EP 4161869 A1 20230412 - METHOD AND REACTOR FOR PRODUCING SYNTHESIS GAS FROM A CARBON AND HYDROGEN SOURCE IN THE PRESENCE OF AN OXY FLAME
Title (en)
METHOD AND REACTOR FOR PRODUCING SYNTHESIS GAS FROM A CARBON AND HYDROGEN SOURCE IN THE PRESENCE OF AN OXY FLAME
Title (de)
VERFAHREN UND REAKTOR ZUR HERSTELLUNG VON SYNTHESEGAS AUS EINER KOHLENSTOFF- UND WASSERSTOFFQUELLE IN GEGENWART EINER OXYFLAMME
Title (fr)
MÉTHODE ET RÉACTEUR POUR LA PRODUCTION DE GAZ DE SYNTHÈSE À PARTIR D'UNE SOURCE DE CARBONE ET D'HYDROGÈNE EN PRÉSENCE D'UNE OXY-FLAMME
Publication
Application
Priority
- CA 3081971 A 20200604
- CA 2021050761 W 20210603
Abstract (en)
[origin: CA3166916A1] The technology relates to a method for producing synthesis gas comprising carbon monoxide (CO) and hydrogen (H2), in which method the synthesis gas is produced by a reduction reaction of a first flow comprising a carbon source and an excess of hydrogen in contact with an oxy flame. The hydrogen originates from a reducing stream a first portion of which is located in the first flow and a second portion of which is used to generate the oxy flame by combusting the hydrogen in the presence of a second flow comprising oxygen (O2), the second flow originating from an oxidising stream. The first flow and the second flow are at a distance from each other such that the oxy flame supports the reaction between the carbon source and the hydrogen. A reactor which can have different configurations is also proposed for implementing the method.
IPC 8 full level
C01B 3/02 (2006.01); B01J 19/24 (2006.01); C10L 3/00 (2006.01)
CPC (source: EP KR US)
B01J 4/002 (2013.01 - EP KR); B01J 19/0006 (2013.01 - EP KR); B01J 19/0013 (2013.01 - US); B01J 19/2415 (2013.01 - US); B01J 19/244 (2013.01 - EP KR); C01B 3/02 (2013.01 - EP); C01B 3/12 (2013.01 - US); C01B 3/36 (2013.01 - EP KR); C01B 3/363 (2013.01 - US); C10G 2/32 (2013.01 - EP KR); C10G 2/34 (2013.01 - US); C10G 47/22 (2013.01 - EP KR); C10K 3/008 (2013.01 - EP); C10K 3/026 (2013.01 - EP KR US); B01J 2219/00155 (2013.01 - EP); B01J 2219/00157 (2013.01 - US); B01J 2219/00159 (2013.01 - EP); B01J 2219/00164 (2013.01 - EP); C01B 2203/0238 (2013.01 - EP); C01B 2203/0255 (2013.01 - KR US); C01B 2203/0283 (2013.01 - US); C01B 2203/0816 (2013.01 - KR); C01B 2203/0822 (2013.01 - US); C01B 2203/1241 (2013.01 - US); Y02E 60/36 (2013.01 - EP); Y02P 20/141 (2015.11 - EP)
Designated contracting state (EPC)
AL 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
Designated extension state (EPC)
BA ME
Designated validation state (EPC)
KH MA MD TN
DOCDB simple family (publication)
CA 3081971 A1 20211204; AU 2021283462 A1 20230202; BR 112022023777 A2 20221220; CA 3166916 A1 20211209; CA 3166916 C 20230912; CN 115667128 A 20230131; EP 4161869 A1 20230412; JP 2023529629 A 20230711; KR 20230019463 A 20230208; US 11999618 B2 20240604; US 2023249969 A1 20230810; US 2024279055 A1 20240822; WO 2021243462 A1 20211209
DOCDB simple family (application)
CA 3081971 A 20200604; AU 2021283462 A 20210603; BR 112022023777 A 20210603; CA 2021050761 W 20210603; CA 3166916 A 20210603; CN 202180039534 A 20210603; EP 21818956 A 20210603; JP 2022574558 A 20210603; KR 20227046278 A 20210603; US 202118007973 A 20210603; US 202418644830 A 20240424