IP Library Granted Patent US 10,519,047
Granted Patent B2
US 10,519,047 · App. 13/335,683 · Granted Dec 31, 2019

Process and system for production of synthesis gas

Inventors: Dennis E. J. Johnson (Colorado Springs, CO); Grigori A. Abramov (Littleton, CO); Richard A. Kleinke (Commerce City, CO); Marcus A. Wiley (Highlands Ranch, CO)
Assignee: Thermo Technologies, LLC
C02F1/32C10B1/10C10J3/66C10K1/101C10J2300/0903C10J2300/093C10J2300/0916C10J2300/0943C10J2300/0946Y02E50/32Y02P20/145
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Quick Facts
Patent No.
US 10,519,047
App. No.
13/335,683
Granted
Dec 31, 2019
Kind
B2
Abstract

Methods and apparatus may permit the generation of consistent output synthesis gas from highly variable input feedstock solids carbonaceous materials. A stoichiometric objectivistic chemic environment may be established to stoichiometrically control carbon content in a solid carbonaceous materials gasifier system. Processing of carbonaceous materials may include dominative pyrolytic decomposition and multiple coil carbonaceous reformation. Dynamically adjustable process determinative parameters may be utilized to refine processing, including process utilization of negatively electrostatically enhanced water species, process utilization of flue gas, and adjustment of process flow rate characteristics. Recycling may be employed for internal reuse of process materials, including recycled negatively electrostatically enhanced water species, recycled flue gas, and recycled contaminants. Synthesis gas generation may involve predetermining a desired synthesis gas for output and creating high yields of such a predetermined desired synthesis gas.

Claims (19)

1. A gasifier system comprising:

i) a pyrolysis chamber configured to be operated within a desired elevated pressure range and within a desired elevated temperature range;

ii) at least one mechanically propelled rotating carousel platform configured for the decomposition of carbonaceous materials by pyrolysis and at least one mechanically propelled rotating carousel platform configured for the steam reformation of said pyrolytically decomposed carbonaceous materials positioned within the pyrolysis chamber and configured to be operated within substantially the same pressure range as the pyrolysis chamber;

the pyrolysis chamber being mounted in a spaced apart relationship from a thermal circumscribing heat shield encasement, said spaced apart relationship defining a space between the pyrolysis chamber and the thermal circumscribing heat shield encasement; the pyrolysis chamber being configured for mixing and advancing a carbonaceous material disposed therein; and

iii) a heating system configured to heat the space and the pyrolysis chamber, while maintaining a cool exterior to the thermal circumscribing heat shield encasement.

2. The gasifier system of claim 1 , further including:

i) at least one delivery system configured for supplying a quantity of the carbonaceous material to the pyrolysis chamber at an elevated pressure; and

ii) at least one drive mechanism configured for rotating the at least one mechanically propelled rotating carousel platform configured for the decomposition of carbonaceous materials by pyrolysis and the at least one mechanically propelled rotating carousel platform configured for the steam reformation of said pyrolytically decomposed carbonaceous materials within the pyrolysis chamber.

3. The gasifier of claim 2 , wherein the drive mechanism is configured to allow for adjustment to a speed of axial rotation of the at least one mechanically propelled rotating carousel platform configured for the decomposition of carbonaceous materials by pyrolysis and the at least one mechanically propelled rotating carousel platform configured for the steam reformation of said pyrolytically decomposed carbonaceous materials.

4. The gasifier of claim 2 , wherein the delivery system is configured to deliver the carbonaceous material into the pyrolysis chamber under an elevated pressure, whereby pressures within the space and the pyrolysis chamber are not lowered below desired operating ranges.

5. The gasifier of claim 2 , wherein the delivery system includes a pressurizing system having a pressurizing chamber and a pair of opposing first and second gate valves; the first and second gate valves being configured for delivering a supply of the carbonaceous material at an elevated pressure into the pyrolysis chamber.

6. The gasifier of claim 1 , wherein the pyrolysis chamber and the space are configured to be operated at substantially the same elevated pressure.

7. The gasifier of claim 1 , wherein the at least one mechanically propelled rotating carousel platform configured for the decomposition of carbonaceous materials by pyrolysis and the at least one mechanically propelled rotating carousel platform configured for the steam reformation of said pyrolytically decomposed carbonaceous materials are configured to rotate about a longitudinal axis.

8. The gasifier of claim 1 , wherein the pyrolysis chamber includes at least one outlet port configured for allowing at least one product to be removed from the pyrolysis chamber.

9. The gasifier of claim 1 , wherein the pyrolysis chamber includes at least one discharge assembly configured for allowing disposal of at least one byproduct to be removed from the pyrolysis chamber.

10. The gasifier of claim 1 , wherein the pyrolysis chamber contains one or more flights positioned along an interior surface of the pyrolysis chamber; the flights being configured for mixing and advancing the carbonaceous material through the pyrolysis chamber.

11. The gasifier of claim 1 , wherein the heating system is configured to deliver a varying amount of heat to one or more zones within the pyrolysis chamber.

12. The gasifier of claim 1 , wherein the heating system is configured for supplying different amounts of heat to the at least one mechanically propelled rotating carousel platform configured for the decomposition of carbonaceous materials by pyrolysis and the at least one mechanically propelled rotating carousel platform configured for the steam reformation of said pyrolytically decomposed carbonaceous materials.

13. The gasifier of claim 1 , further including a heat exchanger system configured to capture heat from the system.

Assignments (2)
LICENSE Recorded Feb 2, 2016
From: THERMO TECHNOLOGIES, LLC
To: THERMO CONVERSIONS, LLC
Reel/Frame 037642/0600 →
NUNC PRO TUNC ASSIGNMENT Recorded Jan 19, 2012
From: JOHNSON, DENNIS E.J.; ABRAMOV, GRIGORI A.; KLEINKE, RICHARD A.; WILEY, MARCUS A.
To: THERMO TECHNOLOGIES, LLC
Reel/Frame 027561/0672 →
Continuity (6)
Continuation 13110784 · May 18, 2011
Continuation 12246395 · Oct 6, 2008
Continuation PCTUS2007066466 · Apr 11, 2007
Continuation 12296202
Provisional Application 60791401 · Apr 11, 2006
Related Publication 20120096768A1 · Apr 26, 2012
Cited By (11)
US 12,410,370 US 12,435,278 US 12,453,993 US 12,453,994 US 12,473,506 US 12,509,636 US 12,545,840 US 12,559,682 US 12,595,424 US 12,649,879 US 12,661,631