IP Library Granted Patent US 11,441,077
Granted Patent B2
US 11,441,077 · App. 16/828,448 · Granted Sep 13, 2022

Coke plant including exhaust gas sharing

Inventors: John F. Quanci (Haddonfield, NJ); Peter U. Chun (Naperville, IL); Milos J. Kaplarevic (Chicago, IL); Vince G. Reiling (Wheaton, IL)
Assignee: SUNCOKE TECHNOLOGY AND DEVELOPMENT LLC
C10B5/04C10B5/12C10B15/02C10B41/00C10B45/00F22B1/18C10B5/00C10B5/02C10B5/06C10B5/08C10B49/02
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Quick Facts
Patent No.
US 11,441,077
App. No.
16/828,448
Granted
Sep 13, 2022
Kind
B2
Abstract

A coke plant includes multiple coke ovens where each coke oven is adapted to produce exhaust gases, a common tunnel fluidly connected to the plurality of coke ovens and configured to receive the exhaust gases from each of the coke ovens, multiple standard heat recovery steam generators fluidly connected to the common tunnel where the ratio of coke ovens to standard heat recovery steam generators is at least 20:1, and a redundant heat recovery steam generator fluidly connected to the common tunnel where any one of the plurality of standard heat recovery steam generators and the redundant heat recovery steam generator is adapted to receive the exhaust gases from the plurality of ovens and extract heat from the exhaust gases and where the standard heat recovery steam generators and the redundant heat recovery steam generator are all connected in parallel with each other.

Claims (33)

1. A system for controlling steam generation within an industrial facility, comprising:

two or more steam generators, each of the two or more steam generators (i) comprising a water inlet, a steam outlet, a process gas inlet, and a process gas outlet, and (ii) being fluidly connected to a common tunnel at the process gas inlet, wherein the common tunnel is configured to receive a plurality of process streams from multiple sources, wherein each of the two or more steam generators is (i) configured to extract heat from the process streams to generate steam, and (ii) fluidically coupled to a corresponding steam generator damper configured to be positioned, via an actuator, to any one of a plurality of positions between open and closed; and

a controller operably coupled to the one of more steam generators and the actuators of the steam generator dampers, and configured to operate in a normal mode and a gas sharing mode,

wherein, in the normal mode, (i) the process gases are routed to a first amount of the two or more steam generators such that the two or more steam generators are configured to produce steam at a first capacity, and (ii) the controller sets a target oven draft of the common tunnel to a first draft pressure,

wherein, in the gas sharing mode, (i) the process gases are routed to a second amount of the two or more steam generators such that the two or more steam generators are configured to produce steam at a second capacity, the second amount being less than the first amount and (ii) the controller sets a target oven draft of the common tunnel to a second draft pressure less than the first draft pressure, and

wherein, upon receiving an indication that one or the two or more steam generators is offline, the controller automatically switches from the normal mode to the gas sharing mode and adjusts the target oven draft from the first draft pressure to the second draft pressure.

2. The system of claim 1 , wherein the first capacity is more than the second capacity.

3. The system of claim 1 , wherein the second amount is one less than the first amount.

4. The system of claim 1 , wherein the process gases are exhaust gases produced via a plurality of coke ovens.

5. The system of claim 1 , wherein at least a portion of the multiple sources are coke ovens.

6. The system of claim 1 , wherein each of the two or more steam generators is fluidly coupled, via the steam outlet, to an electricity-generating plant.

7. The system of claim 1 , further comprising a plurality of coke ovens, each of the coke ovens including an oven chamber configured to generate process gas, and an uptake duct in fluid communication with the oven chamber and configured to receive the process gas generated via the oven chamber.

8. The system of claim 1 , wherein the common tunnel comprises a pressure sensor configured to detect an oven draft, and wherein the controller is operably coupled to the pressure sensor and configured to provide instructions for controlling flow of the process gases based on the detected oven draft.

9. The system of claim 8 , further comprising a plurality of coke ovens, each of the coke ovens including (i) an oven chamber configured to generate process gas, (ii) an uptake duct in fluid communication with the oven chamber and configured to receive the process gas generated via the oven chamber, and (iii) an uptake damper in fluid communication with the uptake duct and positioned via an actuator.

10. A system for controlling steam generation within an industrial facility, comprising:

a steam generator (i) comprising a water inlet, a steam outlet, a process gas inlet, and a process gas outlet, and (ii) fluidly connected to a common tunnel at the process gas inlet, wherein the common tunnel is configured to receive a plurality of process streams from multiple sources, and wherein the steam generator is (i) configured to extract heat from the process streams to generate steam, and (ii) fluidically coupled to a steam generator damper configured to be positioned, via an actuator, to at least one of a plurality of positions between open and closed; and

a controller operably coupled to the steam generator and configured to operate in a first mode and a second mode,

wherein, in the first mode, (i) the process gases are routed to the steam generator such that the steam generator is configured to produce steam at a first capacity, and (ii) the controller sets a target oven draft of the common tunnel to a first draft pressure,

wherein, in the second mode, (i) at least a portion of the process gases are not routed to the steam generator such that the steam generator is configured to produce steam at a second capacity less than the first capacity and (ii) the controller sets a target oven draft of the common tunnel to a second draft pressure less than the first draft pressure, and

wherein, upon receiving an indication that a second steam generator is offline, the controller automatically switches from the first mode to the second mode and adjusts the target oven draft from the first draft pressure to the second draft pressure.

11. The system of claim 10 , wherein the process gases are exhaust gases produced via a plurality of coke ovens.

12. The system of claim 10 , wherein at least a portion of the multiple sources are coke ovens.

13. The system of claim 10 , wherein the steam generator is fluidly coupled, via the steam outlet, to an electricity-generating plant.

14. The system of claim 10 , wherein the first mode is a normal or default mode and the second mode is a gas sharing mode.

15. The system of claim 10 , further comprising a coke oven including an oven chamber configured to generate process gas, and an uptake duct in fluid communication with the oven chamber and configured to receive the process gas generated via the oven chamber.

16. The system of claim 10 , wherein the common tunnel comprises a pressure sensor configured to detect an oven draft, and wherein the controller is operably coupled to the pressure sensor and configured to provide instructions for controlling flow of the process gases to the steam generator based on the detected oven draft.

17. A system for controlling steam generation within an industrial facility, comprising:

a plurality of steam generators, each of the steam generators (i) comprising a water inlet, a steam outlet, a process gas inlet, and a process gas outlet, and (ii) being fluidly connected to a common tunnel at the process gas inlet, wherein the common tunnel is configured to receive a plurality of process streams from multiple sources, and wherein each of the steam generators is (i) configured to extract heat from the process streams to generate steam, and (ii) fluidically coupled to a corresponding steam generator damper configured to be positioned, via an actuator, to at least one of a plurality of positions between open and closed; and

a controller operably coupled to the steam generators and configured to operate in a first mode and a second mode,

wherein, in the first mode, (i) the process gases are routed to a first amount of the steam generators such that the steam generators are configured to produce steam at a first capacity, and (ii) the controller sets a target oven draft of the common tunnel to a first draft pressure,

wherein, in the second mode, (i) the process gases are routed to a second amount of the steam generators such that the steam generators are configured to produce steam at a second capacity, the second amount being less than the first amount, and (ii) the controller sets a target oven draft of the common tunnel to a second draft pressure less than the first draft pressure, and

wherein, upon receiving an indication that one or more of the steam generators is offline, the controller automatically switches from the first mode to the second mode and adjusts the target oven draft from the first draft pressure to the second draft pressure.

18. The system of claim 17 , wherein the first capacity is more than the second capacity, and wherein each of the steam generators is fluidly coupled, via the steam outlet, to an electricity-generating plant.

Assignments (3)
SECURITY INTEREST Recorded Jul 25, 2025
From: SUNCOKE TECHNOLOGY AND DEVELOPMENT LLC
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 072254/0272 →
SECURITY INTEREST Recorded Jul 13, 2021
From: SUNCOKE TECHNOLOGY AND DEVELOPMENT LLC
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS COLLATERAL AGENT
Reel/Frame 056846/0548 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 2, 2021
From: QUANCI, JOHN F.; CHUN, PETER U.; KAPLAREVIC, MILOS J.
To: SUNCOKE TECHNOLOGY AND DEVELOPMENT LLC
Reel/Frame 056743/0148 →
Cited By (12)
US 12,190,701 US 12,195,671 US 12,215,289 US 12,286,591 US 12,305,119 US 12,319,976 US 12,331,367 US 12,410,369 US 12,600,915 US 12,673,348 US 12,692,453 US 12,692,562