Catalytic oxidation product gas management
US-2018370648-A1 · Dec 27, 2018 · US
US10918896B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10918896-B2 |
| Application number | US-202016797745-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 21, 2020 |
| Priority date | Oct 19, 2010 |
| Publication date | Feb 16, 2021 |
| Grant date | Feb 16, 2021 |
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The invention includes components and methodology for fixed and semi-fixed systems for extinguishing fire in large industrial flammable liquid storage tanks, including aerated foam projecting nozzles discharging substantially focused streams together with aeration chambers and risers.
Opening claim text (preview).
What is claimed is: 1. A fixed firefighting system for large industrial tanks, comprising: two connected nozzles, each nozzle structured to project aerated foam of between 100 gallons per minute (gpm) and 1000 gpm in substantially focused streams and in roughly opposing directions; the two connected nozzles attached downstream of, and in fluid communication with an ambient air aeration chamber; a third centrally directed nozzle structured to project aerated foam of between 100 gpm and 1000 gpm, located and structured in combination with the two connected nozzles to discharge a substantially focused stream toward a center of an industrial tank; a stream shaper located in a cylindrical tip portion of the third centrally directed nozzle; and the three nozzles structured for fixed attachment proximate a wall surface of the industrial tank. 2. The system of claim 1 , wherein each of the two connected nozzles are structured to project in directly opposite directions plus or minus 15 degrees. 3. The system of claim 1 , wherein the third centrally directed nozzle is structured to project toward a center of the industrial tank plus or minus 30 degrees. 4. The system of claim 1 , wherein the two connected nozzles are structured to project aerated foam of between 100 gpm and 900 gpm. 5. The system of claim 1 , wherein the third centrally directed nozzle is structured to project aerated foam of between 100 gpm and 900 gpm. 6. The system of claim 1 , wherein the third centrally directed nozzle is structured to project such that at least 60% of the foam discharge remains within a 20 degree cone around a third discharge axis. 7. The system of claim 1 , wherein the ambient air aeration chamber is structured to produce aerated foam with an expansion ratio of between 2-to-1 and 8-to-1. 8. The system of claim 1 , wherein the ambient air aeration chamber is structured to produce aerated foam with an expansion ratio of between 3-to-1 and 5-to-1. 9. The system of claim 1 including a riser for communicating water and foam concentrate, attached to, and in fluid communication with the two connected nozzles and the third centrally directed nozzle. 10. The system of claim 1 , wherein the third centrally directed nozzle is structured to project in a horizontal direction plus or minus 30 degrees. 11. A fixed firefighting system for industrial tanks, comprising: two connected nozzles, each nozzle structured to project aerated foam of between 100 gallons per minute (gpm) and 1000 gpm roughly horizontally and in roughly opposing directions; the two connected nozzles attached downstream of, and in fluid communication with an ambient air aeration chamber; a third centrally directed nozzle structured to project aerated foam of between 100 gpm and 1000 gpm, located and structured in combination with the two connected nozzles to discharge a substantially focused stream toward a center of an industrial tank; a stream shaper located in a cylindrical tip portion of the third centrally directed nozzle; and the three nozzles structured for fixed attachment proximate a wall surface of the industrial tank. 12. The system of claim 11 , wherein each of the two connected nozzles are structured to project in the horizontal direction plus or minus 15 degrees. 13. The system of claim 11 , wherein each of the two connected nozzles are each structured to project in directly opposite directions plus or minus 15 degrees. 14. The system of claim 11 , wherein the third centrally directed nozzle is structured to project toward a center of the industrial tank plus or minus 30 degrees. 15. The system of claim 11 , wherein the two connected nozzles are structured to project aerated foam of between 100 gpm and 900 gpm. 16. The system of claim 11 , wherein the third centrally directed nozzle is structured to project aerated foam of between 100 gpm and 900 gpm. 17. The system of claim 11 , wherein the third centrally directed nozzle is structured to project such that at least 60% of the foam discharge remains within a 20 degree cone around a third discharge axis. 18. The system of claim 11 , wherein the ambient air aeration chamber is structured to produce aerated foam with an expansion ratio of between 2-to-1 and 8-to-1. 19. The system of claim 11 , wherein the ambient air aeration chamber is structured to produce aerated foam with an expansion ratio of between 3-to-1 and 5-to-1. 20. The system of claim 11 including a riser for communicating water and foam concentrate, attached to, and in fluid communication with the two connected nozzles and the third centrally directed nozzle. 21. The system of claim 11 , wherein the third centrally directed nozzle is structured to project in a horizontal direction plus or minus 30 degrees.
Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means · CPC title
for aerating or carbonating within receptacles or tanks, e.g. distribution machines (B01F23/2361 takes precedence) · CPC title
by bubbling (mixers with gas or liquid agitation, e.g. with air supply tubes B01F33/40) · CPC title
electric · CPC title
the liquid or other fluent material being symmetrically deflected about the axis of the nozzle · CPC title
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