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Extract from the Register of European Patents

EP About this file: EP4243961

EP4243961 - TWO STEP AMINE ABSORPTION PROCESS FOR REMOVAL CO2/H2S FROM BIOGAS [Right-click to bookmark this link]
StatusRequest for examination was made
Status updated on  18.08.2023
Database last updated on 02.11.2024
FormerThe international publication has been made
Status updated on  21.05.2022
Formerunknown
Status updated on  26.11.2021
Most recent event   Tooltip30.09.2024New entry: Renewal fee paid 
Applicant(s)For all designated states
Airco Process Technology A/S
Prins Georgs Kvarter 1 Snoghøj
7000 Fredericia / DK
[2023/38]
Inventor(s)01 / FIND, Rasmus
7100 Vejle / DK
 [2023/38]
Representative(s)AWA Denmark A/S
Strandgade 56
1401 Copenhagen K / DK
[2023/38]
Application number, filing date21807133.016.11.2021
[2023/38]
WO2021EP81882
Priority number, dateEP2020020783416.11.2020         Original published format: EP 20207834
[2023/38]
Filing languageEN
Procedural languageEN
PublicationType: A1 Application with search report
No.:WO2022101509
Date:19.05.2022
Language:EN
[2022/20]
Type: A1 Application with search report 
No.:EP4243961
Date:20.09.2023
Language:EN
The application published by WIPO in one of the EPO official languages on 19.05.2022 takes the place of the publication of the European patent application.
[2023/38]
Search report(s)International search report - published on:EP19.05.2022
ClassificationIPC:B01D53/14
[2023/38]
CPC:
B01D53/1406 (EP,US); B01D53/1425 (US); B01D53/1462 (US);
B01D53/1468 (EP); B01D53/1475 (EP); B01D53/1493 (EP);
B01D53/526 (US); B01D53/62 (US); B01D53/78 (US);
B01D53/96 (US); C10L3/103 (US); C10L3/104 (US);
B01D2252/20405 (US); B01D2252/20421 (US); B01D2252/20431 (US);
B01D2252/20478 (EP); B01D2252/20484 (US); B01D2252/20489 (US);
B01D2256/245 (EP,US); B01D2257/304 (US); B01D2257/504 (US);
B01D2258/05 (EP,US); Y02A50/20 (EP); Y02C20/40 (EP) (-)
Designated contracting statesAL,   AT,   BE,   BG,   CH,   CY,   CZ,   DE,   DK,   EE,   ES,   FI,   FR,   GB,   GR,   HR,   HU,   IE,   IS,   IT,   LI,   LT,   LU,   LV,   MC,   MK,   MT,   NL,   NO,   PL,   PT,   RO,   RS,   SE,   SI,   SK,   SM,   TR [2023/38]
TitleGerman:ZWEISTUFIGES AMINABSORPTIONSVERFAHREN ZUR ENTFERNUNG VON CO2/H2S AUS BIOGAS[2023/38]
English:TWO STEP AMINE ABSORPTION PROCESS FOR REMOVAL CO2/H2S FROM BIOGAS[2023/38]
French:PROCÉDÉ D'ABSORPTION D'AMINE EN DEUX ÉTAPES POUR ÉLIMINER LE CO2/H2S D'UN BIOGAZ[2023/38]
Entry into regional phase09.06.2023National basic fee paid 
09.06.2023Designation fee(s) paid 
09.06.2023Examination fee paid 
Examination procedure09.06.2023Examination requested  [2023/38]
09.06.2023Date on which the examining division has become responsible
14.12.2023Amendment by applicant (claims and/or description)
Fees paidRenewal fee
12.10.2023Renewal fee patent year 03
30.09.2024Renewal fee patent year 04
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Cited inInternational search[XY]US4557911  (GODDIN JR CLIFTON S [US], et al) [X] 1-6,9-14,20-23,25-27 * see, in particular, figure 3 items 4,8,10,12 for two step absorption and items 23,70,72,122,94 and 102 for regeneration and recycle of absorbent; see also table 1 : P(2)=50 psia; P(16)= 292 psia; see table 3 compressor (item 8). * [Y] 1-27;
 [Y]US2004060334  (PALMER GARY [CA]) [Y] 1-27 * see figures 5 and 6 sour gas into first absorber 20 and acid gas 16 compressed by compressor 46 into second absorber 30; also figure 7 sour gas to first (high pressure) absorber 20 and recycled acid gas compressed into second absorber and recycled acid gas compressed into third absorber *;
 [A]US2007006731  (MENZEL JOHANNES [DE]) [A] 1-27* see, in particular, first absorbent column 2; second absorbent column 13 *;
 [A]  - AROONWILAS ADISORN ET AL, "Mass Transfer Coefficients and Correlation for CO 2 Absorption into 2-Amino-2-methyl-1-propanol (AMP) Using Structured Packing", IND. ENG. CHEM. RES., (19981231), vol. 37, pages 569 - 575, XP055774688 [A] 1-27 * see, in particular, figure 2 and page 571, right column , last 8 lines. *
 [A]  - ISA F. ET AL, "An overview on CO 2 removal via absorption: Effect of elevated pressures in counter-current packed column", JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, AMSTERDAM, NL, (20160701), vol. 33, doi:10.1016/j.jngse.2016.06.003, ISSN 1875-5100, pages 666 - 677, XP055774770 [A] 1-27 * see, in particular, table 4 , left column, pressure (bar). *

DOI:   http://dx.doi.org/10.1016/j.jngse.2016.06.003
 [A]  - ABDUL HALIM HAIRUL N. ET AL, "Mass Transfer Performance of CO 2 Absorption from Natural Gas using Monoethanolamine (MEA) in High Pressure Operations", vol. 54, no. 5, doi:10.1021/ie504024m, ISSN 0888-5885, (20150202), pages 1675 - 1680, INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, URL: https://pubs.acs.org/doi/pdf/10.1021/ie504024m, XP055774669 [A] 1-27 * see, in particular table 1 pressure data and table 2 pressure data *

DOI:   http://dx.doi.org/10.1021/ie504024m
 [A]  - AROONWILAS A ET AL, "High-efficiency structured packing for CO2 separation using 2-amino-2-methyl-1-propanol (AMP)", SEPARATION AND PURIFICATION TECHNOLOGY, (19970101), vol. 12, pages 67 - 79, XP055774692 [A] 1-27 * see in particular figure 4 and point 5.1 "Effect of CO2 partial pressure" *
by applicantDE102009056660
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