Coal blends, foundry coke products, and associated systems, devices, and methods

Patent metadata

Field	Value
Publication number	US-12286591-B2
Application number	US-202318501795-A
Country	US
Kind code	B2
Filing date	Nov 3, 2023
Priority date	Nov 4, 2022
Publication date	Apr 29, 2025
Grant date	Apr 29, 2025

Abstract

Methods and systems for coking coal blends to produce foundry coke products are disclosed herein. Methods for producing coke products can include charging a coal blend into a coke oven; and heating the charged coal blend such that a crown temperature of the coke oven is greater than a lower bound coking temperature. The pyrolysis duration begins when the crown temperature of the oven is greater than the lower bound coking temperature, and ends when the crown temperature of the oven is less than the lower bound coking temperature.

First claim

We claim:

1. A method of producing a coke product, the method comprising:
adding water to a coal blend;
charging the coal blend into a coke oven; and
heating the charged coal blend such that, during a pyrolysis duration of a coking cycle for the charged coal blend, a crown temperature of the coke oven is greater than a lower bound coking temperature,
wherein:
the lower bound coking temperature is within a range of 1200-2300° F.;
the pyrolysis duration begins when the crown temperature of the oven is greater than the lower bound coking temperature;
the pyrolysis duration ends when the crown temperature of the oven is less than the lower bound coking temperature;
the crown temperature is greater than a sole flue temperature of the coke oven throughout the pyrolysis duration; and
the pyrolysis duration is greater than 24 hours.

2. The method of claim 1 , wherein the lower bound coking temperature is within a range of 1800-2200° F.

3. The method of claim 1 , wherein an upper limit of the crown temperature is limited by an upper bound coking temperature that is greater than 2300° F.

4. The method of claim 1 , wherein the crown temperature of the coke oven during the pyrolysis duration is 2100-2300° F.

5. The method of claim 1 , wherein the crown temperature is within a 100° F. temperature range during at least twelve hours of the pyrolysis duration.

6. The method of claim 1 , wherein, during the pyrolysis duration, a sole flue temperature is below 2000° F.

7. The method of claim 1 , wherein, during the pyrolysis duration, a sole flue temperature is 1400-1800° F.

8. The method of claim 1 , wherein a soak time of the charged coal blend is less than 10.0 hours.

9. The method of claim 1 , wherein adding water to the coal blend comprises:
determining whether a testing moisture of the coal blend satisfies a target moisture value; and
in response to a determination that the testing moisture of the coal blend does not satisfy the target moisture values, adding water to the coal blend.

10. The method of claim 1 , wherein a moisture weight fraction of the coal blend charged into the coke oven is at least 8.0%.

11. The method of claim 1 , wherein adding water to the coal blend comprises adding water to a belt carrying the coal blend.

12. The method of claim 1 wherein adding water to the coal blend is based on a volatile matter of the coal blend.

13. The method of claim 1 , wherein adding water to the coal blend comprises adding water such that a moisture content of the charged coal is no more than 5% smaller or larger than a volatile matter mass fraction of the coal blend.

14. The method of claim 1 , wherein the pyrolysis duration is approximately 48 hours.

15. The method of claim 1 , wherein a volatile matter mass fraction of the coal blend is less than 27.0%.

16. The method of claim 1 , wherein the coke oven includes an uptake damper movable to a plurality of positions between open and closed, and wherein heating the coal blend comprises maintaining the uptake damper of the coke oven in a position less than half-way open during a majority of an initial 24 hours of the coking cycle.

17. The method of claim 1 , wherein heating the coal blend is based on a temperature change rate being no more than a temperature rate threshold that is less than or equal to 50° F. per hour.

18. The method of claim 1 , wherein heating the coal blend comprises closing a sole flue damper or maintaining the sole flue damper in a closed position for a majority of the pyrolysis duration.

19. The method of claim 1 , wherein a ratio of a soak time of the charged coal blend to a cycle duration of the charged coal blend is less than 33.0%.

20. A method, comprising:
heating a coal blend within a coke oven to a coking temperature during a pyrolysis duration of a coking,
wherein:
the pyrolysis duration begins when a crown temperature of the oven is greater than a lower bound coking temperature;
the pyrolysis duration ends when the crown temperature of the oven is less than the lower bound coking temperature;
the lower bound coking temperature is within a range of 1200-2300° F.;
the crown temperature is greater than a sole flue temperature of the coke oven throughout the pyrolysis duration; and
the pyrolysis duration is greater than 24 hours.

21. The method of claim 20 , wherein, for at least 12 hours of the pyrolysis duration, the coking temperature varies no more than 75° F.

Assignees

• Suncoke Tech & Development Llc

Inventors

• Quanci John Francis
• RICHARDSON John Michael
• Perkins Jonathan Hale

Classifications

• C10B15/02

  with floor heating · CPC title

• G01N33/222 Primary

  Solid fuels, e.g. coal · CPC title

• C10L2290/60

  Measuring or analysing fractions, components or impurities or process conditions during preparation or upgrading of a fuel · CPC title

• C10L2290/24

  Mixing, stirring of fuel components · CPC title

• C10L5/48

  on industrial residues and waste materials {(C10L5/403, C10L5/406 take precedence)} · CPC title