Method for producing water absorbent resin
The present invention is a method for producing a water absorbent resin which method is a method for producing surface cross-linked water absorbent resin particles, the method including the successive steps of: (a) adding a surface cross-linking agent and water to a particulate water absorbent resin in a mixer; and (b) reacting the resulting water absorbent resin mixture taken out from the mixer with the surface cross-linking agent in a reactor by heating or active energy ray irradiation, water vapor being used as part or all of the water added in the mixer. This makes it possible to provide a method for producing a water absorbent resin in which method a surface cross-linked water absorbent resin that has excellent properties can be obtained efficiently at low cost with high productivity.
1. A method for producing a water absorbent resin which method is a method for producing surface cross-linked water absorbent resin particles, wherein:
in the step (a) of adding a surface cross-linking agent and water to a particulate water absorbent resin in a mixer, a temperature of the particulate water absorbent resin is preset to 30° C. to 150° C.; and
a continuous mixing apparatus is used which meets the following requirements (i) through (iii):
(i) at least one stirring vane revolves at 300 rpm to 3000 rpm;
(ii) a revolving shaft of the at least one stirring vane is in a vertical direction; and
(iii) a mixing vessel is vertically divided into two or more rooms by a partition whose aperture ratio is 5% to 70%; and
the particulate water absorbent resin is supplied to the mixer in an amount of 10 kg/hr to 300 kg/hr per liter of the volume of the mixing vessel of the mixer.
2. The method as set forth in claim 1 , wherein an inner wall of the mixer is heated to 50° C. to 150° C.
3. The method as set forth in claim 1 , wherein a part or all of the inner wall of the mixer is made of a material which is in contact with water at an angle of not less than 60° and has a heat distortion temperature of not less than 70° C.
4. The method as set forth in claim 1 , wherein the mixer is provided with the partition whose aperture ratio is 5% to 70% and which rotates about the revolving shaft of the at least one stirring vane.
5. The method as set forth in claim 1 , wherein the mixer is provided with an outlet having a dam structure in which an angle with respect to a horizontal plane and/or a length in a horizontal direction from a side wall of the mixer to the revolving shaft can be changed provided that the angle falls within a range of 10° to 80° and the length falls within a range of 1% to 40% of a maximum radius of the mixing vessel.
6. The method as set forth in claim 1 , wherein the mixer has a value (H/D) of 0.1 to 1, the value being obtained by dividing a height (H) of an interior of the mixing vessel by a maximum diameter (D) of the mixing vessel.