IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0063916
(2006-08-17)
|
등록번호 |
US-8673056
(2014-03-18)
|
우선권정보 |
EP-05076906 (2005-08-17) |
국제출원번호 |
PCT/NL2006/000427
(2006-08-17)
|
§371/§102 date |
20080728
(20080728)
|
국제공개번호 |
WO2007/021183
(2007-02-22)
|
발명자
/ 주소 |
- De Bas, Mathieu André
- Kuiper, Jacob
- De Pater, Jeroen
|
출원인 / 주소 |
- Gastreatment Services B.V.
|
대리인 / 주소 |
|
인용정보 |
피인용 횟수 :
0 인용 특허 :
10 |
초록
▼
The invention is directed to processes and apparatuses for gas treatment, in particular for the purification of methane rich gas streams, such as gas obtained from the conversion from organic matter (“biogas”). In accordance with the present invention there is provided an apparatus and a process for
The invention is directed to processes and apparatuses for gas treatment, in particular for the purification of methane rich gas streams, such as gas obtained from the conversion from organic matter (“biogas”). In accordance with the present invention there is provided an apparatus and a process for producing a purified methane comprising gas stream (P) from a methane containing gas stream (A), comprising the steps of: (a) pressurising said methane containing gas stream (A) and subsequently cooling it, whereby a stream comprising condensed contaminants (C) and a methane comprising stream (B) are obtained; (b) optionally feeding said methane comprising stream (B) to an adsorption unit and/or a catalytic conversion unit, whereby the concentration of contaminants in stream (B) is further decreased; and (c) cooling the methane comprising stream (B) to a temperature which is sufficient to condensate CO2 from said stream (B), whereby said purified methane comprising gas stream (P) is obtained.
대표청구항
▼
1. Process for producing a purified methane comprising gas stream (P) from a methane containing gas stream (A), comprising the steps of: (a) pressurizing said methane containing gas stream (A) and subsequently cooling it, whereby a stream comprising condensed contaminants (C) and a methane comprisin
1. Process for producing a purified methane comprising gas stream (P) from a methane containing gas stream (A), comprising the steps of: (a) pressurizing said methane containing gas stream (A) and subsequently cooling it, whereby a stream comprising condensed contaminants (C) and a methane comprising stream (B) are obtained, wherein said methane comprising stream (B) includes an amount of CO2;(b) optionally feeding said methane comprising stream (B) to an adsorption unit or a catalytic conversion unit, whereby the concentration of contaminants in stream (B) is further decreased;(c) cooling the methane comprising stream (B) to a temperature, whereby condensated CO2 is formed; and(d) removing said condensated CO2 from said methane comprising stream (B),whereby said purified methane comprising gas stream (P) and a condensated CO2 stream are obtained. 2. Process according to claim 1, wherein, in step (a), said methane containing gas stream (A) is cooled to a temperature of −25° C. or less. 3. Process according to claim 1, wherein said cooling in step (a) is carried out by feeding methane containing gas stream (A) to a first heat exchanger, while at the same time a second heat exchanger is allowed to defrost, optionally followed by switching said first heat exchanger and said second heat exchanger. 4. Process according to claim 3, wherein said first heat exchanger and said second heat exchanger are allowed to exchange heat between them. 5. Process according to claim 3, wherein said stream comprising condensed contaminants (C) is obtained from said second heat exchanger that is allowed to defrost. 6. Process according to claim 1, wherein said stream comprising condensed contaminants (C) comprises siloxanes. 7. Process according to claim 1, wherein said stream comprising condensed contaminants (C) comprises contaminants selected from the group consisting of water, H2S, SO2, halogen compounds, any hydrocarbon higher than methane and combinations thereof. 8. Process according to claim 1, wherein in step (c) said methane comprising stream (B) is cooled to a temperature of about −60° C. 9. Process according to claim 8, which is followed by a step, wherein said methane comprising stream (B) is cooled to a CO2 vapour/liquid equilibrium temperature of −80° C. or less. 10. Process according to claim 1, wherein in step (b) said methane comprising stream (B) is fed to an adsorption unit and a catalytic conversion unit. 11. Process according to claim 10, wherein said adsorption unit and said catalytic conversion unit comprise a single unit comprising a bed of solid particles. 12. Process according to claim 1, wherein said methane containing gas stream (A) is a biogas, preferably obtained from a landfill, a digester, a wastewater treatment facility, or a combination thereof. 13. Apparatus for producing a purified methane comprising gas stream (P) from a methane containing gas stream (A), comprising: (a) a compressor for pressurizing said methane containing gas stream (A), wherein said methane containing gas stream (A) includes an amount of CO2; and a cooler unit located downstream of said compressor;(b) optionally an adsorption unit or a catalyst conversion unit located downstream from said compressor and said cooler unit; and(c) a second cooler unit connected to said adsorption unit or said catalyst conversion unit by piping for cooling said methane containing gas stream (A) to form condensated CO2, said second cooler unit comprising an outlet for condensated CO2, wherein said condensated CO2 is equal to at least about half the amount of CO2, and an outlet for said purified gas stream (P), wherein said second cooler unit comprises a first heat exchanger, and a second heat exchanger, which may be operated in parallel. 14. Apparatus according to claim 13, wherein said cooler unit under (a) comprises a first heat exchanger, and a second heat exchanger, which may be operated in parallel. 15. Apparatus according to claim 13, wherein the piping downstream of part (b) does not have any heat tracing or insulation. 16. Apparatus according to claim 13, wherein the said second cooler unit and said adsorption unit or said catalyst conversion unit downstream of part (a) are constructed from SS304, carbon steel, or combinations thereof. 17. Process according to claim 1, wherein said stream comprising condensed contaminants (C) comprises contaminants selected from the group consisting of water, H2S, SO2, halogen compounds, C5 and higher hydrocarbons, and combinations thereof.
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