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    • 6. 发明授权
    • Candle precoated filter for residual volume filtration
    • 蜡烛预涂过滤器用于残留体积过滤
    • US5384034A
    • 1995-01-24
    • US64168
    • 1993-05-19
    • Hartmut Hetzel
    • Hartmut Hetzel
    • B01D29/50B01D24/46B01D29/11B01D29/46B01D29/62B01D35/16B01D36/02B01D25/22
    • B01D36/02B01D29/114B01D35/16B01D2201/0484
    • A candle type precoated filter for residual volume filtration has a pressure vessel having a cylindrical upper part and a conical base, a plurality of filter elements arranged substantially vertically and including at least one residual filter element and other filter elements formed so that the at least one residual filter element is lengthened toward the base and is longer than the other filter elements and a separating wall which separates the residual filter element in an upper portion of the pressure vessel from the other filter elements so as to be tight against media and to project out in a lower portion of the pressure vessel beyond a length of the other filter element.
    • PCT No.PCT / CH91 / 00196 Sec。 371日期:1993年5月19日 102(e)日期1993年5月19日PCT 1991年9月10日PCT PCT。 出版物WO93 / 04762 日期:1993年3月18日。用于残余体积过滤的蜡烛型预涂过滤器具有压力容器,该压力容器具有圆柱形上部和圆锥形底座,多个过滤元件基本上垂直布置并且包括至少一个剩余过滤元件和其它过滤元件 形成为使得至少一个剩余过滤元件朝向基部延长并且比其它过滤元件长;以及分隔壁,其将压力容器的上部中的残余过滤元件与其它过滤器元件分离,以便 紧靠介质并在压力容器的下部突出超过另一个过滤元件的长度。
    • 8. 发明授权
    • Process for separating polyurethane hydrolyzates into polyether and
diamine
    • 将聚氨酯水解产物分离成聚醚和二胺的方法
    • US4399236A
    • 1983-08-16
    • US299418
    • 1981-09-04
    • Georg NiederdellmannNorbert RoemerJurgen SchenkHartmut HetzelErnst Grigat
    • Georg NiederdellmannNorbert RoemerJurgen SchenkHartmut HetzelErnst Grigat
    • C08G18/00C08G18/82C08J11/00C08J11/10C08J11/04C08G18/48
    • C08J11/10C08J2375/04Y02W30/702
    • The present invention is directed to a process for separating polyurethane hydrolyzates, preferably polyurethane foam hydrolyzates, into substantially amine-free foamable polyethers and diamines, comprising (a) (i) briefly expanding a hot polyurethane hydrolyzate obtained in a continuous screw extruder to normal pressure or in vacuo and, without using readily volatile components (ii) spraying said hydrolyzate directly into a tubular coil evaporator which is heated to 180.degree.-300.degree. C. and at the end of which a pressure of from 0.1 to 20 mbar is applied and (iii) separating a hydrolyzate containing less than 1% by weight of NH.sub.2 in a following cyclone from most of the diamine evaporated and all the solvent used, the diamine being separated from the solvent used in a following distillation column, optionally without any further heat input; (b) precipitating any diamine still present quantitatively in the form of its hydrochloride by introducing excess hydrogen chloride into the hydrolyzate, optionally diluted with inert solvents; and (c) the regenerated polyether obtained after removal by filtration of the precipitated amine salt being freed under reduced pressure from inert solvent and excess hydrogen chloride.
    • 本发明涉及将聚氨酯水解物(优选聚氨酯泡沫水解产物)分离成基本上不含胺的可发泡聚醚和二胺的方法,其包括(a)(i)将在连续螺杆挤出机中获得的热聚氨酯水解产物短暂膨胀至常压 或在真空中,并且不使用易挥发性组分(ii)将所述水解产物直接喷射到加热至180-300℃的管状线圈蒸发器中,并且其末端施加0.1至20mbar的压力, (iii)在以下旋风分离器中从大部分蒸发的二胺和所有使用的溶剂中分离含有小于1重量%的NH 2的水解产物,二胺与随后的蒸馏塔中使用的溶剂分离,任选没有任何进一步的热 输入 (b)通过将过量的氯化氢引入水解产物中,任选地用惰性溶剂稀释,沉淀出以其盐酸盐形式定量存在的任何二胺; 和(c)通过过滤除去沉淀的胺盐后得到的再生聚醚,在惰性溶剂和过量的氯化氢中减压除去。