IP Library Granted Patent US 10,138,426
Granted Patent B2
US 10,138,426 · App. 15/693,354 · Granted Nov 27, 2018

Combined hydrothermal liquefaction and catalytic hydrothermal gasification system and process for conversion of biomass feedstocks

Inventors: Douglas C. Elliott (Richland, WA); Gary G. Neuenschwander (Burbank, WA); Todd R. Hart (Kennewick, WA)
Assignee: Battelle Memorial Institute
C10B49/16C10G1/06C10G1/065C10G3/40C10G3/50C10J3/00C10L3/08C10L9/08C10L9/086C10J2200/06C10J2300/0916C10J2300/0973C10J2300/1681Y02E50/14Y02P20/145Y02P30/20
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Quick Facts
Patent No.
US 10,138,426
App. No.
15/693,354
Granted
Nov 27, 2018
Kind
B2
Abstract

A combined hydrothermal liquefaction (HTL) and catalytic hydrothermal gasification (CHG) system and process are described that convert various biomass-containing sources into separable bio-oils and aqueous effluents that contain residual organics. Bio-oils may be converted to useful bio-based fuels and other chemical feedstocks. Residual organics in HTL aqueous effluents may be gasified and converted into medium-BTU product gases and directly used for process heating or to provide energy.

Claims (9)

1. A continuous process, comprising the steps of:

providing a biomass conversion product comprising a bio oil fraction and an aqueous fraction, wherein each fraction is separable from the other fraction;

continuously separating the bio oil fraction from the aqueous fraction by coalescing bio oil droplets, wherein said coalescence takes place at a temperature from ambient to about 360° C. and a pressure between about 100 atm and 210 atm; and

converting at least a portion of the aqueous fraction to a product gas containing a fuel gas.

2. The process of claim 1 , further comprising removing solids from the biomass conversion product.

3. The process of claim 1 , further comprising combusting the product gas to generate power.

4. The process of claim 1 , wherein the product gas comprises one or more of methane, hydrocarbons with a carbon number greater than that of methane, and carbon dioxide.

5. The process of claim 1 , wherein the continuously separating is performed in a self-cleaning apparatus.

6. The process of claim 1 , wherein the continuously separating is performed within a closed stage apparatus.

Continuity (3)
Continuation 13893011 · May 13, 2013
Provisional Application 61657416 · Jun 8, 2012
Related Publication 20180023003A1 · Jan 25, 2018