Absorbing structure having improved blocking properties

1. A process for making an absorbing polymer structure (Pa) comprising the following steps:

preparing an absorbing polymer comprising the step of polymerizing

(α1) 0.1 to 99.999 wt. % of polymerized, ethylenically unsaturated, acid group-containing monomers or their salts, or polymerized, ethylenically unsaturated monomers containing a protonated or quaternated nitrogen atom, or their mixtures; and

(α2) 0.001 to 10 wt. % of a crossliniking agent,

resulting in an untreated dried absorbing polymer structure (Pu) having an outer region and an absorption under load (AUL) at a load of 0.3 psi (AUL 0.3 ), and an absorption under load at a load of 0.9 psi (AUL 0.9 ), and having a centrifuge retention capacity (CRC) of from 10 to 100 g/g;

preparing a treated absorbing polymer structure (Pb) comprising the steps of treating the outer region of the untreated absorbing polymer structure (Pu) wherein the (AUL 0.3 ) is increased to at least 25 g/g, and the (AUL 0.9 ) is increased to at least 18 g/g; and further treating the outer surface of the treated absorbing polymer structure (Pb) with a coating agent to reduce the (AUL 0.3 ), and the (AUL 0.9 ) values of the treated polymer structure (Pb).

2. The process according to claim 1 , wherein the centrifuge retention capacity (CRC) of the treated absorbing polymer structure (Pb) is reduced less in percentage terms referred in the value before the contact, than the reduction in percentage terms in the value of the (AUL 0.3 ).

3. The process according to claim 1 , wherein the-coating agent comprises an organic constituent and an inorganic constituent.

4. The process according to claim 1 , wherein the untreated absorbing polymer structure (Pu) exhibits at least one of the following properties:

(a) a maximum absorption of a 0.9 wt. % aqueous NaCl solution is in a range from 10 to 1000 ml/g,

(b) a fraction that can be extracted with a 0.9 wt. % aqueous NaCl solution is less than 30 wt. % referred to the untreated absorbing polymer structure,

(c) a swelling time to achieve 80% of the maximum absorption of a 0.9 wt. % aqueous NaCl solution is in the range from 0.01 to 180 minutes,

(d) a bulk density is in the range from 300 to 1000 g/l,

(e) a pH value of 1 g of the untreated absorbing polymer structure in 1 liter of water is in the range from 4 to 10,

(f) a gel stability is in the range from 1 to 100 sec. at a first measurement before a warming-up, and less than 30 sec. at a second measurement after the warming-up, or

(g) a penetration is at most 15 cm afler 2 hours or at most 20 cm after 24 hours.

5. The process according to claim 1 , wherein the treated absorbing polymer structure (Pb) exhibits at least one of the following properties:

(A) a maximum absorption of a 0.9 wt. % aqueous NaCl solution is in a range from 10 to 800 ml/g,

(B) a fraction that can be extracted with a 0.9 wt. % aqueous NaCl solution is less than 30 wt. % referred to the treated absorbing polymer structure,

(C) a swelling time to achieve 80% of the maximum absorption of a 0.9 wt. % aqueous NaCl solution is in the range from 0.01 to 180 minutes,

(D) a bulk density is in the range from 300 to 1000 g/l,

(E) a pH value of 1 g of the treated absorbing polymer structure in 1 liter of water is in the range from 4 to 10,

(F) a CRC is in the range from 10 to 100 g/g, or

(G) a gel stability is in the region of at least 500 sec. at a first measurement before a warming-up and at least 80 sec. at a second measurement after the warming-up.

6. The process according to claim 3 , comprising the step of contacting the treated absorbing polymer structure (Pb) with a wetting agent.

7. The process according to claim 6 , wherein the treated absorbing polymer structure (Pb) is first brought into contact with the coating agent and then with the wetting agent.

8. The process according to claim 1 , wherein the coating agent is a coating agent particle.

9. The process according to claim 8 , wherein the coating agent particle is smaller than the polymer structure.

10. The process according to claim 3 , wherein the organic constituent is selected from sodium carboxymethylcellulose and potassium carboxymethylcellulose and the inorganic constituent is a silicon compound.

11. The process according to claim 3 , wherein the organic constituent is a polymer (Ps).

12. The process according to claim 11 , wherein the polymer (Ps), in the form of a 4 wt. % solution in deionized water, has a viscosity at 20° C. in the range from 1 to 100,000 mPa·s.

13. The process according to claim 11 , wherein the polymer (Ps) is a saccharide.

14. The process according to claim 3 , wherein the inorganic constituent is a solid having at least one of the following properties:

(α) a BET surface of at least 10 m 2 /g,

(β) a pH value in a 4% aqueous dispersion in the range from 2 to 9, or

(γ) a compacted bulk density of less than 800 g/l.

15. The process according to claim 10 , wherein the inorganic constituent is a silica compound.

16. The process according to claim 1 , wherein the first treatment is carried out using a chemical crossliniking agent or by thermal crossliniking, or by both.

17. The process according to claim 1 , wherein the treated, absorbing polymer structure (Pb) has an inner region surrounded by the outer region, and the outer region has a higher degree of crossliniking than the inner region.

18. The process according to claim 17 , wherein the radius of the outer region is less than twice the radius of the inner region.

19. A process for making an absorbing polymer structure (Pa) comprising the steps of preparing an absorbing polymer comprising the steps of polymerizing

(α1) from 30 wt. % to 98.95 wt. % of a monoethylenically unsaturated, acid containing monomer, or salts thereof; and

(α2) 0.001 to 10 wt. % of a crossliniking agent,

said absorbing polymer resulting in an untreated dried absorbing polymer structure (Pu) having an outer surface region and an absorption under load (AUL) at a load of 0.3 psi, (AUL 0.3 ), and an absorption under load at a load of 0.9 psi, (AUL 0.9 ), and having a centrifuge retention capacity (CRC) of from 10 to 100 g/g;

preparing a treated absorbing polymer structure (Pb) comprising the steps of treating the outer region of the untreated absorbing polymer structure (Pu) wherein the (AUL 0.3 ) is increased to 30g/g or more, and the (AUL 0.9 ) is increased to 18 g/g or more;

and further treating the outer surface of the treated absorbing polymer structure (Pb) with a coating agent comprising carboxymethylcellulose wherein the (AUL 0.3 ) of the treated absorbing polymer structure (Pb) is reduced to less than 30 g/g, and the (AUL 0.9 ) of the treated absorbing polymer structure (Pb) is reduced to less than 18 g/g.

20. The process according to claim 19 , wherein the monoethylenically unsaturated, acid-containing monomer is acrylic acid.

21. The process according to claim 19 , wherein the coating agent further comprises a silica compound.