IP Library › Granted Patent US 8,507,740
Granted Patent B2
US 8,507,740 · App. 13/380,343 · Granted Aug 13, 2013

Biorefinery method

Inventor: Thomas Willner (Hamburg, DE)
Assignee: Nexxoil AG
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Quick Facts
Patent No.
US 8,507,740
App. No.
13/380,343
Granted
Aug 13, 2013
Kind
B2
Abstract

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.

Claims (16)

1. A method for producing a petrochemical product from biomass, involving the following steps:

a) dewatering and drying biomass;

b) producing crude oil by the direct liquefaction of the dried biomass;

c) hydrogenating the crude oil into hydrocarbons; and

d) refining the hydrocarbons into a petrochemical product, wherein

the hydrogen used for hydrogenating the crude oil is extracted from wastewater accumulated during dewatering and drying of the biomass and/or during direct liquefaction and from residue accumulated during the direct liquefaction.

2. The method according to claim 1 , wherein the hydrogen is produced by water vapor gasification and carbon monoxide conversion of wastewater and residue.

3. The method according to claim 1 , wherein the direct liquefaction is carried out in a heavy oil sump phase.

4. The method according to claim 1 , wherein the direct liquefaction is carried out in a regenerating heavy oil sump phase.

5. The method according to claim 1 , wherein the residue is taken from the heavy oil sump phase developing during the direct liquefaction.

6. The method according to claim 1 , wherein the direct liquefaction is carried out as a reactive distillation at atmospheric pressure and without catalytic converters.

7. The method according to claim 1 , wherein inorganic residue accumulated during hydrogen extraction is used for fertilizer production.

8. The method according to claim 1 , wherein the wastewater accumulated during the dewatering and drying of the biomass and/or during the direct liquefaction is used for biogas production.

9. The method according to claim 1 , wherein the gas accumulated during the production of crude oil is used for generation of energy.

10. The method according to claim 1 , wherein the biomass has plant or animal origin.

11. The method according to claim 1 , wherein the petrochemical product is a fuel or a heating oil.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 9, 2019
From: NEXXOIL AG
To: NEXXOIL GMBH
Reel/Frame 050011/0951 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 12, 2012
From: WILLNER, THOMAS
To: NEXXOIL AG
Reel/Frame 027843/0839 →
Priority Claims (1)
DE 10 2009 030 843 · Jun 26, 2009 · national
Continuity (1)
Related Publication 20120165582A1 · Jun 28, 2012