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    • 6. 发明授权
    • Olefin oligomerization
    • 烯烃低聚
    • US07994376B2
    • 2011-08-09
    • US12480384
    • 2009-06-08
    • Brooke L. SmallBruce E. Kreischer
    • Brooke L. SmallBruce E. Kreischer
    • C07C2/30
    • C07C2/32C07C2531/28C07C2531/30C07C11/02
    • Provided is a method of oligomerizing alpha olefins. In an embodiment, an oligomerization catalyst system is contacted in at least one continuous reactor with a feed comprising olefins; an effluent comprising product olefins having at least four carbon atoms is withdrawn from the reactor; the oligomerization catalyst system comprises iron or cobalt, or combinations thereof; and the single pass conversion of ethylene is at least about 40 weight percent among product olefins having at least four carbon atoms. In another embodiment, the single pass conversion of ethylene comprises at least about 65 weight percent among product olefins having at least four carbon atoms. In another embodiment, product olefins of the effluent having twelve carbon atoms comprise at least about 95 weight percent 1-dodecene. In another embodiment, product olefins comprise at least about 80 weight percent linear 1-alkenes. In another embodiment, product olefins comprise at least about 20 weight percent alpha olefins having from about 8 to about 20 carbon atoms. In another embodiment, the oligomerization catalyst system provided comprises a selective 1-hexene (S1H) catalyst.
    • 提供了一种使α-烯烃低聚的方法。 在一个实施方案中,低聚催化剂体系在至少一个连续反应器中与包含烯烃的进料接触; 含有至少四个碳原子的产物烯烃的流出物从反应器中排出; 所述低聚催化剂体系包含铁或钴,或其组合; 并且在具有至少四个碳原子的产物烯烃中乙烯的单程转化率至少为约40重量%。 在另一个实施方案中,乙烯的单程转化在具有至少四个碳原子的产物烯烃中包含至少约65重量%。 在另一个实施方案中,具有十二个碳原子的流出物的产物烯烃包含至少约95重量%的1-十二碳烯。 在另一个实施方案中,产物烯烃包含至少约80重量%的直链1-烯烃。 在另一个实施方案中,产物烯烃包含至少约20重量%的具有约8至约20个碳原子的α-烯烃。 在另一个实施方案中,提供的低聚催化剂体系包括选择性1-己烯(S1H)催化剂。
    • 7. 发明申请
    • Olefin Oligomerization
    • 烯烃低聚
    • US20090270567A1
    • 2009-10-29
    • US12480384
    • 2009-06-08
    • Brooke L. SmallBruce E. Kreischer
    • Brooke L. SmallBruce E. Kreischer
    • C08F2/01C08F4/42C08F4/52
    • C07C2/32C07C2531/28C07C2531/30C07C11/02
    • Provided is a method of oligomerizing alpha olefins. In an embodiment, an oligomerization catalyst system is contacted in at least one continuous reactor with a feed comprising olefins; an effluent comprising product olefins having at least four carbon atoms is withdrawn from the reactor; the oligomerization catalyst system comprises iron or cobalt, or combinations thereof; and the single pass conversion of ethylene is at least about 40 weight percent among product olefins having at least four carbon atoms. In another embodiment, the single pass conversion of ethylene comprises at least about 65 weight percent among product olefins having at least four carbon atoms. In another embodiment, product olefins of the effluent having twelve carbon atoms comprise at least about 95 weight percent 1-dodecene. In another embodiment, product olefins comprise at least about 80 weight percent linear 1-alkenes. In another embodiment, product olefins comprise at least about 20 weight percent alpha olefins having from about 8 to about 20 carbon atoms. In another embodiment, the oligomerization catalyst system provided comprises a selective 1-hexene (S1H) catalyst.
    • 提供了一种使α-烯烃低聚的方法。 在一个实施方案中,低聚催化剂体系在至少一个连续反应器中与包含烯烃的进料接触; 含有至少四个碳原子的产物烯烃的流出物从反应器中排出; 所述低聚催化剂体系包含铁或钴,或其组合; 并且在具有至少四个碳原子的产物烯烃中乙烯的单程转化率至少为约40重量%。 在另一个实施方案中,乙烯的单程转化在具有至少四个碳原子的产物烯烃中包含至少约65重量%。 在另一个实施方案中,具有十二个碳原子的流出物的产物烯烃包含至少约95重量%的1-十二碳烯。 在另一个实施方案中,产物烯烃包含至少约80重量%的直链1-烯烃。 在另一个实施方案中,产物烯烃包含至少约20重量%的具有约8至约20个碳原子的α-烯烃。 在另一个实施方案中,提供的低聚催化剂体系包括选择性1-己烯(S1H)催化剂。