Compositions comprising tetrafluoeopropene & carbon dioxide
    5.
    发明申请
    Compositions comprising tetrafluoeopropene & carbon dioxide 有权
    包含四氟丙烯和二氧化碳的组合物

    公开(公告)号:US20060043331A1

    公开(公告)日:2006-03-02

    申请号:US11118833

    申请日:2005-04-29

    IPC分类号: C09K5/04

    摘要: Disclosed are compositions useful in a wide variety of applications, including heat transfer fluids which possess a highly desirable and unexpectedly superior combination of properties, and heat transfer systems and methods based on these fluids. The preferred heat transfer fluid comprises from about 1 to about 40 percent, on a weight basis, of carbon dioxide (CO2) and from about 99 to about 60 percent, on a weight basis, of a compound having the Formula I XCFzR3-z (I), where X is a C2 or a C3 unsaturated, substituted or unsubstituted, alkyl radical, each R is independently Cl, F, Br, I or H, and z is 1 to 3. A preferred compound of Formula I is tetrafluoropropene, particularly 1,1,1,3-tetrafluoropropene and/or 1,1,1,3-tetrafluoropropene.

    摘要翻译: 公开了可用于各种应用的组合物,包括具有非常理想和意想不到的优异组合的传热流体,以及基于这些流体的传热系统和方法。 优选的传热流体包含以重量为基准的约1至约40重量%的二氧化碳(CO 2 H 2)和约99至约60重量%的化合物 具有式I XCF z R 3-z(I),其中X是C 2或C 3, 不饱和的,取代或未取代的烷基,每个R独立地为Cl,F,Br,I或H,z为1至3.优选的式I化合物是四氟丙烯, 四氟丙烯和/或1,1,1,3-四氟丙烯。

    Heat transfer fluid comprising 1,3,3,3-tetrafluoeopropene and carbon dioxide
    7.
    发明申请
    Heat transfer fluid comprising 1,3,3,3-tetrafluoeopropene and carbon dioxide 有权
    包含1,3,3,3-四氟丙烯和二氧化碳的传热流体

    公开(公告)号:US20050241805A1

    公开(公告)日:2005-11-03

    申请号:US10837521

    申请日:2004-04-29

    摘要: Disclosed are compositions useful in a wide variety of applications, including heat transfer fluids which possess a highly desirable and unexpectedly superior combination of properties, and heat transfer systems and methods based on these fluids. The preferred heat transfer fluid comprises from about 1 to about 40 percent, on a weight basis, of carbon dioxide (CO2) and from about 99 to about 60 percent, on a weight basis, of a compound having the Formula I XCFzR3-z (I), where X is a C2 or a C3 unsaturated, substituted or unsubstituted, alkyl radical, each R is independently Cl, F, Br, I or H, and z is 1 to 3. A preferred compound of Formula I is tetrafluoropropene, particularly 1,1,1,3-tetrafluoropropene.

    摘要翻译: 公开了可用于各种应用的组合物,包括具有非常理想和意想不到的优异组合的传热流体,以及基于这些流体的传热系统和方法。 优选的传热流体包含以重量为基准的约1至约40重量%的二氧化碳(CO 2 H 2)和约99至约60重量%的化合物 具有式I XCF z R 3-z(I),其中X是C 2或C 3, 不饱和的,取代或未取代的烷基,每个R独立地为Cl,F,Br,I或H,z为1至3.优选的式I化合物是四氟丙烯, 四氟丙烯。

    Integrated process to coproduce trans-1-chloro-3,3,3-trifluoropropene, trans-1,3,3,3-tetrafluoropropene, and 1,1,1,3,3-pentafluoropropane
    8.
    发明授权
    Integrated process to coproduce trans-1-chloro-3,3,3-trifluoropropene, trans-1,3,3,3-tetrafluoropropene, and 1,1,1,3,3-pentafluoropropane 有权
    共同生产反式-1-氯-3,3,3-三氟丙烯,反式-1,3,3,3-四氟丙烯和1,1,1,3,3-五氟丙烷的综合方法

    公开(公告)号:US09334207B2

    公开(公告)日:2016-05-10

    申请号:US13219831

    申请日:2011-08-29

    摘要: Disclosed is an integrated manufacturing process to co-produce (E)1-chloro-3,3,3-trifluoropropene, (E)1,3,3,3-tetrafluoropropene, and 1,1,1,3,3-pentafluoro-propane starting from a single chlorinated hydrocarbon feed stock, 240fa. The process includes a combined liquid or vapor phase reaction/purification operation which directly produces (E)1-chloro-3,3,3-trifluoropropene (1233zd(E)) from 240fa. In the second liquid phase fluorination reactor 1233zd(E) is contacted with HF in the presence of catalyst to produce 1,1,1,3,3-pentafluoropropane (245fa) with high conversion and selectivity. A third reactor is used for dehydrofluorination of 245fa to produce (E)1,3,3,3-tetrafluoropropene (1234ze(E)) by contacting in the liquid phase with a caustic solution or in the vapor phase using a dehydrofluorination catalyst. This operation may be followed by one or more purification processes to recover the 1234ze(E) product.

    摘要翻译: 公开了共同生产(E)1-氯-3,3,3-三氟丙烯,(E)1,3,3,3-四氟丙烯和1,1,1,3,3-五氟 丙烷从单一氯化烃原料240fa开始。 该方法包括从240fa直接产生(E)1-氯-3,3,3-三氟丙烯(1233zd(E))的组合的液相或汽相反应/纯化操作。 在第二液相氟化反应器1233zd(E)中,在催化剂存在下与HF接触,得到具有高转化率和选择性的1,1,1,3,3-五氟丙烷(245fa)。 第三反应器用于245fa的脱氟化氢以通过使用脱氟化氢催化剂在液相中与苛性碱溶液接触或以蒸气相接触来制备(E)1,3,3,3-四氟丙烯(1234ze(E))。 该操作之后可以进行一个或多个纯化过程以恢复1234ze(E)产物。