Process for Producing Superabsorbents

    公开(公告)号:US20220016596A1

    公开(公告)日:2022-01-20

    申请号:US17289328

    申请日:2019-11-04

    Applicant: BASF SE

    Abstract: The invention relates to a process for producing superabsorbent polymer particles, comprising storing acrylic acid in at least one tank (B1) at a production site for acrylic acid and in at least one tank (B2) at a production site for superabsorbent polymer particles, wherein the at least one tank (B1) at the production site for acrylic acid and the at least one tank (B2) at the production site for superabsorbent polymer particles are interconnected by one single pipe line (3) and the flow inside the pipe line (3) is temporary reversed during interruptions of the production superabsorbent polymer particles.

    PROCESS FOR PRODUCING SUPERABSORBENT PARTICLES

    公开(公告)号:US20250041828A1

    公开(公告)日:2025-02-06

    申请号:US18694478

    申请日:2022-09-16

    Applicant: BASF SE

    Abstract: A process for producing surface postcrosslinked superabsorbent particles, wherein an aqueous monomer solution with a small amount of initiator is polymerized to give a polymer gel, the resultant polymer gel is extruded through a die plate, the extruded polymer gel is dried on an air circulation belt drier having one or more zones, and the resultant polymer particles are ground and classified and then thermally surface postcrosslinked, wherein the temperatures of the drying gas supplied in the course of drying in the forward zones of the air circulation belt drier are from 120 to 160° C., and the speeds of the air supplied are from 1.2 to 3.0 m/s.

    Process for producing superabsorbents

    公开(公告)号:US12161994B2

    公开(公告)日:2024-12-10

    申请号:US17289328

    申请日:2019-11-04

    Applicant: BASF SE

    Abstract: The invention relates to a process for producing superabsorbent polymer particles, comprising storing acrylic acid in at least one tank (B1) at a production site for acrylic acid and in at least one tank (B2) at a production site for superabsorbent polymer particles, wherein the at least one tank (B1) at the production site for acrylic acid and the at least one tank (B2) at the production site for superabsorbent polymer particles are interconnected by one single pipe line (3) and the flow inside the pipe line (3) is temporary reversed during interruptions of the production superabsorbent polymer particles.

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