Manufacturing method for polyacrylic acid (salt) -based water-absorbent resin powder
一种制造方法、树脂粉末的技术,应用在涂层等方向,能够解决吸水速度和通液性困难、吸水速度、通液性变大等问题,达到操作性和混合比率的稳定性优异、保存稳定性提高、降低残留副产物的效果
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manufacture example 1
[0762] As a continuous production device (capacity 1500 [kg / hr]) of water-absorbent resin powder, prepared from the polymerization process, gel pulverization process, drying process, pulverization process, classification process, surface crosslinking process (spraying process, heat treatment process) , cooling process), sizing process, and a device that connects the conveying process between the various processes. The continuous production apparatus was operated under the operating conditions of each process described below, and the continuous production of the water-absorbent resin powder was started. In addition, in the manufacture example 1, the manufacture of the water-absorbent resin particle (a) before surface crosslinking is demonstrated.
[0763] First, as a polymerization step, 0.09 mol% (relative to the monomer) of acrylic acid as an internal crosslinking agent was added to an acrylic acid partially neutralized sodium salt aqueous solution (monomer concentration: 38%...
manufacture example 2
[0768] In the same manner as in Production Example 1, as a continuous production apparatus (capacity 1500 [kg / hr]) of water-absorbent resin powder, a polymerization process, a gel pulverization process, a drying process, a pulverization process, a classification process, and a surface crosslinking process were prepared. (spraying process, heat treatment process, cooling process), sizing process, and a conveying process that connects each process. The continuous production apparatus was operated under the operating conditions of each process described below, and the continuous production of the water-absorbent resin powder was started. In addition, in the manufacture example 2, the manufacture of the water-absorbent resin particle (b) before surface crosslinking is demonstrated.
[0769] In Production Example 2, the same operations as in Production Example 1 were performed except that the conditions shown below were changed. That is, the amount of polyethylene glycol diacrylat...
Embodiment 1
[0771] (melting and storage of ethylene carbonate)
[0772] As a melting device for ethylene carbonate, a double-arm type kneader with an internal volume of 500 L including a jacket through which a heating medium could flow and a scraper stirring shaft was prepared.
[0773] After putting 300 kg of ethylene carbonate in the form of a solid sheet (a few mm on one side) into the double-arm kneader, pass warm water at 80°C through the jacket and the scraper stirring shaft, and rotate the scraper stirring blade at 10 rpm to start solid-state kneading. Melting of ethylene carbonate.
[0774] Stirring was stopped when the temperature of molten ethylene carbonate reached 50° C., and it was transported and stored in an intermediate tank (raw material tank) in a molten (heated) state. This transportation was carried out using a transportation pipe and a pump that were heat-retained with warm water at 50°C. It should be noted that a filter is provided before the pump. In addition, th...
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