Fluid catalytic cracking process and apparatus for maximizing light olefin yield and other applications
US-2020376456-A1 · Dec 3, 2020 · US
US12013182B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12013182-B2 |
| Application number | US-201917049238-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 5, 2019 |
| Priority date | Apr 24, 2018 |
| Publication date | Jun 18, 2024 |
| Grant date | Jun 18, 2024 |
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The invention relates to a method for drying a wet polymer composition obtained from a polymerization process, comprising: a) introducing the wet polymer composition and a drying gas into a fluidized bed dryer to form a fluidized bed of the wet polymer composition and b) heating the fluidized bed to obtain a dry polymer composition, wherein the fluidized bed further comprises an anti-fouling agent comprising inert nanoparticles.
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The invention claimed is: 1. A method for drying a wet polymer composition obtained from a polymerization process, comprising: a) introducing the wet polymer composition and a drying gas into a fluidized bed dryer to form a fluidized bed of the wet polymer composition and b) heating the fluidized bed to obtain a dry polymer composition, wherein the fluidized bed further comprises an anti-fouling agent comprising inert nanoparticles, wherein the wet polymer composition comprises powders of one or more polymers selected from the group consisting of polyolefins. 2. The method according to claim 1 , wherein the fluidized bed dryer contains internal heating elements. 3. A method according to claim 1 , wherein the wet polymer composition comprises powders of a polymer and residual volatile hydrocarbons used during the polymerization of the polymer, wherein the amount of the residual volatile hydrocarbons in the wet polymer composition is 5 to 50 wt %. 4. The method according to claim 1 , wherein the drying gas is selected from the group consisting of nitrogen, air and carbon dioxide. 5. The method according to claim 1 , wherein the amount of the anti-fouling agent is 0.1 to 5 wt %, of the dry polymer composition. 6. The method according to claim 1 , wherein the inert nanoparticles are selected from the group consisting of fumed silica, carbon black and organoclay. 7. The method according to claim 1 , wherein the anti-fouling agent consists of the inert nanoparticles or the anti-fouling agent comprises a hydrophobic coating provided on the inert nanoparticles. 8. The method according to claim 1 , wherein the method is a continuous process in which a flow of the wet polymer composition is continuously supplied to the fluidized bed dryer and a flow the dry polymer composition is continuously collected from the fluidized bed dryer. 9. The method according to claim 8 , wherein the anti-fouling agent is introduced into the fluidized bed dryer together with the wet polymer composition. 10. The method according to claim 8 , wherein the anti-fouling agent is introduced into the fluidized bed dryer together with the drying gas. 11. The method according to claim 1 , wherein the method is a batch-process in which the wet polymer composition is supplied to the fluidized bed dryer and dried and subsequently the dry polymer composition is collected from the fluidized bed dryer. 12. The method according to claim 11 , wherein the anti-fouling agent is introduced into the fluidized bed dryer together with the wet polymer composition. 13. The method according to claim 1 , further comprising the polymerization process to obtain the wet polymer composition. 14. The method according to claim 1 , wherein the anti-fouling agent is introduced into the fluidized bed dryer before step a) and the anti-fouling agent is not introduced into the fluidized bed dryer during or after steps a) and b). 15. The method according to claim 2 , wherein the internal heating elements have a surface temperature during step b) of from 70° C. to below the melting point of polymer in the wet polymer composition. 16. The method according to claim 1 , where the wet polymer composition comprises powders of one or more polymers selected from the group consisting of ethylene homopolymer, propylene homopolymer, and copolymers of ethylene or propylene with linear alpha olefins or dienes. 17. The method according to claim 5 , wherein the amount of the anti-fouling agent is 0.3 to 1.5 wt %, of the dry polymer composition. 18. A method for drying a wet polymer composition obtained from a polymerization process, comprising: a) introducing the wet polymer composition and a drying gas into a fluidized bed dryer to form a fluidized bed of the wet polymer composition and b) heating the fluidized bed to obtain a dry polymer composition, wherein the fluidized bed further comprises an anti-fouling agent comprising inert nanoparticles, wherein the wet polymer composition comprises powders of a polymer and residual volatile hydrocarbons used during the polymerization of the polymer, wherein the amount of the residual volatile hydrocarbons in the wet polymer composition is 5 to 50 wt %.
Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement (F26B13/00 takes precedence {; feed or discharge arrangements F26B25/002}) · CPC title
Silica · CPC title
Separation of polymers from solutions · CPC title
Controlling the temperature · CPC title
with introduction into the fluidised bed of more than one kind of moving particles · CPC title
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