Coating methods using organosilica materials and uses thereof
US-2016167016-A1 · Jun 16, 2016 · US
US9919285B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9919285-B2 |
| Application number | US-201314416443-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 10, 2013 |
| Priority date | Jul 26, 2012 |
| Publication date | Mar 20, 2018 |
| Grant date | Mar 20, 2018 |
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A sorbent is described, suitable for removing heavy metals, particularly mercury, from fluid streams including 20-75% by weight of copper (expressed as copper (II) oxide) in the form of one or more copper sulphides, the sorbent having a sulphur to copper atomic ratio in the range 0.7 to 0.95:1.
Opening claim text (preview).
The invention claimed is: 1. A sorbent suitable for removing mercury from fluid streams comprising 20-75% by weight of copper (expressed as copper (II) oxide) in the form of granules comprising one or more copper sulphide, a support and a binder, said sorbent having a sulphur to copper atomic ratio in the range 0.7 to 0.95:1, wherein the sorbent is formed by: (i) combining a copper oxide or copper hydroxycarbonate with one or more binders and a support material in a granulator to form a granulated sorbent precursor, (ii) sulphiding the sorbent precursor with a gas mixture comprising 0.5-5% by volume hydrogen sulphide at a temperature in the range of 1-150° C. to form a sulphided copper material, and (iii) partially reducing the sulphided copper material to a lower oxidation state with a hydrogen gas mixture containing 20-80% H 2 by volume at a temperature in the range 150-350° C. for 5-24 hours to form the sorbent. 2. A sorbent according to claim 1 , wherein the copper content of the sorbent is in the range of 20-40% by weight. 3. A sorbent according to claim 1 , wherein the S:Cu atomic ratio of the sorbent is in the range of 0.8-0.95. 4. A sorbent according to claim 1 , wherein the binder is a clay, cement or organic polymer binder, or a mixture thereof. 5. A sorbent according to claim 1 , wherein the support material is alumina, hydrated alumina, metal-aluminate, silica, titania, zirconia, zinc oxide, an aluminosilicate, a zeolite, metal carbonate, or carbon, or a mixture thereof. 6. A sorbent according to claim 1 further comprising one or more zinc compounds. 7. A method for the production of a sorbent comprising 20-75% by weight of copper (expressed as copper (II) oxide) in the form of granules comprising one or more copper sulphides, a support and a binder, said sorbent having a sulphur to copper atomic ratio in the range 0.7 to 0.95:1, comprising the steps of: (i) making a sorbent precursor comprising an oxide or hydroxycarbonate of copper by either applying a layer of a copper compound on the surface of a shaped support material by dipping or spraying the shaped support material with a slurry of copper compound, and drying the coated support material; or by combining an oxide or hydroxycarbonate of copper, with one or more binders and a support material (ii) sulphiding the sorbent precursor with a gas mixture comprising 0.5-5% by volume hydrogen sulphide at a temperature in the range 1-150° C. to form a sulphided copper material, and (iii) partially reducing the sulphided copper material to a lower oxidation state with a hydrogen gas mixture containing 20-80% H2 by volume at a temperature in the range 150-350° C. for 5-24 hrs to form the sorbent, wherein the sorbent precursor or sorbent is shaped. 8. A method according to claim 7 wherein the sulphiding stage is carried out with hydrogen sulphide in an inert gas at a H 2 S concentration in the range 0.5 to 5% by volume. 9. A method according to claim 7 wherein the reduction temperature is in the range 175-300° C. 10. A process for the removal of mercury from a process fluid stream by contacting the fluid stream with the sorbent according to claim 1 . 11. A process for the removal of mercury from a process fluid stream by contacting the fluid stream with the sorbent prepared according to the method of claim 7 . 12. A sorbent according to claim 2 wherein the S:Cu atomic ratio of the sorbent is in the range 0.8-0.9. 13. A method according to claim 9 wherein the reduction temperature is in the range 200-250° C.
containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts · CPC title
Inorganic carriers, supports or substrates · CPC title
Chemical treatments not covered by groups B01J20/3007 - B01J20/3078 · CPC title
Sulfides of compounds other than those provided for in B01J20/045 · CPC title
involving a post-treatment of the coated or impregnated product · CPC title
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