Method of selective extraction of platinoids, from a support containing same, with an extraction medium consisting of a supercritical fluid and an organic ligand
US-10494695-B2 · Dec 3, 2019 · US
US2016289792A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016289792-A1 |
| Application number | US-201615185113-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 17, 2016 |
| Priority date | Oct 22, 2014 |
| Publication date | Oct 6, 2016 |
| Grant date | — |
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A process is provided for preparing a spent noble metal fixed-bed catalyst for precious metals recovery, comprising: a) adding the catalyst to a caustic solution to wash the spent catalyst and to make a wash slurry having an alkaline pH, wherein the spent catalyst has been in contact with chloroaluminate ionic liquid catalyst, and wherein the spent catalyst comprises from 5 to 35 wt % chloride; and b) filtering the wash slurry and collecting: i) a filter cake having from at least 70 wt % of the chloride in the spent catalyst removed and having the noble metals retained, and ii) a wash filtrate. Also provided is a filter cake comprising a washed consolidated cake having 40 to 75 wt % solids, a cake moisture content from 25 to less than 60 wt %, 0.1 to 1.5 wt % total noble metals, and a residual chloride content of from zero to less than 4 wt %.
Opening claim text (preview).
It is claimed: 1 . A filter cake suitable for precious metals recovery, comprising: a washed consolidated cake having a % solids from 40 to 75 wt %, a cake moisture content from 25 to less than 60 wt %, 0.1 to 1.5 wt % total noble metals, and a residual chloride content of from zero to less than 4 wt % that is at least 80 wt % lower than an initial chloride content of a spent noble metal fixed-bed catalyst that had been in contact with a chloroaluminate ionic liquid catalyst and the chloroaluminate ionic liquid catalyst was trapped inside the spent noble metal fixed-bed catalyst. 2 . The filter cake of claim 1 , wherein the washed consolidated cake is not water reactive. 3 . The filter cake of claim 1 , wherein the washed consolidated cake comprises a filter aid. 4 . The filter cake of claim 3 , wherein the filter aid comprises from 50 to 98 wt % silica. 5 . The filter cake of claim 3 , wherein the filter aid is selected from the group consisting of diatomaceous earth, fly ash, perlite, cellulose, calcined rice hull ash, and fibers from used paper products. 6 . The filter cake of claim 5 , wherein the filter aid is calcined rice hull ash. 7 . The filter cake of claim 1 , wherein the washed consolidated cake comprises no aluminum hydroxide colloidal gels. 8 . The filter cake of claim 1 , wherein the cake moisture content is from 30 to less than 50 wt %. 9 . The filter cake of claim 1 , wherein the noble metals comprise platinum group metals. 10 . The filter cake of claim 9 , wherein the platinum group metals comprise platinum, palladium, or a mixture thereof.
General processes for recovering metals or metallic compounds from spent catalysts (for recovering specific metals C22B11/00 - C22B61/00) · CPC title
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