Engine concepts for handling producer gas from biomass

Patent metadata

Field	Value
Publication number	US-11236279-B2
Application number	US-201716471077-A
Country	US
Kind code	B2
Filing date	Dec 20, 2017
Priority date	Dec 21, 2016
Publication date	Feb 1, 2022
Grant date	Feb 1, 2022

Abstract

Internal combustion engines tolerant to tar-containing producer gas are disclosed. Two concepts are described. The engines are tolerant to producer gas from a biomass gasifier with minimal pretreatment. When biomass is gasified to be burned for power generation or to be used to synthesize chemicals such as biofuels, a large fraction of the installation cost is spent on equipment to clean up the heavy organic components (also referred to as ‘tars’) from the gas stream, hereafter referred to as ‘producer gas’. The invention described herein may be used to enable power generation from gasified biomass with minimal treatment. It may also be used to treat biomass at a very low cost for other uses such as synthesizing chemicals. The producer gas is not necessarily limited to biomass derived. Producer gas derived from coal or other sources has similar issues and the invention described herein would be equally applicable.

First claim

What is claimed is:

1. A system for producing power from a producer gas, wherein the producer gas comprises heavy organic components known as tar, comprising:
a clean-up engine, comprising one or more cylinders, wherein an input to the one or more cylinders of the clean-up engine comprises a rich mixture of the producer gas and an oxygen-containing gas, wherein the producer gas enters the clean-up engine at a temperature greater than a dew point of the tar, wherein the tar is not removed from the producer gas prior to entering the clean-up engine and wherein the clean-up engine exhausts a cleaned producer gas;
a power engine, comprising one or more cylinders, where the cleaned producer gas exhausted from the clean-up engine is directed to the one or more cylinders of the power engine; and
a generator that produces power due to rotation of a driveshaft in the power engine.

2. The system of claim 1 , wherein the clean-up engine lacks an ignition source and relies on increased pressure of the rich mixture to cause ignition.

3. The system of claim 1 , wherein the rich mixture contains less than 50% of the stoichiometric amount of oxygen-containing gas.

4. The system of claim 1 , wherein the oxygen-containing gas comprises air.

5. The system of claim 1 , wherein the oxygen-containing gas comprises ozone.

6. The system of claim 1 , wherein the oxygen-containing gas is pure oxygen.

7. The system of claim 1 , wherein the oxygen-containing gas comprises oxygen-enriched air.

8. The system of claim 1 , wherein the cleaned producer gas is exhausted at an elevated pressure.

9. The system of claim 1 , wherein water or another liquid is directly injected into the clean-up engine during an exhaust stroke to maintain a chemical composition of the cleaned producer gas close to a chemical composition at peak temperature and pressure.

10. The system of claim 1 , wherein an expansion ratio of the clean-up engine is higher than a compression ratio to decrease a temperature of the cleaned producer gas.

11. The system of claim 1 , wherein the producer gas is generated by gasification of organic material.

12. The system of claim 11 , wherein the organic material comprises biomass.

13. The system of claim 11 , wherein the organic material comprises municipal solid waste.

14. The system of claim 11 , wherein the organic material comprises industrial organic waste.

15. The system of claim 1 , wherein the cleaned producer gas is passed through a heat exchanger prior to entering the power engine.

16. The system of claim 1 , wherein the cleaned producer gas comprises lighter organic components, and the cleaned producer gas is maintained at a temperature above a dew point of the lighter organic components prior to entering the power engine.

17. The system of claim 1 , wherein the power engine comprises a dual fuel engine, and a second fuel comprises diesel fuel.

18. The system of claim 17 , wherein the power engine comprises a prechamber into which the diesel fuel is introduced.

19. The system of claim 1 , wherein the one or more cylinders of the clean-up engine and the one or more cylinders of the power engine reside in a single engine.

20. The system of claim 19 , wherein an equal number of cylinders are used as part of the clean-up engine and as part of the power engine.

21. The system of claim 1 , further comprising a heat exchanger disposed between the clean-up engine and the input to the power engine.

22. The system of claim 1 , further comprising a synthesis plant, wherein the cleaned producer gas is used for synthesizing chemicals by the synthesis plant.

23. The system of claim 22 , wherein fuel is synthesized when electricity is not needed.

24. A system to produce chemicals from a producer gas, wherein the producer gas comprises heavy organic components known as tar, comprising:
a clean-up engine, comprising one or more cylinders, wherein an input to the one or more cylinders of the clean-up engine comprises a rich mixture of the producer gas and an oxygen-containing gas, wherein the producer gas enters the clean-up engine at a temperature greater than a dew point of the tar, wherein the tar is not removed from the producer gas prior to entering the clean-up engine and wherein the clean-up engine exhausts a cleaned producer gas; and
a synthesis plant, wherein the cleaned producer gas is used for synthesizing chemicals by the synthesis plant.

25. The system of claim 24 , wherein the cleaned producer gas is passed through a heat exchanger prior to entering the synthesis plant.

26. The system of claim 24 , wherein the synthesis plant produces methanol, ethanol, or FT liquids.

27. A method of cleaning producer gas, wherein the producer gas comprises heavy organic components known as tar, comprising:
introducing the producer gas at a temperature greater than a dew point of the tar to a cylinder of an engine, wherein the tar is not removed from the producer gas prior to introduction to the engine;
introducing less than a stoichiometric amount of an oxygen-containing gas into the cylinder to create a rich mixture comprising the producer gas and the oxygen-containing gas;
compressing the rich mixture within the cylinder;
combusting the rich mixture to destroy the tar; and
exhausting cleaned producer gas from the cylinder.

28. The method of claim 27 , wherein the producer gas and the oxygen-containing gas are mixed prior to introduction to the cylinder.

29. The method of claim 28 , wherein the cylinder lacks an ignition source and relies on increased pressure of the rich mixture to cause ignition.

30. The method of claim 28 , wherein the rich mixture contains less than 50% of the stoichiometric amount of oxygen-containing gas.

31. The method of claim 27 , wherein the oxygen-containing gas comprises air.

32. The method of claim 27 , wherein the oxygen-containing gas comprises ozone.

33. The method of claim 27 , wherein the oxygen-containing gas is pure oxygen.

34. The method of claim 27 , wherein the oxygen-containing gas comprises oxygen-enriched air.

35. The method of claim 27 , wherein the cleaned producer gas is exhausted at an elevated pressure.

Assignees

• Massachusetts Inst Technology

Inventors

• Kasseris Emmanouil
• Bromberg Leslie

Classifications

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title

• C10K3/005 Primary

  by partial oxidation · CPC title

• C10J2300/1606

  Combustion processes · CPC title

• F23G5/027

  pyrolising or gasifying stage (pyrolisation of sludge C02F11/00; destructive distillation of carbonaceous materials C10B53/00) · CPC title

• Y02T10/30

  Use of alternative fuels, e.g. biofuels · CPC title