IP Library Granted Patent US 8,436,120
Granted Patent B2
US 8,436,120 · App. 11/943,422 · Granted May 7, 2013

Method of producing hodge carbonyls and oligomeric lignin

Inventors: Jan Piskorz (Waterloo, CA); Piotr Majerski (Waterloo, CA)
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Quick Facts
Patent No.
US 8,436,120
App. No.
11/943,422
Granted
May 7, 2013
Kind
B2
Abstract

A method of treating biomass feed by pyrolyzing it in the presence of superheated steam at a selected temperature for a sufficient time to produce at least one product stream.

Claims (21)

1. An improved fast pyrolysis method of the type used to decompose biomass into a non-bio-oil product, said fast pyrolysis method characterized by the steps of i) combining the biomass, a carrier gas, and a particulate solid source of heat in a pyrolysis chamber, ii) allowing the biomass to decompose during an apparent vapor residence time, and ii) collecting a product, wherein the improvement comprises the steps of:

Step (a) directing superheated steam into the pyrolysis chamber;

Step (b) applying to the pyrolysis chamber sufficient heat from an external source to raise the temperature in the chamber to at least about 430° C.;

Step (c) collecting a stream containing char;

Step (d) collecting an aerosol stream;

Step (e) producing a gas stream and a condensables stream from the aerosol stream of Step (d); and,

Step (f) separating the condensables stream of Step (e) into i) an aqueous product stream and ii) oligomeric lignin.

2. The improved method of claim 1 , wherein the aqueous product stream of Step (f) includes at least one Hodge' carbonyl.

3. The improved method of claim 1 , wherein the aqueous product stream of Step (f) includes at least one product selected from the group consisting of hydroxyacetaldehyde, glyceraldehydes, acetol, pyruvaldehyde, glyoxal, 5-hydroxymethylfurfural, furfurals, formaldehyde, and water-soluble phenolics.

4. The improved method of claim 1 wherein the apparent vapor residence time is approximately 1 second.

5. The improved method of claim 4 wherein the temperature of Step (b) is between approximately 430° C. and approximately 570° C.

6. The improved method of claim 1 wherein the temperature of Step (b) is between approximately 430° C. and approximately 570° C.

7. The improved method of claim 1 wherein the biomass includes a cellulosic material.

8. The improved method of claim 7 wherein the cellulosic material is selected from the group consisting of cellulosic pulps, cellulosic sludges, and micro-crystalline cellulose powders.

9. The improved method of claim 1 wherein the biomass includes at least one lignocellulosic material.

10. The improved method of claim 9 wherein the heat applied at Step (b) is sufficient to produce a temperature in the pyrolysis chamber in the range of approximately 430° C. to approximately 550° C.

11. The improved method of claim 1 further comprising:

Step (g) absorbing the oligomeric lignin of Step (f) onto the char of Step (c) whereby a composite of the oligomeric lignin and the char is produced.

12. Oligomeric lignin produced by the method of claim 1 .

13. A solid fertilizer having a coating, wherein said coating comprises the oligomeric lignin of claim 1 .

14. The composite of oligomeric lignin and char produced by the improved method of claim 11 .

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 21, 2022
From: KERRY LUXEMBOURG S.A.R.L.
To: KERRY GROUP SERVICES INTERNATIONAL LIMITED
Reel/Frame 058792/0891 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 21, 2018
From: RESOURCE TRANSFORMS INTERNATIONAL LTD.
To: KERRY LUXEMBOURG S.A.R.L.
Reel/Frame 046650/0122 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 4, 2018
From: PISKORZ, JAN; MAJERSKI, PIOTR
To: RESOURCE TRANSFORMS INTERNATIONAL LTD.
Reel/Frame 045719/0838 →
Continuity (1)
Related Publication 20090126433A1 · May 21, 2009