Coating methods using organosilica materials and uses thereof
US-2016167016-A1 · Jun 16, 2016 · US
US2018229211A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018229211-A1 |
| Application number | US-201815954917-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 17, 2018 |
| Priority date | Nov 10, 2015 |
| Publication date | Aug 16, 2018 |
| Grant date | — |
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Copper adsorbents which are resistant to the reduction by the components of the synthesis gas at normal operation conditions. The adsorbents are produced by admixing small amounts of an inorganic halide, such as NaCl, to the basic copper carbonate precursor followed by calcination at a temperature sufficient to decompose the carbonate. The introduction of the halide can be also achieved during the forming stage of adsorbent preparation. These reduction resistant copper oxides can be in the form of composites with alumina and are especially useful for purification of synthesis gas and the removal of mercury, arsine, phosphine, as well as hydrogen sulfide.
Opening claim text (preview).
1 . A process for removing contaminants from a stream, the process comprising: contacting a stream with a sorbent in a contaminant removal zone, wherein the sorbent comprises copper, cupric oxide, cuprous oxide, and a halide, the stream comprising at least hydrogen and including one or more contaminants selected from a group consisting of mercury, arsenic, phosphine and sulfur compounds; and, selectively removing one or more of the contaminants from the stream to provide a purified stream. 2 . The process of claim 1 wherein the sorbent further comprises a porous support material selected from a group consisting of alumina, silica, silica-aluminas, silicates, aluminates, silico-aluminates, zeolites, titania, zirconia, hematite, ceria, magnesium oxide, and tungsten oxide. 3 . The process of claim 2 wherein the porous support material comprises a transition alumina formed by a flash calcination of aluminum hydroxide. 4 . The process of claim 1 , wherein the stream comprises a stream of synthesis gas. 5 . The process of claim 1 , wherein the sorbent comprises from approximately 1 to approximately 35 wt % copper. 6 . The process of claim 1 , further comprising at least one of: sensing at least one parameter of the process and generating a signal or data from the sensing; generating and transmitting a signal; or generating and transmitting data. 7 . The process of claim 1 , wherein the sorbent comprises from approximately 0.05 to approximately 2 wt % of the halide. 8 . A process for removing contaminants from a stream, the process comprising: passing a stream to a contaminant removal zone, the stream comprising at least hydrogen and including one or more contaminants selected from a group consisting of mercury, arsenic, phosphine and sulfur compounds and the contaminant removal zone comprising a sorbent configured to selectively remove one or more contaminants from the stream, wherein the sorbent comprises copper, cupric oxide, cuprous oxide, and a halide; and, recovering a purified stream from the contaminant removal zone. 9 . The process of claim 8 further comprising loading pristine sorbent into the contaminant removal zone before the stream comprising at least hydrogen is passed to the contaminant removal zone. 10 . The process of claim 9 further comprising reducing the pristine sorbent in the contaminant removal zone with hydrogen from the stream comprising hydrogen. 11 . The process of claim 10 wherein the stream comprising at least hydrogen is passed to the contaminant removal zone after the pristine sorbent is loaded into the contaminant removal zone without drying the sorbent. 12 . The process of claim 8 wherein the sorbent comprises between approximately 0.05 to 2 wt % of the halide. 13 . The process of claim 8 wherein the sorbent further comprises a support material selected from a group consisting of alumina, silica, silica-aluminas, silicates, aluminates, silico-aluminates, zeolites, titania, zirconia, hematite, ceria, magnesium oxide, and tungsten oxide. 14 . The process of claim 8 , wherein the sorbent comprises from 1 to 35 wt % total copper. 15 . The process of claim 14 , wherein the cuprous oxide comprises from approximately 45 to approximately 75% of the copper in the sorbent. 16 . The process of claim 8 , wherein the sorbent is at least partially sulfided. 17 . A process for removing contaminants from a stream, the process comprising: forming a sorbent from a mixture of a porous support, a basic copper carbonate, and a halide material; activating the sorbent such that the sorbent comprises copper, cupric oxide, and cuprous oxide; loading the sorbent into a contaminant removal zone after the sorbent has been activated; passing a stream comprising at least hydrogen to the contaminant removal zone configured to remove at least one contaminant selected from a group consisting of mercury, arsenic, phosphine and sulfur compounds from the stream and provide a purified stream. 18 . The process of claim 17 wherein the sorbent comprises a plurality of particles and at least some of the particles have a 7×8 mesh size. 19 . The process of claim 18 wherein the particles comprises porous beads with a bulk density between 640 kg/nr to 1280 kg/nr. 20 . The process of claim 18 , wherein the sorbent comprises between 1 to 35 wt % total copper and from approximately 45 to approximately 75% of the copper in the sorbent comprises cuprous oxide.
Hydrogen sulfide · CPC title
Coated, impregnated or composite adsorbents · CPC title
Sulfur containing contaminants, e.g. hydrogen sulfide · CPC title
Carbonoxysulfide COS · CPC title
with selectively adsorptive solids, e.g. active carbon · CPC title
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