IP Library Granted Patent US 10,429,128
Granted Patent B2
US 10,429,128 · App. 14/358,792 · Granted Oct 1, 2019

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

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,429,128
App. No.
14/358,792
Granted
Oct 1, 2019
Kind
B2
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.

Claims (17)

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.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 21, 2021
From: EVONIK OPERATIONS GMBH
To: EVONIK SUPERABSORBER GMBH
Reel/Frame 057885/0211 →
CHANGE OF NAME Recorded Dec 30, 2019
From: EVONIK DEGUSSA GMBH
To: EVONIK OPERATIONS GMBH
Reel/Frame 051449/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 2, 2014
From: GARTNER, HERBERT; HAGER, MARC; PLOCHINGER, HARALD; AUERNIG, SABINE; KOHLER, HANS-PETER; LACKER, ELISABETH
To: EVONIK DEGUSSA GMBH
Reel/Frame 033231/0505 →