PRODUCTION OF HIGH PURITY BUTENE-1 FROM C4 OLEFINS/PARAFFINS MIXED GAS
    2.
    发明申请
    PRODUCTION OF HIGH PURITY BUTENE-1 FROM C4 OLEFINS/PARAFFINS MIXED GAS 有权
    从C4油脂/ PARAFFINS混合气体生产高纯度BUTENE-1

    公开(公告)号:US20100116639A1

    公开(公告)日:2010-05-13

    申请号:US12593252

    申请日:2008-04-11

    IPC分类号: B01D3/00

    摘要: The present invention relates to a hybrid process comprising an adsorption process and a distillation process for the separation of butene-1 from a C4 hydrocarbon mixture gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. The above hybrid process comprises introducing a gaseous C4 mixture into the adsorption tower loaded with adsorbents which adsorb olefins selectively to discharge C4 paraffins to the outlet of the tower, desorbing C4 olefins selectively adsorbed in the adsorption tower to produce high purity C4 olefins mixture gas in which isobutane and normal butane was removed, and separating the high C4 olefins mixture gas (a mixture of butene-1, trans-2-butene, cis-2-butene, and a trace amount of C4 paraffins) via distillation to obtain high purity butene-1 including a trace amount of isobutane in the top of the distillation tower and obtain a mixture gas including trans-2-butene, cis-2-butene and a trace amount of normal butane in the bottom of the tower.

    摘要翻译: 本发明涉及一种混合方法,其包括吸附过程和用于从包含丁烯-1,反式-2-丁烯,顺式-2-丁烯,正丁烷,异丁烷的C 4烃混合气体中分离丁烯-1的蒸馏方法 等等。上述混合方法包括将气态C 4混合物引入到负载有吸附剂的吸附塔中,所述吸附剂选择性吸附烯烃以将C4链烷烃排出到塔的出口,解吸选择性吸附在吸附塔中的C4烯烃以产生高纯度C4烯烃 除去异丁烷和正丁烷的混合气体,通过蒸馏将高C4烯烃混合气体(丁烯-1,反式-2-丁烯,顺式-2-丁烯和痕量的C4链烷烃的混合物)分离成 在蒸馏塔顶部得到含有痕量异丁烷的高纯度丁烯-1,得到底部的反式-2-丁烯,顺式-2-丁烯和痕量正丁烷的混合气体 他塔。

    Adsorption separation and purification apparatus and process for high
purity isobutane production
    4.
    发明授权
    Adsorption separation and purification apparatus and process for high purity isobutane production 失效
    高纯异丁烷生产吸附分离纯化装置及工艺

    公开(公告)号:US6022398A

    公开(公告)日:2000-02-08

    申请号:US34023

    申请日:1998-03-02

    摘要: A high purity isobutane adsorption separation and purification apparatus is provided including a pressure regulator which regulates the pressure of an isobutane-containing gas; the at least one adsorption bed packed with zeolite 5A and carbon molecular sieve arranged downstream of and operatively associated with the pressure regulator; a flow control valve disposed between the pressure regulator and the at least one adsorption bed; a surge tank operatively associated with and for receiving a purified isobutane product from the at least one adsorption bed; a vacuum pump operatively associated with and for removal of impurities from the at least one adsorption bed; and valves disposed between the pressure regulator and the at least one adsorption bed, between the at least one adsorption bed and the surge tank, and between the at least one adsorption bed and the vacuum pump. An adsorptive separation and isobutane purification process is also provided which may be used with the apparatus of the invention.

    摘要翻译: 提供了一种高纯度异丁烷吸附分离和净化装置,包括调节含异丁烷的气体的压力的压力调节器; 填充有沸石5A的至少一个吸附床和布置在压力调节器的下游并与压力调节器可操作地相关联的碳分子筛; 设置在所述压力调节器和所述至少一个吸附床之间的流量控制阀; 调节罐,其与所述至少一个吸附床可操作地相关联并用于接收纯化的异丁烷产物; 与所述至少一个吸附床可操作地相关联并用于从所述至少一个吸附床去除杂质的真空泵; 以及设置在所述压力调节器和所述至少一个吸附床之间,所述至少一个吸附床和所述缓冲罐之间以及所述至少一个吸附床和所述真空泵之间的阀。 还提供了可与本发明的装置一起使用的吸附分离和异丁烷纯化方法。

    Production of high purity butene-1 from C4 olefins/paraffins mixed gas
    8.
    发明授权
    Production of high purity butene-1 from C4 olefins/paraffins mixed gas 有权
    从C4烯烃/石蜡混合气体生产高纯度丁烯-1

    公开(公告)号:US08431762B2

    公开(公告)日:2013-04-30

    申请号:US12593252

    申请日:2008-04-11

    IPC分类号: C07C7/12

    摘要: The present invention relates to a hybrid process comprising an adsorption process and a distillation process for the separation of butene-1 from a C4 hydrocarbon mixture gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. The above hybrid process comprises introducing a gaseous C4 mixture into the adsorption tower loaded with adsorbents which adsorb olefins selectively to discharge C4 paraffins to the outlet of the tower, desorbing C4 olefins selectively adsorbed in the adsorption tower to produce high purity C4 olefins mixture gas in which isobutane and normal butane was removed, and separating the high C4 olefins mixture gas (a mixture of butene-1, trans-2-butene, cis-2-butene, and a trace amount of C4 paraffins) via distillation to obtain high purity butene-1 including a trace amount of isobutane in the top of the distillation tower and obtain a mixture gas including trans-2-butene, cis-2-butene and a trace amount of normal butane in the bottom of the tower.

    摘要翻译: 本发明涉及一种混合方法,其包括吸附过程和用于从包含丁烯-1,反式-2-丁烯,顺式-2-丁烯,正丁烷,异丁烷的C 4烃混合气体中分离丁烯-1的蒸馏方法 等等。上述混合方法包括将气态C 4混合物引入到负载有吸附剂的吸附塔中,所述吸附剂选择性吸附烯烃以将C4链烷烃排出到塔的出口,解吸选择性吸附在吸附塔中的C4烯烃以产生高纯度C4烯烃 除去异丁烷和正丁烷的混合气体,通过蒸馏将高C4烯烃混合气体(丁烯-1,反式-2-丁烯,顺式-2-丁烯和痕量的C4链烷烃的混合物)分离成 在蒸馏塔顶部得到含有痕量异丁烷的高纯度丁烯-1,得到底部的反式-2-丁烯,顺式-2-丁烯和痕量正丁烷的混合气体 他塔。