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6,6-Dibenzyl-fulven | 99997-35-0

中文名称
——
中文别名
——
英文名称
6,6-Dibenzyl-fulven
英文别名
6,6-Dibenzylfulvene;(2-cyclopenta-2,4-dien-1-ylidene-3-phenylpropyl)benzene
6,6-Dibenzyl-fulven化学式
CAS
99997-35-0
化学式
C20H18
mdl
——
分子量
258.363
InChiKey
SFVBPFFEXPAETQ-UHFFFAOYSA-N
BEILSTEIN
——
EINECS
——
  • 物化性质
  • 计算性质
  • ADMET
  • 安全信息
  • SDS
  • 制备方法与用途
  • 上下游信息
  • 反应信息
  • 文献信息
  • 表征谱图
  • 同类化合物
  • 相关功能分类
  • 相关结构分类

计算性质

  • 辛醇/水分配系数(LogP):
    5.9
  • 重原子数:
    20
  • 可旋转键数:
    4
  • 环数:
    3.0
  • sp3杂化的碳原子比例:
    0.1
  • 拓扑面积:
    0
  • 氢给体数:
    0
  • 氢受体数:
    0

反应信息

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文献信息

  • Crosslinked metallocene compound for olefin polymerization and method of polymerizing olefin with the same
    申请人:Tohi Yasushi
    公开号:US20060161013A1
    公开(公告)日:2006-07-20
    The bridged metallocene compound or the olefin polymerization catalyst which comprises the compound, enables high polymerization activity in polymerizing one or more monomers selected from ethylene and α-olefins. The bridged metallocene compound contains specific substituted cyclopentadienyl and fluorenyl groups which are linked via carbon or silicon atoms. In the method for the preparation of polyolefins, one or more monomers, preferably ethylene as an essential monomer, selected from ethylene and α-olefins are copolymerized in the presence of the olefin polymerization catalyst comprising the bridged metallocene compound, so that an ethylene based polymer with an ethylene content of more than 50 mol % is obtained.
    桥式属茂化合物或烯烃聚合催化剂包括该化合物,能够在聚合乙烯和α-烯烃中选择一个或多个单体的聚合中实现高聚合活性。桥式属茂化合物包含特定的取代环戊二烯基和基团,它们通过碳或原子连接。在制备聚烯烃的方法中,通过在桥式属茂化合物的存在下共聚合一个或多个单体,优选乙烯作为必要单体,选择乙烯和α-烯烃中的一个或多个单体,从而获得乙烯为基础的聚合物,其乙烯含量超过50摩尔%。
  • Catalyst for olefin polymerization, method for producing olefin polymer, method for producing propylene-based copolymer, propylene polymer, propylene-based polymer composition, and use of those
    申请人:Tohi Yasushi
    公开号:US20080220193A1
    公开(公告)日:2008-09-11
    A catalyst for olefin polymerization, comprising: (A-1) a bridged metallocene compound represented by the following Formula [1-1], and (b) at least one compound selected from: (b-1) an organoaluminum oxy compound, (b-2) a compound which forms an ion pair, and (b-3) an organoaluminum compound: wherein in Formula [1-1], R 1 , R 2 , R 3 , R 4 , R 5 , R 8 , R 9 , and R 12 are each selected from a hydrogen, a hydrocarbon group and a silicon-containing group; the four groups of R 6 , R 7 , R 10 , and R 11 are not hydrogen atoms, and are each selected from a hydrocarbon group or a silicon-containing group; R 13 and R 14 are each a hydrocarbon group or the like, excluding a hydrogen atom and a methyl group; M is Ti, Zr or the like; Y is carbon or the like; Q is a halogen or the like; and j is an integer from 1
    催化剂,用于烯烃聚合,包括:(A-1)桥联属茂化合物,其表示为以下式[1-1];以及(b)至少一种化合物,选自:(b-1)有机铝氧化合物,(b-2)形成离子对的化合物,以及(b-3)有机铝化合物。在式[1-1]中,R1、R2、R3、R4、R5、R8、R9和R12各自选自氢、烃基和含基团;R6、R7、R10和R11的四个基团不是氢原子,各自选自烃基或含基团;R13和R14各自是烃基或类似的基团,不包括氢原子和甲基基团;M是Ti、Zr或类似的属;Y是碳或类似的元素;Q是卤素或类似的元素;j是整数1或更大。
  • PROCESS FOR PREPARING OLEFIN POLYMER USING MIXED CATALYST
    申请人:Yukita Takashi
    公开号:US20110077369A1
    公开(公告)日:2011-03-31
    [Problem] To efficiently obtain an α-olefin polymer having a high melting point and a high molecular weight. [Solution to Problem] The process for preparing an olefin polymer of the present invention is a process for preparing an olefin polymer, comprising polymerizing at least one monomer selected from α-olefins of 2 or more carbon atoms, wherein the polymerization is carried out at a temperature of not lower than 40° C. in the presence of a catalyst comprising a transition metal compound component (A) which comprises two or more kinds of transition metal compounds (a) represented by the following formula [A1] and an organometallic compound component (B) which comprises an organometallic compound (b), propylene is contained in the monomer, and the olefin polymer is an olefin polymer whose weight-average molecular weight (Mw) and number-average molecular weight (Mn), as determined by gel permeation chromatography (GPC), satisfy the relationship of 1≦(Mw/Mn)≦3, and which has a melting point (Tm), as determined by DSC, of not lower than 150° C. and an intrinsic viscosity ([η]) of not less than 1.5 dl/g.
    [问题] 高效地获得具有高熔点和高分子量的α-烯烃聚合物。 [解决方案] 本发明的烯烃聚合物制备过程是一种制备烯烃聚合物的过程,包括聚合选择自2个或更多碳原子的α-烯烃中的至少一个单体,其中在催化剂的存在下在不低于40℃的温度下进行聚合反应,所述催化剂包括由以下式[A1]所表示的两种或两种以上的过渡属化合物(a)组成的过渡属化合物组分(A)和包括有机属化合物(b)的有机属化合物组分(B),单体中含有丙烯,并且通过凝胶渗透色谱法(GPC)确定的重均分子量(Mw)和数均分子量(Mn)满足1≦(Mw/Mn)≦3,其熔点(Tm)不低于150℃,固有粘度([η])不小于1.5 dl/g的烯烃聚合物。
  • Process for preparing olefin polymer using mixed catalyst
    申请人:Mitsui Chemicals, Inc.
    公开号:US08293856B2
    公开(公告)日:2012-10-23
    [Problem] To efficiently obtain an α-olefin polymer having a high melting point and a high molecular weight. [Solution to Problem] The process for preparing an olefin polymer of the present invention is a process for preparing an olefin polymer, comprising polymerizing at least one monomer selected from α-olefins of 2 or more carbon atoms, wherein the polymerization is carried out at a temperature of not lower than 40° C. in the presence of a catalyst comprising a transition metal compound component (A) which comprises two or more kinds of transition metal compounds (a) represented by the following formula [A1] and an organometallic compound component (B) which comprises an organometallic compound (b), propylene is contained in the monomer, and the olefin polymer is an olefin polymer whose weight-average molecular weight (Mw) and number-average molecular weight (Mn), as determined by gel permeation chromatography (GPC), satisfy the relationship of 1≦(Mw/Mn)≦3, and which has a melting point (Tm), as determined by DSC, of not lower than 150° C. and an intrinsic viscosity ([η]) of not less than 1.5 dl/g.
    [问题] 高效地获得具有高熔点和高分子量的α-烯烃聚合物。 [解决方案] 本发明的制备烯烃聚合物的过程是一种制备烯烃聚合物的过程,包括聚合选择自2个或更多碳原子的α-烯烃中的至少一个单体,在存在催化剂的情况下,在不低于40℃的温度下进行聚合。所述催化剂包括过渡属化合物组分(A),该组分包括由以下式[A1]表示的两种或两种以上的过渡属化合物(a)以及有机属化合物组分(B),其中包括有机属化合物(b),单体中包含丙烯,并且所述烯烃聚合物的重均分子量(Mw)和数均分子量(Mn),由凝胶渗透色谱法(GPC)确定,满足1≤(Mw/Mn)≤3的关系,其熔点(Tm)由DSC确定,不低于150℃,固有粘度([η])不小于1.5 dl/g。
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