants rich permeate,
3) contacting the hydrocarbon rich retentate obtained in step 2) with a second membrane to obtain a hydrocarbon rich retentate and an acidic contaminants rich permeate,
4) compressing the acidic contaminants rich permeate obtained in step 3) up till a pressure between 30 and 120 bara, and
5) mixing the compressed permeate obtained in step 4) with the feedstream of step 1)
in which the permeate in step 3) contains less than 10 vol % of acidic contaminants.
13. The process according to claim 1 , comprising a pretreatment of the hydrocarbonaceous feedstream in order to remove water, the pretreatment being selected from a glycol treatment, a glycerol treatment or a molsieve treatment, the process optionally also comprising removal of C5+ compounds and/or C2-C4 compounds from the hydrocarbonaceous feedstream.
14. The process according to claim 1 , wherein the process optionally also comprising removal of C5+ compounds and/or C2-C4 compounds from the hydrocarbonaceous feedstream.
15. The process according to claim 12 , in which the acidic contaminants comprise one or more compounds selected from carbon dioxide and hydrogen sulphide.
16. The process according to claim 15 , in which the feedstream comprises carbon dioxide in an amount between 10 and 95 vol % based on the total feedstream, and in which the feedstream comprises hydrogen sulphide in an amount between 0 and 45 vol % based on the total feedstream.
17. The process according to claim 12 , in which the permeate obtained in step 2) has a pressure between 1 and 30 bara.
18. The process according to claim 12 , in which the permeate in step 2) has an acidic contaminants content of >90 vol % based on the total retentate stream.
19. The process according to claim 12 , in which the permeate in step 3) has an acidic contaminants content of between 40 and 90 vol% based on the total retentate stream.
20. The process according to claim 12 , in which the retentate in step 3) has a hydrocarbons content of more than 90 vol %, based on the retentate.