Non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods
The present technology is generally directed to non-perpendicular connections between coke oven uptakes and a hot common tunnel, and associated systems and methods. In some embodiments, a coking system includes a coke oven and an uptake duct in fluid communication with the coke oven. The uptake duct has an uptake flow vector of exhaust gas from the coke oven. The system also includes a common tunnel in fluid communication with the uptake duct. The common tunnel has a common flow vector and can be configured to transfer the exhaust gas to a venting system. The uptake flow vector and common flow vector can meet at a non-perpendicular interface to improve mixing between the flow vectors and reduce draft loss in the common tunnel.
1. A coking system, comprising:
a common tunnel configured to direct a gas from one or more coke ovens to a common stack, wherein the common tunnel has a common tunnel flow with a common tunnel flow vector, and wherein the common tunnel flow vector, on a spherical coordinate system having an x-axis, y-axis, and z-axis, has an x-component extending along a long axis of the common tunnel, a y-component extending along a width of the common tunnel, and a z-component extending along a height of the common tunnel;
a coke oven in fluid connection with the common tunnel via an uptake, wherein:
the uptake connects to the common tunnel at an intersection;
the uptake includes an uptake flow having an uptake flow vector, at the intersection, with an x-component, a y-component, and a z-component on the spherical coordinate system; and
wherein the uptake is disposed at an angle with respect to the common tunnel, at the intersection, such that the uptake flow vector x-component has a direction in common with of the common flow vector x-component but the uptake flow vector z-component differs from the z-component of the common tunnel flow vector, thereby encouraging mixing and combustion of unburned volatile material and oxygen inside the common tunnel.
2. The coking system of claim 1 wherein an inner characteristic dimension of the uptake at least one of increases or decreases in the direction of the intersection.
3. The coking system of claim 1 wherein the uptake further includes an angled baffle at or near the intersection, the baffle configured to redirect the uptake flow.
4. The coking system of claim 1 wherein the common tunnel has an elliptical cross-sectional shape.
5. The coking system of claim 1 wherein the z-component of the uptake flow vector is in a downward direction, such that buoyancy of gases exiting the uptake are at least partially countered and combustion of the gases is encouraged to occur toward a lower portion of the common tunnel.