VERFAHREN ZUR SCHAUMHERSTELLUNG MITTELS UNTER DRUCK GELÖSTEM KOHLENDIOXID
    2.
    发明授权
    VERFAHREN ZUR SCHAUMHERSTELLUNG MITTELS UNTER DRUCK GELÖSTEM KOHLENDIOXID 失效
    程序对泡沫塑料生产BY压力下溶解的二氧化碳

    公开(公告)号:EP0907478B1

    公开(公告)日:2001-10-04

    申请号:EP97927040.2

    申请日:1997-05-26

    摘要: The invention relates to a process for continuous production of polyurethane slab-stock foam using carbon dioxide (40), dissolved physically under pressure, as the foaming agent. Before mixing the constituents polyhydric alcohol (36) and isocyanate (35), said carbon dioxide (40) is dissolved in the polyhydric alcohol constituent, and air or nitrogen (39) is dissolved in the isocyanate constituent. Both constituents are delivered to a mixing chamber (3) in which there is a pressure 70 to 150 % of the solution pressure of the CO2 in the polyhydric alcohol constituent. The isocyanate constituent is delivered at a pressure of at least 30 bar to the mixing chamber, and by dropping to the mixing chamber pressure is sprayed into said mixing chamber. Air or nitrogen amounting to 1 g per kg of CO2 is dissolved in the isocyanate constituent, and the mixture drops to atmospheric pressure on leaving the mixing chamber.

    VERFAHREN ZUR SCHAUMHERSTELLUNG MITTELS UNTER DRUCK GELÖSTEM KOHLENDIOXID
    6.
    发明公开
    VERFAHREN ZUR SCHAUMHERSTELLUNG MITTELS UNTER DRUCK GELÖSTEM KOHLENDIOXID 失效
    程序对泡沫塑料生产BY压力下溶解的二氧化碳

    公开(公告)号:EP0907478A1

    公开(公告)日:1999-04-14

    申请号:EP97927040.0

    申请日:1997-05-26

    IPC分类号: B29C44 C08G18 C08J9 B29K75 B29K105

    摘要: The invention relates to a process for continuous production of polyurethane slab-stock foam using carbon dioxide (40), dissolved physically under pressure, as the foaming agent. Before mixing the constituents polyhydric alcohol (36) and isocyanate (35), said carbon dioxide (40) is dissolved in the polyhydric alcohol constituent, and air or nitrogen (39) is dissolved in the isocyanate constituent. Both constituents are delivered to a mixing chamber (3) in which there is a pressure 70 to 150 % of the solution pressure of the CO2 in the polyhydric alcohol constituent. The isocyanate constituent is delivered at a pressure of at least 30 bar to the mixing chamber, and by dropping to the mixing chamber pressure is sprayed into said mixing chamber. Air or nitrogen amounting to 1 g per kg of CO2 is dissolved in the isocyanate constituent, and the mixture drops to atmospheric pressure on leaving the mixing chamber.