The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 07, 2024

Filed:

Dec. 16, 2020
Applicant:

Steeper Energy Aps, Vedbæk, DK;

Inventors:

Steen Brummerstedt Iversen, Vedbæk, DK;

Claus Uhrenholt Jensen, Vodskov, DK;

Henrik Egholm, Hjørring, DK;

Anders Bach Velling, Aalborg, DK;

Esben Ravn, Aalborg, DK;

Assignee:

STEEPER ENERGY APS, Vedbaek, DK;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 53/04 (2006.01); C10G 53/10 (2006.01);
U.S. Cl.
CPC ...
C10G 53/04 (2013.01); C10G 53/10 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/201 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01); C10G 2300/802 (2013.01);
Abstract

The invention relates to a method of separating and purifying products from a hydrothermal and/or solvothermal conversion process of carbonaceous material adapted to convert a feed stream comprising carbonaceous material at a pressure of at least 100 bar and a temperature of at least 300° C., where the converted feed stream (product mixture) comprises a mixture of COcontaining gas, an oil phase, an aqueous phase comprising water soluble organics and dissolved salts, and inorganic solid phase; where the product mixture is cooled to a temperature in the range 40 to 250° C., and depressurized to a pressure in the range 1 to 30 bar, the method comprising—separating a gas comprising COfrom the product mixture in a degasser such as a flash separator, and—separating a water phase from the at least partly degassed converted feed mixture in a first separation step of the separation, and adding washing agents in the form of an acidifying agent and a diluent to the at least partly degassed and at least partly dewatched product mixture, and separating the mixture with added washing agents into an oil rich phase, a water rich phase and a solid rich phase in a second step of the separation process, and further at least partly recovering the diluent from the oil rich phase.


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