Polyacrylic acid (salt)-type water absorbent resin and method for producing of same
Disclosed is a method for producing a water absorbent resin, by which a surface-crosslinked water absorbent resin having excellent physical properties can be efficiently obtained at low cost, while assuring high productivity. When the production scale is increased to a continuous production at 1 t/hr or more, the physical properties are improved and stabilized (for example, standard deviation of the physical properties is reduced) by a surface-crosslinking treatment, and the absorption against pressure (AAP) and liquid permeability (SFC) are further improved. Specifically disclosed is a method for producing a water absorbent resin, which is characterized in that the stirring shaft of the continuous mixing apparatus for the surface-crosslinking agent is heated during the mixing step of the surface-crosslinking agent or that the continuous mixing apparatus for the surface-crosslinking agent is operated at a pressure that is reduced relative to the ambient pressure and a gas flow is passed through the mixing apparatus during the mixing of the surface-crosslinking agent so that the gas flow in the mixing apparatus is 40° C. or more (when defined with respect to the gas temperature at the exit).
1. A method for producing a polyacrylic acid (salt)-type water absorbent resin comprising steps of:
preparing an aqueous monomer solution of an acrylic acid (salt),
continuously polymerizing the aqueous monomer solution into a hydrous gel-like crosslinked polymer,
finely shredding the hydrous gel-like crosslinked polymer during or after polymerization,
drying the obtained particulate hydrous gel-like crosslinked polymer to obtain a dried water absorbent resin powder,
adding a surface-crosslinking agent to the dried water absorbent resin powder with a continuous mixing apparatus, wherein the pressure inside of the continuous mixing apparatus is a reduced pressure greater than 0 kPa and is 10 kPa or lower than atmospheric pressure, and
carrying out reaction of the mixture, wherein
a stifling shaft of the continuous mixing apparatus for the surface-crosslinking agent is heated in the step of mixing the surface-crosslinking agent.
2. A method for producing a polyacrylic acid (salt)-type water absorbent resin comprising steps of:
preparing an aqueous monomer solution of an acrylic acid (salt),
continuously polymerizing the aqueous monomer solution into a hydrous gel-like crosslinked polymer,
finely shredding the hydrous gel-like crosslinked polymer during or after polymerization,
drying the obtained particulate hydrous gel-like crosslinked polymer to obtain a dried water absorbent resin powder,
adding a surface-crosslinking agent to the dried water absorbent resin powder with a continuous mixing apparatus, and
carrying out reaction of the mixture, wherein
the continuous mixing apparatus for the surface-crosslinking agent is operated at below ambient pressure and at a gas current of at least 40° C. to adjust the outlet gas temperature of the gas current in the mixing apparatus during mixing the surface-crosslinking agent, wherein the pressure inside of the continuous mixing apparatus is a reduced pressure greater than 0 kPa and is 10 kPa or lower than atmospheric pressure.
3. The production method according to claim 1 or 2 , wherein the stirring shaft of the continuous mixing apparatus for the surface-crosslinking agent is so heated as to be at a higher temperature than the inner wall temperature of the continuous mixing apparatus.
4. The production method according to claim 1 or 2 , wherein the pressure of the inside of the continuous mixing apparatus for surface-crosslinking agent is reduced.
5. The production method according to claim 1 or 2 , wherein 50 to 100% in the inner surface area of the continuous mixing apparatus is of a metal.
6. The production method according to claim 1 or 2 , wherein the inner face of the inside of the continuous mixing apparatus for the surface-crosslinking agent is of a stainless steel with a surface roughness (Rz) of 800 nm or lower.
7. The production method according to claim 1 or 2 , wherein the reaction step for the mixture is carried out at 150° C. to 250° C.
8. The production method according to claim 1 or 2 , wherein the water absorbent resin powder is pneumatically transported by using compressed air with a dew point of −5° C. to −100° C.
9. The production method according to claim 1 or 2 , wherein the mixing apparatus is a hoe type blender.
10. The production method according to claim 1 or 2 , wherein the temperature of the mixture is 50 to 95° C. until the mixture flows to the reaction step after the surface-crosslinking agent is mixed.
11. The production method according to claim 1 or 2 , wherein the reaction step of the mixture has two or more lines in the polymerization step.
12. The production method according to claim 1 or 2 , wherein the average residence time of the water absorbent resin in the continuous mixing apparatus is within 1 minute.
13. The production method according to claim 1 or 2 , wherein the temperature of the mixture is increased by 0.5° C. or more by continuously mixing the crosslinking agent to the dried water absorbent resin powder.
14. The production method according to claim 1 or 2 , wherein the water absorbent resin has 20 g/g or higher of water absorption against pressure (AAP) for an aqueous 0.9 wt. % sodium chloride solution at a pressure of 4.8 kPa, 1 (×10 −7 ·cm 3 ·s·g −1 ) or higher of saline flow conductivity of 0.69 wt. % physiological saline solution (SFC), and 20 g/g or higher of water absorption under no pressure (CRC).