Systems and methods for water gas shift with reduced steam consumption
US-2016311682-A1 · Oct 27, 2016 · US
US9757685B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9757685-B2 |
| Application number | US-201314082253-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 18, 2013 |
| Priority date | Nov 19, 2012 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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Preparation of aqueous slurries of calcium dihydroxide. Preparation of aqueous suspensions of calcium hydroxide.
Opening claim text (preview).
The invention claimed is: 1. A process for the preparation of an aqueous slurry of calcium hydroxide, the process comprising: agitating a mixture of water and a copolymer to form an aqueous solution; adding powdered calcium hydroxide to said aqueous solution and agitating to provide an initial slurry; applying a homogeneous shear level greater than 50,000 s −1 to the initial slurry; and optionally, while applying said shear level to said initial slurry, adding more copolymer and/or more powdered calcium hydroxide to said initial slurry, wherein said copolymer consists: of methacrylic acid monomers and/or any of its salts, optionally of acrylic acid monomers and/or any of its salts, of one or more monomers with the formula (I): R—X—R′ (I) wherein: R represents a polymerizable unsaturated group, R′ represents hydrogen or an alkyl group with from 1 to 4 carbon atoms, X represents a structure with n unit(s) of ethylene oxide EO and m unit(s) of propylene oxide PO, arranged randomly or regularly, and m and n are independent non-zero integers and are between 1 and 150, and wherein said process produces an aqueous slurry of calcium hydroxide with a dry content of at least 40% by weight, the viscosity of the aqueous slurry measured by a Brookfield DVIII viscometer at 10 RPM being between 25 and 1,000 mPa·s at 20° C. 2. The process according to claim 1 , wherein the copolymer has a molecular mass between 30,000 and 200,000 g/mol as determined by Gel Permeation Chromatography (GPC). 3. The process according to claim 1 , wherein the monomer of formula (I) is such that n+m 17. 4. The process according to claim 1 , wherein the R group of said monomer of formula (I) represents the methacrylate group. 5. The process according to claim 1 , wherein the R′ group of the monomer of formula (I) represents H or CH 3 . 6. The process according to claim 1 , wherein the monomer of formula (I) consists of, expressed as a percentage by weight of each of its components: 5 to 30% by weight of methacrylic acid monomers and/or any of its salts, 0 to 10% by weight of acrylic acid monomers and/or any of its salts, 70 to 95% by weight of monomers of formula (I). 7. The process according to claim 1 , wherein a mixer of the rotor-stator type is used to apply said shear. 8. The process according to claim 1 , wherein the shear is applied in a device equipped with a recirculating loop. 9. The process according to claim 1 , wherein the shear is applied in a device configured to deliver an output of at least 1,000 W/m 3 . 10. The process according to claim 1 , wherein the R group of said monomer of formula (I) represents an acrylate, methacrylate, methacrylurethane, vinyl or allyl group.
Selection of liquid materials for use as absorbents · CPC title
Heavy metals or compounds thereof, e.g. mercury · CPC title
characterised by a specific solution or suspension · CPC title
of calcium · CPC title
Oxides or hydroxides (production of lime C04B2/00) · CPC title
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