Method for producing water-absorbent resin powder, and drying device and drying method for particulate hydrous gel
The production method includes a drying step of drying a particulate crosslinked hydrogel polymer obtained by polymerizing a monomer, which is a material of a water-absorbent resin, using a heating device to obtain dried particles. The heating device includes: a rotary container that contains the particulate crosslinked hydrogel polymer therein and rotates; and a plurality of heating tubes that are located within the rotary container, extend in an axial direction of the rotary container, and rotate together with the rotary container. A gel temperature of the particulate crosslinked hydrogel polymer to be subjected to the drying step, the gel temperature being measured by a contact thermometer, is not lower than 50° C.
1. A method for producing water-absorbent resin powder, the method comprising
a drying step of drying a particulate crosslinked hydrogel polymer obtained by polymerizing a monomer aqueous solution containing a monomer, which is a material of a water-absorbent resin, using a heating device to obtain dried particles, wherein
the heating device includes: a rotary container that contains the particulate crosslinked hydrogel polymer therein and rotates; and a plurality of heating tubes that are located within the rotary container, extend in an axial direction of the rotary container, and rotate together with the rotary container, and
a gel temperature of the particulate crosslinked hydrogel polymer to be subjected to the drying step, the gel temperature being measured by a contact thermometer, is not lower than 50° C.
2. The method according to claim 1 , wherein a heat medium of 150° C. or higher is supplied to the heating tubes.
3. The method according to claim 1 , wherein a temperature of an inner surface of the rotary container is not lower than 150° C.
4. The method according to claim 1 , wherein a temperature of an inner surface of the rotary container is set to be not lower than 150° C. before the particulate crosslinked hydrogel polymer is put inside.
5. The method according to claim 1 , wherein a gas is introduced as a heat medium into the rotary container, and a temperature of an inner surface of the rotary container is higher than a temperature of the gas.
6. The method according to claim 5 , wherein the temperature of the gas to be introduced into the rotary container is not lower than 100° C.
7. The method according to claim 1 , further comprising a cooling step of cooling the dried particles.
8. The method according to claim 1 , wherein, in the drying step, an additive is added during heating drying of the particulate crosslinked hydrogel polymer contained in the rotary container.
9. The method according to claim 8 , wherein the additive is a surface-crosslinking agent.
10. The method according to claim 1 , wherein the particulate crosslinked hydrogel polymer contains a gel fluidizer.
11. The method according to claim 1 , wherein the gel temperature of the particulate crosslinked hydrogel polymer to be subjected to the drying step is 60 to 120° C.
12. The method according to claim 1 , wherein a particle diameter d 1 of the particulate crosslinked hydrogel polymer to be subjected to the drying step is not greater than 800 μm.
13. The method according to claim 1 , wherein steam of 0.49 MPa or greater is introduced into the plurality of heating tubes.
14. The method according to claim 1 , wherein a Froude number Fr of the heating device is 0.001 to 1.
15. The method of claim 1 , wherein the heating device comprises not less than five of the heating tubes.
16. The method of claim 1 , wherein the heating device comprises a heating means or a thermal insulating means on an outer peripheral surface of the rotary container.
17. The method of claim 1 , wherein the rotary container is inclined from one end toward another end of the rotary container.
18. The method of claim 1 , wherein the rotary container comprises at least one obstructive wall within the rotary container.
19. The method of claim 1 , wherein the heating device has a ratio of a heat transfer area to an effective capacity of the rotary container (heat transfer area/effective capacity) of not less than 10 m −1 , wherein the heat transfer area is a sum of surface areas of outer peripheral surfaces of the heating tubes and an area of an inner peripheral surface of the rotary container.