Apparatus and method for flameless thermal oxidation at optimized equivalence ratios
In a flameless thermal oxidizer including a vessel configured to contain a matrix bed of media, and a vent gas stream conduit and an oxidizing agent conduit each extending into an interior of the vessel at least partially within the matrix bed of media, a method of delivering a vent gas stream and oxidizing agents into the vessel includes the steps of distributing the vent gas stream through the vent gas stream conduit; distributing the oxidizing agents through a mixing conduit; and combining the vent gas stream and the oxidizing agents in the mixing conduit.
1. In a flameless thermal oxidizer including a vessel configured to contain a matrix bed of media, and a vent gas stream conduit and an oxidizing agent conduit each extending into an interior of the vessel at least partially within the matrix bed of media, a method of delivering a vent gas stream and oxidizing agents into the vessel, comprising:
distributing the vent gas stream through the vent gas stream conduit;
distributing the oxidizing agents from the oxidizing agent conduit into respective inlets of a plurality of mixing tubes, the plurality of mixing tubes positioned at least partially within the matrix bed of media;
distributing the vent gas stream from within the vent gas stream conduit through apertures formed in a sidewall of each one of the plurality of mixing tubes;
combining the vent gas stream and the oxidizing agents in each one of the plurality of mixing tubes; and
delivering the combined vent gas stream and oxidizing agents from an outlet of each one of the plurality of mixing tubes into the matrix bed of media.
2. The method of claim 1 , further comprising mixing the vent gas stream and the oxidizing agents at an oxidizing agent to vent gas stream equivalence ratio of between 0.5:1 to 0.8:1 with the plurality of mixing tubes.
3. The method of claim 1 , further comprising mixing the vent gas stream and the oxidizing agents at an oxidizing agent to vent gas stream equivalence ratio of between 0.09:1 to 4:1 with the plurality of mixing tubes.
4. The method of claim 1 , further comprising adding a gaseous fuel to the vent gas stream for enriching said vent gas stream.
5. The method of claim 4 , wherein the gaseous fuel comprises a fuel selected from the group consisting of a natural gas, propane, and refinery gas.
6. The method of claim 1 , further comprising isolating the vent gas stream and the oxidizing agents upstream of the plurality of mixing tubes.
7. The method of claim 1 , wherein the delivering further comprises delivering the combined vent gas stream and oxidizing agents directly into the matrix bed of media.