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A method for removing contaminants from an process stream that includes the use of reticulated material to filter the process stream. The reticulated material also facilitate process stream flow distribution in process units. The reticulated material can be packed with a void space between a substan

A method for removing contaminants from an process stream that includes the use of reticulated material to filter the process stream. The reticulated material also facilitate process stream flow distribution in process units. The reticulated material can be packed with a void space between a substantial number of the reticulated material that can be varied to enhance filtration and flow distribution. The method of filtering also provides a method of removing contaminants leaving process equipment. The methods can be used on a variety of process streams and process equipment. The reticulated material can include ceramics, metallic materials, and chemical vapor deposition elements. The reticulated material can be of various shapes and sizes, and can also be catalytically active.

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What is claimed: 1. A method of removing contaminants from a contaminated process stream comprising the steps of: (a) providing a plurality of reticulated elements in a process unit; (b) randomly packing the plurality of reticulated elements within the process unit thereby providing a void space be

What is claimed: 1. A method of removing contaminants from a contaminated process stream comprising the steps of: (a) providing a plurality of reticulated elements in a process unit; (b) randomly packing the plurality of reticulated elements within the process unit thereby providing a void space between a substantial number of the reticulated elements to enhance filtration of contaminants on a surface of the plurality of reticulated elements to produce a substantially decontaminated process stream; and (c) contacting the contaminated process stream with the plurality of reticulated elements to remove contaminants from the contaminated process stream while allowing the substantially decontaminated process stream to pass unimpeded through the plurality of reticulated elements, wherein the contaminated process stream is a contaminated non-organic based process stream. 2. The method of claim 1, wherein the plurality of reticulated elements have different pore sizes so that the plurality of reticulated elements can filter contaminants of different sizes. 3. The method of claim 1, further including depositing a catalyst on the plurality of reticulated elements prior to contacting the contaminated process stream. 4. The method of claim 1, wherein the reticulated elements comprise a material selected from the group consisting of a ceramic material, a metallic material, and a chemical vapor deposition material. 5. The method of claim 1, wherein a substantial number of the plurality of reticulated elements have a plurality of pores defined by a plurality of web members forming a plurality of flow passageways through the plurality of reticulated elements and an average pore size of the pores is about 6 millimeters to about 100 microns. 6. The method of claim 1, wherein the plurality of reticulated elements have a porosity of about 4 to 800 pores per linear inch. 7. The method of claim 1, wherein the reticulated elements are formed from a reticulated foam material. 8. The method of claim 1, wherein the reticulated elements have a shape selected from the group consisting of substantially spherical shaped balls, raschig rings, saddle shaped pieces, monoliths, squares, a single sheet, hollow cylinders, solid cylinders, and a single disk. 9. The method of claim 8, wherein the reticulated elements are formed having perforations. 10. The method of claim 1, wherein the process unit has an inner cross-sectional configuration and the plurality of the reticulated elements are formed into an assembled sheet that, when constructed, is custom-fit to the process unit's inner cross-sectional configuration. 11. The method of claim 1, wherein the process unit has an inner cross-sectional configuration and the plurality of the reticulated elements are formed into a plurality of segments forming an assembled disk that, when constructed, is custom-fit to the process unit's inner cross-sectional configuration. 12. The method of claim 1, wherein the process unit is selected from the group consisting of a distillation column, a tail gas treater, an incinerator, and a scrubber. 13. The method of claim 1, wherein the reticulated elements comprise a substrate of reticulated elements having a substantially uniform coating of a selected catalyst including a porous alumina coating with one Group VI-B metal. 14. The method of claim 13, wherein the Group VI-B metal is molybdenum. 15. The method of claim 1, wherein the reticulated elements comprise a substrate of reticulated elements having a substantially uniform coating of a selected catalyst including a porous alumina coating with one Group VIII metal. 16. The method of claim 15, wherein a Group VIII metal is nickel or cobalt. 17. The method of claim 1, wherein a Group VI-B metal is impregnated into the reticulated element. 18. The method of claim 1, wherein a Group VIII metal is impregnated into the reticulated element. 19. The method of claim 1, wherein the reticulated elements comprise a porous inorganic oxide selected from the group consisting of alumina, silica, silica-alumina, magnesia, silica-magnesia and titania. 20. The method of claim 1, wherein the reticulated elements comprise a metal oxide selected from the group consisting of titanium, tin, lead, zirconium, ruthenium, tungsten, yttrium, nickel, magnesium, calcium, aluminum, silicon or boron. 21. The method of claim 1, wherein the reticulated elements comprise a metal nitride selected from the group consisting of titanium, zirconium, tungsten, silicon or boron. 22. The method of claim 1, wherein the reticulated elements comprise a metal carbide selected from the group consisting of titanium, zirconium, tungsten, silicon or boron. 23. The method of claim 1, wherein the reticulated elements comprise a metal boride selected from the group consisting of titanium, zirconium or tungsten. 24. The method of claim 1, wherein the reticulated elements comprise a zeolite selected from the group consisting of zeolite L, zeolite X and zeolite Y. 25. A method of perpendicular flow distribution in a non-catalytically reactive process unit comprising the steps of: (a) providing a plurality of reticulated elements in the non-catalytically reactive process unit having a plurality of web members that define flow passageways that facilitate perpendicular flow distribution; and (b) contacting a process stream with the zone of reticulated elements; and (c) subdividing the process stream into a plurality of smaller fluid streams by passing the process stream through the plurality of flow passageways defined by the web members of the plurality of reticulated elements so that the process stream is significantly dispersed in a perpendicular direction. 26. The method of claim 25 further comprising the following steps: (a) removing contaminants from the contaminated process stream by randomly placing the plurality of reticulated elements within the process unit thereby providing a void space between each reticulated element to enhance filtration of contaminants on a surface of the plurality of reticulated elements; and (b) providing a decontaminated and uniformly spread process stream for further processing in downstream process unit. 27. The method of claim 25, wherein the step of providing a plurality of reticulated elements includes providing the plurality of reticulated elements at a location selected from the group consisting of a process unit inlet, an interior of a process unit, a process unit outlet, and combinations thereof. 28. The method of claim 25, wherein the process unit has an inner cross-sectional configuration and the plurality of the reticulated elements are formed into an assembled sheet that, when constructed, is custom-fit to the process unit's inner cross-sectional configuration. 29. The method of claim 1, wherein the plurality of reticulated elements is provided across an entire length of the process unit. 30. A method of removing contaminants from a contaminated process stream comprising the steps of: (a) providing a plurality of reticulated elements in a process unit, wherein the process unit comprises a non-catalytically reactive process unit; (b) randomly packing the plurality of reticulated elements within the process unit thereby providing a void space between a substantial number of the reticulated elements to enhance filtration of contaminants on a surface of the plurality of reticulated elements to produce a substantially decontaminated process stream; and (c) contacting the contaminated process stream with the plurality of reticulated elements to remove contaminants from the contaminated process stream while allowing the substantially decontaminated process stream to pass unimpeded through the plurality of reticulated elements. 31. The method of claim 25, wherein the process unit is selected from the group consisting of a distillation column, a tail gas treater, an incinerator, and a scrubber. 32. The method of claim 30, wherein the process unit is selected from the group consisting of a distillation column, a tail gas treater, an incinerator, and a scrubber. 33. The method of claim 25, wherein the reticulated elements have a shape selected from the group consisting of substantially spherical shaped balls, raschig rings, saddle shaped pieces, monoliths, squares, a single sheet, hollow cylinders, solid cylinders, and a single disk. 34. The method of claim 30, wherein the reticulated elements have a shape selected from the group consisting of substantially spherical shaped balls, raschig rings, saddle shaped pieces, monoliths, squares, a single sheet, hollow cylinders, solid cylinders, and a single disk.