# US 8,785,583 B2 · Process for continuously producing water-absorbing polymer particles

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- Number: US 8,785,583 B2
- Document ID: US8785583B2
- Status: Granted
- Kind: B2
- Application number: 13/484,849
- Filed: 2012-05-31
- Published: 2012-12-06
- Granted: 2014-07-22
- Earliest claimed: 2011-06-03
- Assignees: BASF SE
- Applicants: Rüdiger Funk; Thomas Pfeiffer; Jürgen Schröder
- Inventors: Rüdiger Funk; Thomas Pfeiffer; Jürgen Schröder
- Web page: https://patentgrep.com/patent/US8785583B2

## CPC

- C08F 220/20: of polyhydric alcohols or phenols {, e.g. 2-hydroxyethyl (meth)acrylate or glycerol mono-(meth)acrylate}
- B01J 19/28: Moving reactors, e.g. rotary drums (B01J19/08 takes precedence)
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS

## Abstract

A process for continuously producing water-absorbing polymer particles by polymerizing a monomer solution comprising acrylic acid and/or salts thereof, wherein the acrylic acid supplied has a dimeric acrylic acid content of at least 0.02% by weight and the dimeric acrylic acid content is kept essentially constant.

## Claims

### Claim 1

A process for continuously producing water-absorbing polymer particles, comprising polymerization of a monomer solution or suspension comprising
a) acrylic acid which may be at least partly neutralized,
b) at least one crosslinker,
c) at least one initiator,
d) optionally one or more ethylenically unsaturated monomer copolymerizable with acrylic acid, and
e) optionally one or more water-soluble polymer, to give a polymer gel, drying the resulting polymer gel, comminution of the dried polymer gel to give polymer particles, and classifying the resulting polymer particles, wherein the acrylic acid is supplied continuously and the acrylic acid supplied continuously has a dimeric acrylic acid content of 0.02% to 1% by weight and the dimeric acrylic acid content is kept essentially constant.

### Claim 2 (depends on 1)

The process according to claim 1, wherein the dimeric acrylic acid content in the the acrylic acid supplied continuously varies by less than 10% within 24 hours.

### Claim 3 (depends on 1)

The process according to claim 1, wherein acrylic acid from at least two storage tanks is used.

### Claim 4 (depends on 2)

The process according to claim 2, wherein the acrylic acid in one of the storage tanks has a dimeric acrylic acid content of at least 0.1% by weight.

### Claim 5 (depends on 1)

The process according to claim 1, wherein the water-absorbing polymer particles are surface postcrosslinked.

### Claim 6 (depends on 1)

The process according to claim 1, wherein the water-absorbing polymer particles are surface postcrosslinked and remoisturized.

### Claim 7 (depends on 1)

The process according to claim 1, wherein the water-absorbing polymer particles are surface postcrosslinked and remoisturized at a temperature of at least 50° C.

### Claim 8 (depends on 1)

The process according to claim 1, wherein the water-absorbing polymer particles have a water content of 1 to 10% by weight.

### Claim 9 (depends on 1)

The process according to claim 1, wherein the water-absorbing polymer particles have a centrifuge retention capacity of at least 15 g/g.