会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 57. 发明申请
    • Process and apparatus for catalytic distillations
    • US20040210090A1
    • 2004-10-21
    • US10839398
    • 2004-05-05
    • CATALYTIC DISTILLATION TECHNOLOGIES
    • Willibrord A. GrotenMario J. Maraschino
    • C07C321/02C07C005/25
    • B01D3/141B01D3/009C07C2/06C07C2/66C07C5/03C07C5/10C07C5/23C07C5/2506C07C5/27C07C41/06C07C41/42C07C319/18Y02P20/127C07C43/046
    • A process for reacting a first component with itself or a second component to produce a third component in which a first material comprising a first component or said first component and a second component is fed to divided wall column having a catalytic distillation structure in at least one of the separate vertical sections of the divided wall column where concurrently: (1) a first component alone or with a second component is contacted with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the first component with itself or with the second component to form a product and (2) a first mixture comprising the first component and the product or the first component, the second component and the product; and withdrawing the product from the distillation column reactor; while within the column concurrently with the catalytic reaction and fractionation a second mixture is fractionated, which contains the first component and the product or first and second components (if a second component is present) and the product in a parallel and separate distillation non reaction zone to fractionate the product and withdrawing the product from said distillation non reaction zone. For example, tertiary amyl methyl ether may be prepared by reacting methanol with isoamylene in a C5 stream utilizing a distillation column reactor wherein the distillation column reactor comprises one side of a divided wall column. On one side the product, tertiary amyl methyl ether, is separated from the unreacted methanol and C5's and on the other side the remaining isoamylenes are reacted with methanol and a separation of the tertiary amyl methyl ether and C5's from the methanol/C5 azeotrope is effected.
    • 58. 发明申请
    • Process and apparatus for catalytic distillations
    • US20040204614A1
    • 2004-10-14
    • US10839405
    • 2004-05-05
    • CATALYTIC DISTILLATION TECHNOLOGIES
    • Willibrord A. GrotenMario J. Maraschino
    • C07C319/04C07C319/02C07C041/06
    • B01D3/141B01D3/009C07C2/06C07C2/66C07C5/03C07C5/10C07C5/23C07C5/2506C07C5/27C07C41/06C07C41/42C07C319/18Y02P20/127C07C43/046
    • A process for reacting a first component with itself or a second component to produce a third component in which a first material comprising a first component or said first component and a second component is fed to divided wall column having a catalytic distillation structure in at least one of the separate vertical sections of the divided wall column where concurrently: (1) a first component alone or with a second component is contacted with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the first component with itself or with the second component to form a product and (2) a first mixture comprising the first component and the product or the first component, the second component and the product; and withdrawing the product from the distillation column reactor; while within the column concurrently with the catalytic reaction and fractionation a second mixture is fractionated, which contains the first component and the product or first and second components (if a second component is present) and the product in a parallel and separate distillation non reaction zone to fractionate the product and withdrawing the product from said distillation non reaction zone. For example, tertiary amyl methyl ether may be prepared by reacting methanol with isoamylene in a C5 stream utilizing a distillation column reactor wherein the distillation column reactor comprises one side of a divided wall column. On one side the product, tertiary amyl methyl ether, is separated from the unreacted methanol and C5's and on the other side the remaining isoamylenes are reacted with methanol and a separation of the tertiary amyl methyl ether and C5's from the methanol/C5 azeotrope is effected.
    • 60. 发明授权
    • Process for preparing highly pure raffinate II and Methyl tert-butyl ether
    • 制备高纯度萃余液II和甲基叔丁基醚的方法
    • US06657090B2
    • 2003-12-02
    • US09981985
    • 2001-10-19
    • Armin RixGerda GrundWilfried Bueschken
    • Armin RixGerda GrundWilfried Bueschken
    • C07C4109
    • B01D3/009C07C7/14891C07C11/09C07C41/06C07C41/42C07C2531/08C10L1/023Y02P20/127C07C43/046
    • The present invention provides a process, which includes: contacting at least one C4-hydrocarbon stream which includes isobutene with methanol over at least one acid catalyst and preparing methyl tert-butyl ether (MTBE) and a substantially isobutene-free C4-hydrocarbon mixture; wherein in a first stage in one or more first reactors, the isobutene reacts with the methanol over an acid catalyst to form an equilibrium mixture which includes MTBE, remaining isobutene and methanol; the equilibrium mixture is fed to a second stage which includes a reactive distillation column; and in the reactive distillation column, the remaining isobutene reacts with methanol over an acid ion exchange resin to form MTBE; wherein the reactive distillation column is operated at a pressure ranging from 3 to 15 bar abs., a reaction zone temperature ranging from 55° C. to 75° C., and a reflux ratio of less than 1. The present invention also provides a method of making gasoline, which includes the above process and contacting the MTBE with a fuel.
    • 本发明提供了一种方法,其包括:使至少一种包含异丁烯的C 4烃流与甲醇在至少一种酸催化剂上接触并制备甲基叔丁基醚(MTBE)和基本上不含异丁烯的C 4烃混合物; 其中在一个或多个第一反应器中的第一阶段中,异丁烯通过酸催化剂与甲醇反应形成包括MTBE,剩余的异丁烯和甲醇的平衡混合物;将平衡混合物进料到第二阶段,该第二阶段包括反应性蒸馏塔 ; 在反应蒸馏塔中,剩余的异丁烯通过酸离子交换树脂与甲醇反应以形成MTBE;其中反应蒸馏塔在3至15巴绝对压力的范围内操作,反应区温度为55℃ 至75℃,回流比小于1.本发明还提供一种制备汽油的方法,其包括上述方法并使MTBE与燃料接触。