Method for preparing a sorbent
US-2016279596-A1 · Sep 29, 2016 · US
US2018154331A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018154331-A1 |
| Application number | US-201815887727-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 2, 2018 |
| Priority date | Aug 12, 2015 |
| Publication date | Jun 7, 2018 |
| Grant date | — |
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A composition capable of removing chlorides from a gaseous stream and a process of using same. The compositions have sufficient chloride capacity, offer comparable creation of green oil, and have sufficient structural integrity to be utilized as sorbents in a chloride removal process. Generally, the compositions include a first zinc carbonate, a second zinc carbonate different than the first zinc carbonate and an alumina material. The composition has been cured at a temperature between about 149 to 399° C. The first zinc carbonate may comprise hydrozincite and the second zinc carbonate may comprise smithsonite.
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What is claimed is: 1 . A composition comprising: a first zinc carbonate; a second zinc carbonate different than the first zinc carbonate; an alumina material, wherein the alumina material comprises less than 10 wt % of the composition, and wherein the first zinc carbonate comprises hydrozincite, and wherein the composition has been cured at a temperature between 149 to 399° C. 2 . The composition of claim 1 wherein the second zinc carbonate comprises smithsonite. 3 . The composition of claim 1 wherein the alumina material comprises less than 5 wt % of the composition. 4 . The composition of claim 1 wherein the composition includes at least two pairs of x-ray diffraction peaks at a two-theta value selected from a group consisting of: about 12.80 and about 17.30; about 13.00 and about 36.00; and, about 25.00 and about 32.50. 5 . The composition of claim 4 , wherein the composition further includes at least one x-ray diffraction peak or pair of peaks at a two-theta value selected from a group consisting of: about 34.30; about 35.00 and 38.00; and, about 30.50 and about 34.50. 6 . The composition of claim 1 wherein the composition has been cured at a temperature between 260 to 316° C. 7 . The composition of claim 1 wherein the composition lacks an x-ray diffraction peak at a two-theta value of about 14.50. 8 . The composition of claim 1 further comprising: zinc oxide. 9 . The composition of claim 1 further comprising: about 42 wt % zinc. 10 . The composition of claim 8 further comprising: about 16 wt % sodium. 11 . A composition for adsorbing chloride compounds, the composition comprising: a first zinc carbonate, wherein the first zinc carbonate comprises hydrozincite or smithsonite; a second zinc carbonate different than the first zinc carbonate; an alumina material; and, zinc oxide. 12 . The composition of claim 11 wherein the composition includes at least two pairs of x-ray diffraction peaks at a two-theta value selected from a group consisting of: about 12.80 and about 17.30; about 13.00 and about 36.00; and, about 25.00 and about 32.50. 13 . The composition of claim 11 wherein the first zinc carbonate comprises hydrozincite, and wherein the second zinc carbonate comprises smithsonite. 14 . The composition of claim 13 , wherein the composition has been cured at a temperature between 260 to 316° C. 15 . The composition of claim 11 further comprising: sodium carbonate. 16 . The composition of claim 15 wherein the composition comprises about 42 wt % zinc and about 16 wt % sodium. 17 . The composition of claim 11 wherein the composition is substantially free of boehmite. 18 . A process for removing chloride compounds from a gaseous stream, the process comprising: passing a gaseous stream to an adsorption zone, the adsorption zone comprising an adsorbent and being operated under conditions to remove chloride compounds from the gaseous stream, wherein the adsorbent comprises a first zinc carbonate being hydrozincite or smithsonite, a second zinc carbonate different than the first zinc carbonate, and, zinc oxide. 19 . The process of claim 18 wherein the adsorbent comprises about 42 wt % zinc. 20 . The process of claim 19 wherein the first zinc carbonate comprises smithsonite, and wherein the second zinc carbonate comprises hydrozincite, and wherein the adsorbent is substantially free of boehmite.
comprising aluminium oxide or hydroxide; comprising bauxite · CPC title
being less than 0.5 ml/g · CPC title
Hydrochloric acid · CPC title
Carbonates or bicarbonates, e.g. limestone, dolomite, aragonite · CPC title
Surface area, e.g. B.E.T specific surface area · CPC title
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