Production method for water-absorbing resin
In obtaining a water-absorbing resin with high property in high productivity, produced a production method for a water-absorbing resin in high property and stably. Provided is a production method for a water-absorbing resin, comprising: a step for polymerizing an acrylic acid aqueous solution; a step for drying the resultant water-containing gel; a step for pulverizing and classifying the dried substance; and a step for surface cross-linking after classification, wherein a hopper having an inclination angle of a cone part of equal to or larger than 45 degree, and a drawing rate of 30 to 80% is used.
1. A production method for a water-absorbing resin, comprising:
polymerizing an acrylic acid aqueous solution to obtain a water-containing gel;
drying the water-containing gel to obtain a dried substance;
pulverizing and classifying the dried substance to obtain a powder substance; and
surface cross-linking of the powder substance,
wherein including and subsequent to the drying step, after storing the dried substance or the powder substance in a hopper having an inclination angle of a cone part of 65-85 degree, and a drawing rate of 30 to 80%, at least one or more places, the dried substance or the powder substance is discharged.
2. The production method for a water-absorbing resin according to claim 1 , wherein a shape of the hopper is an inverse circular truncated cone shape or an inverse truncated pyramid shape.
3. The production method according to claim 1 , wherein the drawing rate of the hopper is 35 to 80%.
4. The production method according to claim 1 , wherein a material of the hopper is stainless steel, and surface roughness (Rz) of the inner surface of the hopper is equal to or smaller than 800 nm.
5. The production method according to claim 1 , wherein the powder substance is a water-absorbing resin powder.
6. The production method according to claim 1 , wherein the hopper is installed between a step for pulverizing and classifying the dried substance, and a step for surface cross-linking the powder substance after classification.
7. The production method according to claim 1 , wherein the hopper is installed at two or more places.
8. The production method according to claim 1 , wherein the hopper is heated or retains heat.
9. The production method according to claim 1 , wherein the powder substance is heated or retains heat.
10. The production method according to claim 1 , wherein residence time of the powder substance in the hopper is controlled within 24 hours.
11. The production method according to claim 1 , wherein filling rate with the powder substance in the hopper is controlled at equal to or lower than 90% by volume.
12. The production method according to claim 1 , wherein internal volume of the hopper is 1 to 100 m 3 .
13. The production method according to claim 1 , wherein moisture content of the water-absorbing resin is 0.5 to 20% by weight.
14. The production method according to claim 1 , further comprising a step for adding a polyvalent metal salt or a hydroxide.
15. The production method according to claim 1 , further comprising a step for adding a water-insoluble inorganic particle.
16. The production method according to claim 1 , further comprising a step for adding a chelating agent.
17. The production method according to claim 1 , further comprising a step for adding a surfactant.
18. The production method according to claim 1 , wherein the water-absorbing resin has a mass average particle diameter (D 50 ) of 200 to 600 μm, a ratio of particles of a 850 μm diameter to particles of a 150 μm diameter being equal to or higher than 95% by weight, and a logarithm standard deviation (σξ) of 0.20 to 0.40.
19. The production method according to claim 1 , wherein the water-absorbing resin has a CRC (ERT441.1-02) of 10 to 100 g/g, an AAP (ERT442.2-02,provided that a load is 50 g/cm 2 ) of 15 to 50 g/g, also a water-extractable content of equal to or lower than 30% by weight, an SFC, which is liquid permeation, of equal to or higher than 1 (unit: 10 −7 ·cm 3 ·s·g −1 ), and residual monomers of equal to or lower than 500 ppm by weight.
20. The production method according to claim 1 , wherein 4 times value of a standard deviation (σ) of at least either of the properties of AAP (ERT442.2-02, provided that a load is 50 g/cm 2 ) and CRC (ERT441.1-02) is 0 to 5.5% of an average value (arithmetic average) of the property provided that the standard deviation and the average value are specified by that analysis number “n” of equal to or more than 15, and production of equal to or higher than 15 ton.
21. The production method according to claim 1 , wherein it is a continuous production method of equal to or higher than 0.5 t/hr per one line.