Anionic preflocculation of fillers used in papermaking
US-2015167245-A1 · Jun 18, 2015 · US
US11155478B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11155478-B2 |
| Application number | US-201715648891-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 13, 2017 |
| Priority date | Jul 15, 2016 |
| Publication date | Oct 26, 2021 |
| Grant date | Oct 26, 2021 |
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A transitional treatment composition and methods of treating coal refuse are provided. The transitional treatment composition comprises an anionic acrylate-acrylamide copolymer having from about 30 mole percent to about 50 mole percent (meth)acrylate, from about 50 mole percent to about 70 mole percent (meth)acrylamide, and a reduced specific viscosity of from about 18 dL/g to about 30 dL/g. The transitional treatment composition can be made down in an aqueous liquid.
Opening claim text (preview).
The invention claimed is: 1. A composition consisting of: a coal refuse comprising 20 wt % to 80 wt % non-expandable clay; and an anionic acrylate-acrylamide copolymer having from about 36 mole percent to about 44 mole percent (meth)acrylate and about 56 mole percent to about 64 mole percent (meth)acrylamide, and a reduced specific viscosity of from about 22 dL/g to about 28 dL/g. 2. The composition of claim 1 , wherein the composition is aqueous slurry. 3. The composition of claim 1 , wherein the (meth)acrylate is acrylate. 4. The composition of claim 1 , wherein the (meth)acrylamide is acrylamide. 5. The composition of claim 1 , wherein the anionic acrylate-acrylamide copolymer has a weight average molecular weight of from about 4 million to about 7 million Daltons. 6. The composition of claim 5 , wherein the anionic acrylate-acrylamide copolymer has a weight average molecular weight of from about 5 million to about 7 million Daltons. 7. The composition of claim 6 , wherein the anionic acrylate-acrylamide copolymer has a weight average molecular weight of from about 6 million to about 7 million Daltons. 8. The composition of claim 1 , wherein the non-expandable clay comprises illite, kaolinite, or a combination thereof. 9. A method of treating coal refuse consisting of: combining an anionic acrylate-acrylamide copolymer having from about 36 mole percent to about 44 mole percent (meth)acrylate, from about 56 mole percent to about 64 mole percent (meth)acrylamide, and a reduced specific viscosity of from about 22 dL/g to about 28 dL/g and coal refuse comprising 20 wt % to 80 wt % non-expandable clay. 10. A method of separating water from coal refuse consisting of: combining an anionic acrylate-acrylamide copolymer having from about 36 mole percent to about 44 mole percent (meth)acrylate, from about 56 mole percent to about 64 mole percent (meth)acrylamide, and a reduced specific viscosity of from about 22 dL/g to about 28 dL/g and coal refuse comprising 20 wt % to 80 wt % non-expandable clay downstream of a coal flotation operation to form treated coal refuse; and allowing the treated coal refuse to stand in a settling vessel to form a top layer comprising water having turbidity less than about 200 NTU, and a bottom layer comprising settled treated coal refuse; and optionally, transferring at least a portion of a layer from the settling vessel. 11. The method of claim 10 , further comprising transferring at least a portion of the bottom layer from the settling vessel. 12. The method of claim 10 , further comprising transferring at least a portion of the top layer from the settling vessel. 13. The method of claim 12 , wherein the portion of the top layer is transferred from the settling vessel via overflow. 14. The method of claim 10 , wherein the top layer has a turbidity less than about 100 NTU. 15. The method of claim 10 , wherein the top layer has a turbidity less than about 80 NTU. 16. The method of claim 10 , wherein the top layer has a turbidity less than about 60 NTU. 17. The method of claim 10 , wherein the bottom layer settles at a rate of from about 10 to about 15 inches per minute. 18. The method of claim 10 , wherein the anionic acrylate-acrylamide copolymer and the coal refuse are combined at a plurality of feed points of the anionic acrylate-acrylamide copolymer. 19. The method of claim 18 , wherein the plurality of feed points is at least three feed points.
Processes including a sedimentation step · CPC title
Inorganic compounds · CPC title
Macromolecular compounds · CPC title
Acrylamide; Methacrylamide · CPC title
Flocculation · CPC title
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