IP Library Granted Patent US 8,979,955
Granted Patent B2
US 8,979,955 · App. 13/029,188 · Granted Mar 17, 2015

Production of pyrolysis oil

Inventors: Foster A. Agblevor (Logan, UT); Nii Ofei Mante (Blacksburg, VA)
Assignee: Virginia Tech Intellectual Properties, Inc.
C10B47/24C10B53/02C10C5/00C10L1/00C10G3/49B01J27/053B01J29/40Y02E50/14Y02E50/32C10G2300/1059C10G2400/02C10G2400/04C10G2400/08
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Quick Facts
Patent No.
US 8,979,955
App. No.
13/029,188
Granted
Mar 17, 2015
Kind
B2
Abstract

Methods for fractional catalytic pyrolysis which allow for conversion of biomass into a slate of desired products without the need for post-pyrolysis separation are described. The methods involve use of a fluid catalytic bed which is maintained at a suitable pyrolysis temperature. Biomass is added to the catalytic bed, preferably while entrained in a non-reactive gas such as nitrogen, causing the biomass to become pyrolyzed and forming the desired products in vapor and gas forms, allowing the desired products to be easily separated.

Claims (26)

1. A process for producing pyrolysis oil comprising the steps of:

providing a reactor containing multiple catalysts having different densities and different particle size distributions;

fluidizing the catalysts;

entraining a biomass in the fluidized catalysts, so that the biomass is pyrolyzed; and

collecting the resultant pyrolysis oil.

2. The process of claim 1 , wherein the catalysts are zeolite catalysts.

3. The process of claim 1 , wherein the catalyst is heated to a temperature of about 400° C. to about 650° C.

4. The process of claim 1 , wherein the increase in viscosity of the pyrolysis oil over the course of two years is less than 50%.

5. A process for producing fuel comprising the steps of

providing a reactor containing multiple catalysts having different densities and different particle size distributions;

fluidizing the catalysts;

entraining a biomass in the fluidized catalysts, so that the biomass is pyrolyzed to produce pyrolysis oil; and

cracking the pyrolysis oil.

6. The process of claim 5 , wherein the catalysts are zeolite catalysts.

7. The process of claim 5 , wherein the catalyst is heated to a temperature of about 400° C. to about 650° C.

8. The process of claim 5 , wherein the increase in viscosity of the oil over the course of two years is less than 50%.

9. The process of claim 5 , further comprising the step of blending the pyrolysis oil with gas oil prior to the cracking step to produce an oil blend.

10. The process of claim 9 , wherein the oil blend contains about 5-45% by weight pyrolysis oil.

11. The process of claim 5 , wherein the fuel is a drop-in fuel.

12. A process for producing fuel comprising the steps of

producing pyrolysis oil using the process of claim 1 ;

blending the pyrolysis oil with gas oil to produce an oil blend; and

cracking the oil blend.

13. The process of claim 12 , wherein the increase in viscosity of the pyrolysis oil over the course of two years is less than 50%.

14. The process of claim 12 , wherein the fuel is a drop-in fuel.

15. The process of claim 12 , wherein the fuel is gasoline, diesel, or jet fuel.

Assignments (2)
CONFIRMATORY LICENSE Recorded May 5, 2020
From: VIRGINIA POLYTECHNIC INST AND ST UNIV
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 052578/0425 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 17, 2012
From: AGBLEVOR, FOSTER A.; MANTE, NII OFEI
To: VIRGINIA POLYTECHNIC INSTITUTE AND STATE UNIVERSITY
Reel/Frame 027725/0070 →
Continuity (5)
Continuation In Part 12691385 · Jan 21, 2010
Continuation In Part 12184757 · Aug 1, 2008
Provisional Application 61305188 · Feb 17, 2010
Provisional Application 60953266 · Aug 1, 2007
Related Publication 20110213188A1 · Sep 1, 2011