Fuel production system

Patent metadata

Field	Value
Publication number	US-11970667-B2
Application number	US-202117204910-A
Country	US
Kind code	B2
Filing date	Mar 17, 2021
Priority date	Mar 19, 2020
Publication date	Apr 30, 2024
Grant date	Apr 30, 2024

Abstract

A fuel production system 1 for producing a liquid fuel from biomass feedstock includes a gasification furnace 30 that gasifies biomass feedstock to produce a syngas including hydrogen and carbon monoxide; a liquid fuel production unit 4 that produces a liquid fuel from the syngas produced by the gasification furnace 30; an electrolysis unit 60 that produces hydrogen from water using electric power generated using renewable energy; a hydrogen tank 62 that stores the hydrogen produced by the electrolysis unit 60; and a hydrogen supply pump 64 that supplies the hydrogen from the hydrogen tank 62into the gasification furnace 30 or a biomass feedstock supply channel 20 extending from a biomass feedstock supply unit 2 to the gasification furnace 30.

First claim

What is claimed is:

1. A fuel production system for producing a liquid fuel from biomass feedstock, comprising:
a gasification furnace configured to gasify biomass feedstock to produce a syngas comprising hydrogen and carbon monoxide;
a liquid fuel production unit configured to produce a liquid fuel from the syngas produced by the gasification furnace;
an electrolysis unit configured to produce hydrogen from water using electric power generated using renewable energy;
a hydrogen tank configured to store the hydrogen produced by the electrolysis unit;
a remaining hydrogen amount determining section configured to determine a remaining amount of hydrogen in the hydrogen tank;
a hydrogen supply unit configured to supply the hydrogen from the hydrogen tank into the gasification furnace or a biomass feedstock supply channel connected to the gasification furnace; and
a control unit configured to control an amount of hydrogen supplied by the hydrogen supply unit to adjust a H 2 /CO ratio of the syngas discharged from the gasification furnace, wherein
when the remaining amount of hydrogen is more than a predetermined upper threshold, the control unit increases the amount of hydrogen supplied by the hydrogen supply unit more than when the remaining amount of hydrogen is less than the upper threshold.

2. The fuel production system according to claim 1 , wherein the control unit changes the amount of hydrogen supplied by the hydrogen supply unit according to a type of the biomass feedstock in the gasification furnace.

3. The fuel production system according to claim 1 , wherein
the control unit controls, based on the remaining amount of hydrogen, the amount of hydrogen supplied by the hydrogen supply unit and the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

4. The fuel production system according to claim 2 , wherein
the control unit controls, based on the remaining amount of hydrogen, the amount of hydrogen supplied by the hydrogen supply unit and the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

5. The fuel production system according to claim 3 , wherein when the remaining amount of hydrogen is more than the upper threshold, the control unit performs a hydrogen consumption increasing control to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace and to increase the amount of hydrogen supplied by the hydrogen supply unit, compared to a case in which the remaining amount of hydrogen is less than the upper threshold.

6. The fuel production system according to claim 4 , wherein when the remaining amount of hydrogen is more than the upper threshold, the control unit performs a hydrogen consumption increasing control to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace and to increase the amount of hydrogen supplied by the hydrogen supply unit, compared to a case in which the remaining amount of hydrogen is less than the upper threshold.

7. The fuel production system according to claim 3 , further comprising: a heating unit configured to heat the gasification furnace, wherein
the control unit reduces an amount of heat introduced from the heating unit into the gasification furnace to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

8. The fuel production system according to claim 5 , further comprising: a heating unit configured to heat the gasification furnace, wherein
the control unit reduces an amount of heat introduced from the heating unit into the gasification furnace to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

9. The fuel production system according to claim 5 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit reduces an amount of water supplied from the water supply unit into the gasification furnace to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

10. The fuel production system according to claim 7 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit reduces an amount of water supplied from the water supply unit into the gasification furnace to reduce the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

11. The fuel production system according to claim 3 , wherein when the remaining amount of hydrogen is less than a lower threshold that is smaller than the upper threshold, the control unit performs a hydrogen consumption reducing control to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace and to reduce the amount of hydrogen supplied by the hydrogen supply unit, compared to a case in which the remaining amount of hydrogen is more than the lower threshold.

12. The fuel production system according to claim 4 , wherein when the remaining amount of hydrogen is less than a lower threshold that is smaller than the upper threshold, the control unit performs a hydrogen consumption reducing control to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace and to reduce the amount of hydrogen supplied by the hydrogen supply unit, compared to a case in which the remaining amount of hydrogen is more than the lower threshold.

13. The fuel production system according to claim 11 , further comprising a heating unit configured to heat the gasification furnace, wherein the control unit increases an amount of heat introduced from the heating unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

14. The fuel production system according to claim 12 , further comprising a heating unit configured to heat the gasification furnace, wherein the control unit increases an amount of heat introduced from the heating unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

15. The fuel production system according to claim 11 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit increases an amount of water supplied from the water supply unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

16. The fuel production system according to claim 12 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit increases an amount of water supplied from the water supply unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

17. The fuel production system according to claim 13 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit increases an amount of water supplied from the water supply unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

18. The fuel production system according to claim 14 , further comprising a water supply unit configured to supply water into the gasification furnace, wherein the control unit increases an amount of water supplied from the water supply unit into the gasification furnace to increase the H 2 /CO ratio of the syngas produced by reaction in the gasification furnace.

Assignees

• Honda Motor Co Ltd

Inventors

• Chishima Hiroshi

Classifications

• C10J3/482 Primary

  Gasifiers with stationary fluidised bed · CPC title

• C10J3/723

  Controlling or regulating the gasification process · CPC title

• C25B1/04 Primary

  by electrolysis of water · CPC title

• C25B15/081

  Supplying products to non-electrochemical reactors that are combined with the electrochemical cell, e.g. Sabatier reactor · CPC title

• C10J2300/0916

  Biomass · CPC title