Heat-treatment of water-absorbing polymeric particles in a fluidized bed at a fast heat-up rate

Patent metadata

Field	Value
Publication number	US-10429128-B2
Application number	US-201214358792-A
Country	US
Kind code	B2
Filing date	Dec 18, 2012
Priority date	Jan 27, 2012
Publication date	Oct 1, 2019
Grant date	Oct 1, 2019

Abstract

The present invention relates to a method for heat-treating water-absorbing polymeric particles at a temperature equal to or above 150° C. in a fluidized bed dryer at a fast heat-up rate, the use of a fluidized bed dryer for heat-treating water-absorbing polymeric particles in continuous or batch mode as well as to the heat-treated polymeric particles obtained by the method of the present invention.

First claim

The invention claimed is:

1. A method for heat-treating water-absorbing polymeric particles at a temperature T p1 equal to or above 150° C., wherein said water-absorbing polymeric particles comprise a residual amount of water being between 0.3 to 7 wt.-%, based on the composition, as determined by the EDANA standard test method WSP 203.3(10) when subjected to the heat treatment, the particles are heated in a fluidization chamber of a fluidized bed dryer from an initial particle temperature T 0 equal to or below 50° C. to said temperature T p1 at a heat-up rate of at least 10° C. per minute to effect surface crosslinking of said water-absorbing polymeric particles.

2. The method according to claim 1 , wherein the polymeric particles are heated from said initial particle temperature T 0 to said temperature T p1 in less than 10 minutes and T p1 is in the range of from 170 to 245° C.

3. The method according to claim 1 , wherein said polymeric particles are obtained by polymerising a monomer mixture comprising at least one type of ethylenically unsaturated monomer, at least one type of cross-linker and at least one type of initiator.

4. The method according to claim 3 , wherein the monomer mixture additionally comprises at least one polyhydric alcohol as an additional cross-linker in an amount of at least 50 ppm, based on the total weight of ethylenically saturated monomer.

5. The method according to claim 4 , wherein the polyhydric alcohol comprises glycerin.

6. The method according to claim 1 , wherein after being heated to a temperature T p1 , said polymeric particles are kept in the fluid bed dryer at a temperature T p2 , wherein T p1 and T p2 both are in the range of from 170 to 245° C.

7. The method according to claim 1 , wherein the water-absorbing polymeric particles are heated in the fluidization chamber for a residence time of from 5 to 60 minutes.

8. The method according to claim 1 , wherein a solution comprising at least one organic or inorganic cross-linking agent is applied to the surface of said polymeric particles.

9. The method according to claim 8 , wherein said solution comprises at least one compound selected from the group consisting of polyhydric alcohols, polyglycidyl compounds, cyclic carbonates, polyamines, alkoxysilyl compounds, polyaziridines, polyamidoamines, oxazolidones, bisoxazolines, water-soluble multivalent metal salts, metal oxides or mixtures thereof in an aqueous solvent.

10. The method according to claim 1 , wherein said particles are contacted inside said fluidized bed dryer with at least one hot gas stream having a temperature T g inside said fluidization chamber of said fluidized bed dryer, said fluidization chamber, opening downwardly in at least one lower plenum chamber through at least one gas distribution bottom plate having openings formed there through for upward gas flow from said lower plenum chamber into said fluidization chamber and wherein the superficial gas velocity of said hot gas stream in the fluidized bed is in the range of from 0.1 to 0.57 m/s.

11. The method according to claim 10 , wherein the pressure drop across the gas distribution bottom plate is in the range of from 100 to 900 Pa, and the total pressure drop across the bottom plate and the fluidized bed is in the range of from 2,500 to 5,000 Pa.

12. The method according to claim 2 , wherein the polymeric particles are heated from said initial particle temperature T 0 to said temperature T p1 in less than 10 minutes and T p1 is in the range of from 190 to 235° C.

13. The method according to claim 3 , wherein said ethylenically unsaturated monomer is an acrylic acid present at least partly in form of a salt.

14. The method according to claim 1 , wherein said polymeric particles comprise a residual amount of water being in the range of from 0.5 to 6 wt. %, based on the composition, as determined by the EDANA standard test method WSP 203.3(10).

15. The method according to claim 1 , wherein before being heat-treated, said polymeric particles are wetted at their surface by an amount of water being in the range of from 1 to 5 wt.-% based on the whole composition.

16. The method according to claim 1 , wherein before being heat-treated, said polymeric particles are wetted at their surface by an amount of water being in the range of from 1.5 to 3.5 wt.-% based on the whole composition.

17. The method according to claim 6 , wherein after being heated to a temperature T p1 , said polymeric particles are kept in the fluid bed dryer at a temperature T p2 , wherein T p1 and T p2 both are in the range of from 190 to 235° C.

Assignees

• Evonik Degussa Gmbh

Inventors

• Gartner Herbert
• Hager Marc
• Plochinger Harald
• Auernig Sabine
• Kohler Hans-Peter
• Lacker Elisabeth

Classifications

• B29B2009/168

  Removing undesirable residual components, e.g. solvents, unreacted monomers; Degassing · CPC title

• C08J3/00

  Processes of treating or compounding macromolecular substances · CPC title

• C08J3/124

  Treatment for improving the free-flowing characteristics · CPC title

• F26B3/00 Primary

  Drying solid materials or objects by processes involving the application of heat (in specific machines or apparatus F26B9/00 - F26B19/00) · CPC title

• B29B9/16 Primary

  Auxiliary treatment of granules · CPC title