IP Library Granted Patent US 9,388,364
Granted Patent B1
US 9,388,364 · App. 14/738,563 · Granted Jul 12, 2016

Liquefaction processes and systems and liquefaction process intermediate compositions

Inventors: Andrew J. Schmidt (Richland, WA); Todd R. Hart (Kennewick, WA); Justin M. Billing (Richland, WA); Gary D. Maupin (Richland, WA); Richard T. Hallen (Richland, WA); Daniel B. Anderson (Pasco, WA)
Assignee: Battelle Memorial Institute
C11B1/12B01J19/24C11B3/008B01J2219/00051B01J2219/24
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Quick Facts
Patent No.
US 9,388,364
App. No.
14/738,563
Granted
Jul 12, 2016
Kind
B1
Abstract

Liquefaction processes are provided that can include: providing a biomass slurry solution having a temperature of at least 300° C. at a pressure of at least 2000 psig; cooling the solution to a temperature of less than 150° C.; and depressurizing the solution to release carbon dioxide from the solution and form at least part of a bio-oil foam. Liquefaction processes are also provided that can include: filtering the biomass slurry to remove particulates; and cooling and depressurizing the filtered solution to form the bio-oil foam. Liquefaction systems are provided that can include: a heated biomass slurry reaction zone maintained above 300° C. and at least 2000 psig and in continuous fluid communication with a flash cooling/depressurization zone maintained below 150° C. and between about 125 psig and about atmospheric pressure. Liquefaction systems are also provided that can include a foam/liquid separation system. Liquefaction process intermediate compositions are provided that can include a bio-oil foam phase separated from an aqueous biomass solids solution.

Claims (17)

1. A liquefaction process comprising:

providing a biomass slurry solution having a temperature of at least 300° C. at a pressure of at least 2000 psig;

cooling the solution to a temperature of less than 150° C.; and

depressurizing the solution to release carbon dioxide from the solution and form at least part of a bio-oil foam.

2. The liquefaction process of claim 1 further comprising separating the bio-oil foam from an aqueous solution.

3. The liquefaction process of claim 2 further comprising collapsing the bio-oil foam to a liquid.

4. The liquefaction process of claim 1 wherein the temperature of the biomass slurry is from about 300° C. to about 350° C.

5. The liquefaction process of claim 1 wherein the pressure applied to the biomass slurry solution is from about 2000 psig to about 3000 psig.

6. The liquefaction process of claim 1 wherein the solution is cooled to a temperature from about 20° C. to about 110° C.

7. A liquefaction process comprising:

providing a biomass slurry solution having a temperature of at least 300° C. at a pressure of at least 2000 psig;

filtering the slurry to remove particulates; and

cooling and depressurizing the filtered solution to release carbon dioxide from the solution and form at least part of a bio-oil foam.

8. The liquefaction process of claim 7 wherein the filtered solution is cooled to at least 150° C.

9. The liquefaction process of claim 7 wherein the filtered solution is depressurized to about atmospheric pressure.

10. The liquefaction process of claim 7 further comprising recovering the bio-oil foam and collapsing the foam to a liquid.

11. The liquefaction process of claim 10 wherein the recovering the bio-oil foam comprises removing the foam from an aqueous solution.

Assignments (2)
CONFIRMATORY LICENSE Recorded Nov 25, 2015
From: BATTELLE MEMORIAL INSTITUTE, PACIFIC NORTHWEST DIVISION
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 037138/0309 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 9, 2015
From: SCHMIDT, ANDREW J.; HART, TODD R.; BILLING, JUSTIN M.; MAUPIN, GARY D.; HALLEN, RICHARD T.; ANDERSON, DANIEL B.
To: BATTELLE MEMORIAL INSTITUTE
Reel/Frame 036049/0216 →