Recovery method of pyrolysis product of resin
    1.
    发明授权
    Recovery method of pyrolysis product of resin 有权
    树脂热解产物的回收方法

    公开(公告)号:US08304573B2

    公开(公告)日:2012-11-06

    申请号:US12529725

    申请日:2008-03-07

    摘要: A method of recovering pyrolysis products of resin of the present invention includes cooling gaseous pyrolysis products generated from pyrolysis of the resin in a pyrolysis tank to recover the resin as liquid pyrolysis products. The method includes the following steps (1) to (4): (1) continuously feeding fluidization gas, heated solid particles, and a resin into the pyrolysis tank to fluidize the solid particles and the resin by the fluidization gas; (2) continuously feeding the resin into the pyrolysis tank from a position which is ½ or less of the height of a solid particle layer in the pyrolysis tank in a stationary state; (3) continuously discharging the solid particles from a position lower than the height of a feeding position of the resin; and (4) heating the discharged solid particles in a heating furnace and then feeding the heated solid particles into the pyrolysis tank.

    摘要翻译: 回收本发明树脂热解产物的方法包括冷却由热解槽中的树脂热分解产生的气态热解产物,以回收作为液体热解产物的树脂。 该方法包括以下步骤(1)至(4):(1)将流化气体,加热的固体颗粒和树脂连续供入热解槽中,以使流化气体使固体颗粒和树脂流态化; (2)从处于静止状态的热解槽中的固体颗粒层的高度的1/2以下的位置将树脂连续进料到热解槽中; (3)从低于树脂供给位置的高度的位置连续排出固体颗粒; 和(4)在加热炉中加热排出的固体颗粒,然后将加热的固体颗粒进料到热解槽中。

    Process for producing polyorganosiloxane latex
    2.
    发明授权
    Process for producing polyorganosiloxane latex 有权
    生产聚有机硅氧烷胶乳的方法

    公开(公告)号:US06559224B1

    公开(公告)日:2003-05-06

    申请号:US09465271

    申请日:1999-12-17

    IPC分类号: C08J303

    摘要: In order to easily and effectively polymerize an organosiloxane and produce a polyorganosiloxane latex from which the organosiloxane monomer does not emerge and which has a weight-average diameter controlled to under 0.4 &mgr;m, a paste is polymerized which contains at least a cyclic organosiloxane, a surface active agent, an initiator, and water, and which is an emulsified dispersion of the cyclic organosiloxane, in which the water content is in a proportion of 1 to 66 parts by weight with respect to 100 parts by weight of the cyclic organosiloxane. A latex obtained by diluting the thus-obtained polymerized paste has excellent liquid stability. The above paste, which is an emulsified dispersion of the cyclic organosiloxane, can be produced by mixing the organosiloxane, the surface active agent, the initiator, and the water together in an emulsifying and dispersing machine, and dispersing therein.

    摘要翻译: 为了容易且有效地聚合有机硅氧烷并制备聚有机硅氧烷胶乳,有机硅氧烷单体不会从其中出现,并且其重均直径控制在0.4μm以下,聚合至少包含环状有机硅氧烷的表面,表面 活性剂,引发剂和水,它是环状有机硅氧烷的乳化分散体,其中水含量相对于100重量份的环状有机硅氧烷为1〜66重量份。 通过稀释由此获得的聚合糊获得的胶乳具有优异的液体稳定性。 作为环状有机硅氧烷的乳化分散液的上述糊料可以通过在乳化分散机中将有机硅氧烷,表面活性剂,引发剂和水一起混合并分散而制造。

    RECOVERY METHOD OF PYROLYSIS PRODUCT OF RESIN
    3.
    发明申请
    RECOVERY METHOD OF PYROLYSIS PRODUCT OF RESIN 有权
    树脂热解产物的回收方法

    公开(公告)号:US20100121097A1

    公开(公告)日:2010-05-13

    申请号:US12529725

    申请日:2008-03-07

    IPC分类号: C07C67/00

    摘要: A method of recovering pyrolysis products of resin of the present invention includes cooling gaseous pyrolysis products generated from pyrolysis of the resin in a pyrolysis tank to recover the resin as liquid pyrolysis products. The method includes the following steps (1) to (4): (1) continuously feeding fluidization gas, heated solid particles, and a resin into the pyrolysis tank to fluidize the solid particles and the resin by the fluidization gas; (2) continuously feeding the resin into the pyrolysis tank from a position which is ½ or less of the height of a solid particle layer in the pyrolysis tank in a stationary state; (3) continuously discharging the solid particles from a position lower than the height of a feeding position of the resin; and (4) heating the discharged solid particles in a heating furnace and then feeding the heated solid particles into the pyrolysis tank.

    摘要翻译: 回收本发明树脂热解产物的方法包括冷却由热解槽中的树脂热分解产生的气态热解产物,以回收作为液体热解产物的树脂。 该方法包括以下步骤(1)至(4):(1)将流化气体,加热的固体颗粒和树脂连续供入热解槽中,以使流化气体使固体颗粒和树脂流态化; (2)从处于静止状态的热解槽中的固体颗粒层的高度的1/2以下的位置将树脂连续进料到热解槽中; (3)从低于树脂供给位置的高度的位置连续排出固体颗粒; 和(4)在加热炉中加热排出的固体颗粒,然后将加热的固体颗粒进料到热解槽中。