- Lisle IL, US Parthasarathy Kesavan - Lisle IL, US Rajesh Kumar Kandula - Lisle IL, US Mayela Carolina Fernandez - Lisle IL, US Khambath Vichitvongsa - Granite City IL, US Jeffrey Scott Brombolich - Granite City IL, US Edward A. Glass - Granite City IL, US
The present technology is generally directed to systems and methods for optimizing the burn profiles for coke ovens, such as horizontal heat recovery ovens. In various embodiments the burn profile is at least partially optimized by controlling air distribution in the coke oven. In some embodiments, the air distribution is controlled according to temperature readings in the coke oven. In particular embodiments, the system monitors the crown temperature of the coke oven. After the crown reaches a particular temperature range the flow of volatile matter is transferred to the sole flue to increase sole flue temperatures throughout the coking cycle. Embodiments of the present technology include an air distribution system having a plurality of crown air inlets positioned above the oven floor.
- Lisle IL, US Parthasarathy Kesavan - Lisle IL, US Rajesh Kumar Kandula - Lisle IL, US Mayela Carolina Fernandez - Lisle IL, US Khambath Vichitvongsa - Granite City IL, US Jeffrey Scott Brombolich - Granite City IL, US Richard Alan Mrozowicz - Granite City IL, US Edward A. Glass - Granite City IL, US
The present technology is generally directed to systems and methods for optimizing the burn profiles for coke ovens, such as horizontal heat recovery ovens. In various embodiments the burn profile is at least partially optimized by controlling air distribution in the coke oven. In some embodiments, the air distribution is controlled according to temperature readings in the coke oven. In particular embodiments, the system monitors the crown temperature of the coke oven. After the crown reaches a particular temperature range the flow of volatile matter is transferred to the sole flue to increase sole flue temperatures throughout the coking cycle. Embodiments of the present technology include an air distribution system having a plurality of crown air inlets positioned above the oven floor.
Method And System For Optimizing Coke Plant Operation And Output
- Lisle IL, US Chun Wai Choi - Chicago IL, US Parthasarathy Kesavan - Lisle IL, US Katharine E. Russell - Lisle IL, US Jeffrey Scott Brombolich - O'Fallon IL, US Richard Alan Mrozowicz - Granite City IL, US Edward A. Glass - Granite City IL, US
The present technology is generally directed to methods of increasing coal processing rates for coke ovens. In various embodiments, the present technology is applied to methods of coking relatively small coal charges over relatively short time periods, resulting in an increase in coal processing rate. In some embodiments, a coal charging system includes a charging head having opposing wings that extend outwardly and forwardly from the charging head, leaving an open pathway through which coal may be directed toward side edges of the coal bed. In other embodiments, an extrusion plate is positioned on a rearward face of the charging head and oriented to engage and compress coal as the coal is charged along a length of the coking oven. In other embodiments, a false door system includes a false door that is vertically oriented to maximize an amount of coal being charged into the oven.
- Lisle IL, US Parthasarathy Kesavan - Lisle IL, US Rajesh Kumar Kandula - Lisle IL, US Mayela Carolina Fernandez - Lisle IL, US Khambath Vichitvongsa - Granite City IL, US Jeffrey Scott Brombolich - Granite City IL, US Richard Alan Mrozowicz - Granite City IL, US Edward A. Glass - Granite City IL, US
International Classification:
C10B 21/16 C10B 41/00
Abstract:
The present technology is generally directed to systems and methods for optimizing the burn profiles for coke ovens, such as horizontal heat recovery ovens. In various embodiments the burn profile is at least partially optimized by controlling air distribution in the coke oven. In some embodiments, the air distribution is controlled according to temperature readings in the coke oven. In particular embodiments, the system monitors the crown temperature of the coke oven. After the crown reaches a particular temperature range the flow of volatile matter is transferred to the sole flue to increase sole flue temperatures throughout the coking cycle. Embodiments of the present technology include an air distribution system having a plurality of crown air inlets positioned above the oven floor.
Method And System For Optimizing Coke Plant Operation And Output
- Lisle IL, US Chun Wai Choi - Chicago IL, US Parthasarathy Kesavan - Lisle IL, US Katharine E. Russell - Lisle IL, US Khambath Vichitvongsa - Granite City IL, US Jeffrey Scott Brombolich - O'Fallon IL, US Richard Alan Mrozowicz - Granite City IL, US Edward A. Glass - Granite City IL, US
International Classification:
C10B 57/02 C10B 37/04 C10B 31/00
Abstract:
The present technology is generally directed to methods of increasing coal processing rates for coke ovens. In various embodiments, the present technology is applied to methods of coking relatively small coal charges over relatively short time periods, resulting in an increase in coal processing rate. In some embodiments, a coal charging system includes a charging head having opposing wings that extend outwardly and forwardly from the charging head, leaving an open pathway through which coal may be directed toward side edges of the coal bed. In other embodiments, an extrusion plate is positioned on a rearward face of the charging head and oriented to engage and compress coal as the coal is charged along a length of the coking oven. In other embodiments, a false door system includes a false door that is vertically oriented to maximize an amount of coal being charged into the oven.
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Edward Glass
Education:
Westmoreland High School, Westmoreland, NY, Mayville State University