ON-SITE SYSTEMS AND METHODS FOR TREATING SPENT OXIDIZABLE CATALYST IN INERT GAS ENVIRONMENTS
A system for segregating a mixture of oxidizable catalyst material and inert support media. The system comprises an enclosure configured to contain inert gas. The enclosure includes a plurality of stacked screens disposed therein. The stacked screens include openings that decrease in size from a top of the stack to a bottom of the stack. The enclosure also includes an inlet to deliver the mixture to an uppermost stacked screen and outlets to direct the separated support media and catalyst material to a location outside the enclosure.
1 . A system for segregating a mixture of oxidizable catalyst material and inert support media, the system comprising:
an enclosure configured to contain inert gas;
a plurality of stacked screens within the enclosure, the stacked screens having openings that decrease in size from a top of the stack to a bottom of the stack;
a mixture inlet in the enclosure positioned to enable delivery of the mixture to an uppermost stacked screen;
at least one inert support media outlet associated with at least one of the plurality of stacked screens, wherein the at least one inert support media outlet directs separated inert support media to a location out of the enclosure;
a catalyst material outlet associated with at least another of the plurality of stacked screens, wherein the catalyst material outlet directs separated oxidizable catalyst material to a location outside the enclosure
at least one motor for moving the stacked screens to cause the oxidizable catalyst material in the mixture to separate from and migrate to a location beneath the inert support media; and
an inert gas inlet associated with the enclosure for permitting the inert gas to enter the enclosure to displace oxygen within the enclosure and thereby limit oxidation of the oxidizable catalyst material while the at least one motor moves the plurality of stacked screens.
2 . The system of claim 1 , wherein the enclosure is configured for pressurization of the inert gas.
3 . The system of claim 1 , wherein the inert gas inlet is located in a lower portion of the enclosure to enable the inert gas to flow over the oxidizable catalyst material and exit the enclosure through a top portion of the enclosure.
4 . The system of claim 1 further comprising a sensor for detecting a reduction of oxygen in the enclosure.
5 . The system of claim 1 , further comprising a mixture conveyor for conveying the mixture to the mixture inlet, wherein the mixture conveyor is in flow communication with the enclosure and is enclosed to contain the inert gas.
6 . The system of claim 5 , further comprising at least one flow bin associated with an end of the mixture conveyor for supplying the mixture to the mixture conveyor, wherein the mixture conveyor is sealingly engaged with the flow bin and the enclosure to contain the inert gas.
7 . The system of claim 6 , wherein the mixture conveyor includes a screw auger.
8 . The system of claim 5 , wherein the mixture conveyor includes a controllable inlet for permitting selective passage of the mixture while limiting loss of the inert gas.
9 . The system of claim 1 , further comprising a regulator for at least periodically supplying additional inert gas to the enclosure to account for loss of the inert gas.
10 . The system of claim 1 , further comprising an air lock associated with the inert support media outlet for limiting the inert gas from leaving the enclosure via the inert support media outlet.
11 . The system of claim 1 , further comprising an air lock associated with the catalyst material outlet for limiting the inert gas from leaving the enclosure via the catalyst material outlet.
12 . The system of claim 1 , further comprising a pressurized inert gas tank flow-connected to the enclosure.
13 . The system of claim 1 , wherein the enclosure and plurality of stacked screens are configured as a portable unit for movement between industrial sites.
14 . The system of claim 1 , further comprising a grinder for grinding the separated oxidizable catalyst material into a powder.
15 . The system of claim 14 , wherein the grinder is located in a region supplied with the inert gas.
16 . The system of claim 15 , wherein the grinder is contained within the enclosure and the mixture inlet is a hazardous waste inlet.
17 . The system of claim 1 , further comprising an observation window in an outer wall of the enclosure, and an illuminator within the enclosure to enable external observation of the mixture segregation.
18 . The system of claim 12 , wherein the inert gas tank contains nitrogen.