Catalyst comprising a zeolite Y globally non-dealuminated and containing boron and/or silicon
    54.
    发明授权
    Catalyst comprising a zeolite Y globally non-dealuminated and containing boron and/or silicon 有权
    催化剂包含全部非脱铝并含有硼和/或硅的沸石Y

    公开(公告)号:US06719895B2

    公开(公告)日:2004-04-13

    申请号:US09965804

    申请日:2001-10-01

    IPC分类号: C10G4716

    CPC分类号: C10G47/20 B01J29/166

    摘要: The present invention relates to a hydrocracking process including contacting a hydrocarbon feed with a catalyst which is carried out at a pressure of at least 2 MPa, a temperature of at least 230° C., using a quantity of hydrogen of at least 100 Nl hydrogen/l of feed and with an hourly space velocity of 0.1-10 h−1. The catalyst includes 0.1-99.7% by weight of at least one alumina matrix; 0.1-80% by weight of at least one globally non dealuminated Y zeolite with a lattice parameter of more than 2.438 nm, a global SiO2/Al2O3 mole ratio of less than 8, and a framework SiO2/Al2O3 mole ratio of less than 21 and more than the global SiO2/Al2O3 mole ratio; 0.1-30% by weight of at least one group VIII metal and/or 1-40% by weight of at least one group VIB metal (% oxide); 0.1-20% by weight of at least one promoter element selected from the group formed by boron and silicon (% oxide); 0-20% by weight of at least one group VIIA element; 0-20% by weight of phosphorous (% oxide); and 0.1-20% by weight of at least one group VIIB element.

    摘要翻译: 本发明涉及一种加氢裂化方法,包括使烃进料与催化剂接触,所述催化剂在至少2MPa的压力,至少230℃的温度下使用至少100N氢气的氢气进行 / l的饲料,每小时空速为0.1-10小时-1。 催化剂包含0.1-99.7重量%的至少一个氧化铝基质; 0.1-80重量%的至少一种全部非脱铝Y沸石,其晶格参数大于2.438nm,全体SiO 2 / Al 2 O 3摩尔比 小于8,并且SiO 2 / Al 2 O 3的骨架比小于21且大于全局SiO 2 / Al 2 O 3摩尔比; 0.1-30重量%的至少一种VIII族金属和/或1-40重量% 至少一种VIB族金属(%氧化物); 0.1-20%重量的选自硼和硅(氧化物%)的至少一种助催化剂元素; 0-20%重量的至少一种VIIA族元素 ; 0-20重量%的磷(%氧化物); 和0.1-20重量%的至少一种VIIB族元素。

    Process for purifying naphthalene by selective hydrotreatment followed by separation
    56.
    发明授权
    Process for purifying naphthalene by selective hydrotreatment followed by separation 失效
    通过选择性加氢处理分离纯化萘的方法

    公开(公告)号:US06217750B1

    公开(公告)日:2001-04-17

    申请号:US09008582

    申请日:1998-01-16

    IPC分类号: C10G4560

    摘要: The invention concerns a process for purifying naphthalene. The process comprises selective hydrotreatment corresponding to hydrodesulphuration and/or hydrodenitrogenation and/or hydrodehydroxylation and/or hydrogenation of olefins while limiting naphthalene hydrogenation. The catalyst used comprises a matrix, at least one group VIII metal, at least one group VI metal and optionally phosphorous. It has a specific surface area of at most 220 m2/g, a pore volume of 0.35-0.7 ml/g and an average pore diameter of over 10 nm. The process is carried out at 150-325° C. at a pressure of 0.1-0.9 MPa, with an HSV of 0.05-10 h−1, and a H2/naphthalene ratio of 0.1-1.3 mole/mole. The effluent, freed of H2S, NH3 and water, undergoes a naphthalene separation process by distillation or, as is preferable, by crystallisation. Further, recycling the separated tetralin to the hydrotreatment step can substantially increase the naphthalene yield. In this case, the tetralin/naphthalene ratio at the reactor inlet is in the range 0.005 to 0.08.

    摘要翻译: 本发明涉及萘的纯化方法。 该方法包括对应于加氢脱硫和/或加氢脱氮和/或烯烃的加氢脱羟和/或氢化的选择性加氢处理,同时限制萘氢化。 所使用的催化剂包括基质,至少一种VIII族金属,至少一种VI族金属和任选的磷。 比表面积为220m2 / g以下,孔体积为0.35〜0.7ml / g,平均孔径为10nm以上。 该方法在150-325℃,0.1-0.9MPa的压力下进行,HSV为0.05-10h -1,H 2 /萘比为0.1-1.3摩尔/摩尔。 除去H 2 S,NH 3和水的流出物通过蒸馏或优选通过结晶进行萘分离。 此外,将分离的四氢化萘再循环到加氢处理步骤可以显着提高萘产率。 在这种情况下,反应器入口处的四氢化萘/萘比在0.005至0.08的范围内。