High purity paraffinic solvent compositions
    1.
    发明授权
    High purity paraffinic solvent compositions 失效
    高纯度链烷烃溶剂组合物

    公开(公告)号:US5906727A

    公开(公告)日:1999-05-25

    申请号:US81364

    申请日:1998-05-19

    CPC分类号: C10G45/58

    摘要: Discloses high purity solvent compositions constituted of n-paraffins and isoparaffins, with the isoparaffins containing predominantly methyl branches, and having an isoparaffin:n-paraffin ratio sufficient to provide superior low temperature properties and low viscosities. The solvent compositions are made by a process wherein a waxy, or long chain paraffinic feed, especially a Fischer-Tropsch wax, is reacted over a dual function catalyst to produce hydroisomerization and hydrocracking reactions at 700.degree. F.+ conversion levels ranging from about 20 to 90 wt.% to provide a C.sub.5 -1050.degree. F. crude fraction. The C.sub.5 -1050.degree. F. crude fraction is then topped via atmospheric distillation to produce a low boiling fraction with an upper end point boiling between about 650.degree. F. and 750.degree. F. The low boiling fraction is fractionated and a narrow boiling range solvent obtained therefrom; one which can be further divided into solvent grades of various boiling ranges.

    摘要翻译: 公开了由正链烷烃和异链烷烃构成的高纯度溶剂组合物,其中主要含有甲基支链的异链烷烃,并且具有足以提供优异的低温性能和低粘度的异链烷烃:正链烷烃比率。 溶剂组合物通过以下方法制备,其中蜡状或长链石蜡原料,特别是费 - 托蜡在双功能催化剂上反应,以在700°F下进行加氢异构化和加氢裂化反应。+转化率范围为约20 至90重量%以提供C5-1050°F粗馏分。 然后通过常压蒸馏将C5-1050°F粗馏分顶起来产生沸点高于约650°F至750°F的高沸点馏分。将低沸点馏分分馏,并将窄沸点溶剂 由此获得; 可以进一步分为各种沸程的溶剂等级。

    Hydroisomerization of a predominantly N-paraffin feed to produce high
purity solvent compositions
    2.
    发明授权
    Hydroisomerization of a predominantly N-paraffin feed to produce high purity solvent compositions 失效
    主要是N-链烷烃进料的加氢异构化以产生高纯度溶剂组合物

    公开(公告)号:US5866748A

    公开(公告)日:1999-02-02

    申请号:US636424

    申请日:1996-04-23

    IPC分类号: B01J23/44 C10G45/58 C10G45/62

    CPC分类号: C10G45/58 Y10S208/95

    摘要: A process for the hydroisomerization of a predominantly C.sub.8 -C.sub.20 n-paraffinic feed to produce a high purity C.sub.8 -C.sub.20 paraffinic solvent composition having superior low temperature properties, and low viscosities. The feed is contacted, with hydrogen, over a dual functional catalyst to hydroisomerize and convert the feed to a product comprising a mixture of n-paraffins and isoparaffins, the isoparaffins component of which contains greater than 50 percent of mono-methyl species, with the molar ratio of isoparaffins:n-paraffins ranging from about 0.5:1 to 9:1.

    摘要翻译: 主要C8-C20正链烷烃进料加氢异构化的方法,以产生具有优异的低温性能和低粘度的高纯度C8-C20链烷烃溶剂组合物。 进料与氢气在双官能催化剂上接触,将进料加氢异构化并转化成包含正链烷烃和异链烷烃的混合物的产物,其异链烷烃组分含有大于50%的单甲基物质,其中 异链烷烃的摩尔比:正链烷烃的范围为约0.5:1至9:1。

    High purity paraffinic solvent compositions, and process for their
manufacture
    3.
    发明授权
    High purity paraffinic solvent compositions, and process for their manufacture 失效
    高纯度链烷烃溶剂组合物及其制备方法

    公开(公告)号:US5833839A

    公开(公告)日:1998-11-10

    申请号:US569466

    申请日:1995-12-08

    CPC分类号: C10G45/58

    摘要: Discloses high purity solvent compositions constituted of n-paraffins and isoparaffins, with the isoparaffins containing predominantly methyl branches, and having an isoparaffin:n-paraffin ratio sufficient to provide superior low temperature properties and low viscosities. The solvent compositions are made by a process wherein a waxy, or long chain paraffinic feed, especially a Fischer-Tropsch wax, is reacted over a dual function catalyst to produce hydroisomerization and hydrocracking reactions at 700.degree. F.+ conversion levels ranging from about 20 to 90 wt. % to provide a C.sub.5 -1050.degree. F. crude fraction. The C.sub.5 -1050.degree. F. crude fraction is then topped via atmospheric distillation to produce a low boiling fraction with an upper end point boiling between about 650.degree. F. and 750.degree. F. The low boiling fraction is fractionated and a narrow boiling range solvent obtained therefrom; one which can be further divided into solvent grades of various boiling ranges.

    摘要翻译: 公开了由正链烷烃和异链烷烃构成的高纯度溶剂组合物,其中主要含有甲基支链的异链烷烃,并且具有足以提供优异的低温性能和低粘度的异链烷烃:正链烷烃比率。 溶剂组合物通过以下方法制备,其中蜡状或长链石蜡原料,特别是费 - 托蜡在双功能催化剂上反应,以在700°F下进行加氢异构化和加氢裂化反应。+转化率范围为约20 至90重量% %提供C5-1050°F粗馏分。 然后通过常压蒸馏将C5-1050°F粗馏分顶起来产生沸点高于约650°F至750°F的高沸点馏分。将低沸点馏分分馏,并将窄沸点溶剂 由此获得; 可以进一步分为各种沸程的溶剂等级。