54 |
Titel |
TI |
[EN] BIOREFINERY METHOD |
71/73 |
Anmelder/Inhaber |
PA |
NEXXOIL AG, CH
;
WILLNER THOMAS, DE
|
72 |
Erfinder |
IN |
WILLNER THOMAS, DE
|
22/96 |
Anmeldedatum |
AD |
22.06.2010 |
21 |
Anmeldenummer |
AN |
201013380343 |
|
Anmeldeland |
AC |
US |
|
Veröffentlichungsdatum |
PUB |
28.06.2012 |
33 31 32 |
Priorität |
PRC PRN PRD |
DE
102009030843
26.06.2009
|
33 31 32 |
PRC PRN PRD |
DE
2010000705
22.06.2010
|
51 |
IPC-Hauptklasse |
ICM |
C10L 1/00
(2006.01)
|
51 |
IPC-Nebenklasse |
ICS |
|
|
IPC-Zusatzklasse |
ICA |
|
|
IPC-Indexklasse |
ICI |
|
|
Gemeinsame Patentklassifikation |
CPC |
C10G 1/002
C10G 2300/1014
C10G 2300/1018
C10G 2300/42
C10G 49/007
Y02P 30/20
|
|
MCD-Hauptklasse |
MCM |
C10L 1/00
(2006.01)
|
|
MCD-Nebenklasse |
MCS |
|
|
MCD-Zusatzklasse |
MCA |
|
57 |
Zusammenfassung |
AB |
[EN] The invention relates to a method for producing a petrochemical product from biomass, involving the following steps: dewatering and drying biomass; producing crude oil by the direct liquefaction of the dried biomass; hydrogenating the crude oil into hydrocarbons; and refining the hydrocarbons into a petrochemical product. Said method is characterized in that the hydrogen used for hydrogenating the crude oil is obtained from the wastewater accumulated during the dewatering and drying of the biomass and/or during the direct liquefaction and from the residue accumulated during the direct liquefaction. |
56 |
Entgegengehaltene Patentdokumente/Zitate, in Recherche ermittelt |
CT |
US000008119583B2
|
56 |
Entgegengehaltene Patentdokumente/Zitate, vom Anmelder genannt |
CT |
|
56 |
Entgegengehaltene Nichtpatentliteratur/Zitate, in Recherche ermittelt |
CTNP |
|
56 |
Entgegengehaltene Nichtpatentliteratur/Zitate, vom Anmelder genannt |
CTNP |
|
|
Zitierende Dokumente |
|
Dokumente ermitteln
|
|
Sequenzprotokoll |
|
|
|
Prüfstoff-IPC |
ICP |
C10L 1/00
|