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SOC FRANCAISE DES PROD POUR CATALYSE HYDROCARBON CONVERSION CATALYSTS THEIR PREPARATION AND US

机译:SOC FRANCAISE DES PROD POUR催化剂催化烃转化催化剂及其制备和应用

摘要

1502625 Aromatization SOC FRANCAISE DES PRODUITS POUR CATALYSE 8 Oct 1975 [11 Oct 1974] 41261/75 Heading C5E [Also in Division B1] Hydrocarbon feeds are converted using a catalyst comprising (i) a carrier; (ii) platinum; (iii) at least one metal selected from iridium, rhodium and ruthenium; (iv) coba (v) at least one metal selected from copper, manganese, silver or gold; and, (vi) 0À1-10% wt. (based on the carrier) of a halogen in combined form. The catalyst is particularly suited to the production of aromatic hydrocarbons, e.g. benzene, toluene or xylenes, from gasolines, e.g. steam cracked or reformed gasolines from naphthenic hydrocarbons by dehydrogenation; or from paraffins by dehydrocyclization. For example, an unsaturated charge containing diolefins and mono-olefins may be firstly treated to a hydrogenation step to convert diolefins to monolefins and alkenylaromatics to alkyl aromatics; then the charge may be treated in a hydrogenationhydrodesulphurization step to convert monolefins to paraffins and free the charge from sulphur; and finally, the charge may be treated in the presence of hydrogen with the present catalyst to form aromatics, e.g. at 300-600‹ C., a pressure of 1-60 kg./cm.SP2/SP and a LHSV of 0À1-10. This step may be effected in a plurality of stages, for example a first stage at 400-600‹ C. using a catalyst wherein the catalyst is neutral and of a specific surface lower than 100 m.SP2/SP/g. and a second stage wherein the catalyst has a relatively high surface area and is acidic. The catalyst may be in fixed bed, moving bed or fluidized form. The examples describe treatment of a feed containing pentanes, hexanes, heptanes, cyclopentane, methylcyclopentane, cyclohexane, C 7 and C 8 naphthenes and some benzene and toluene to give a product of increased benzene and toluene content.
机译:1502625芳构化SOC芳烃DES产物倾倒催化剂1975年10月8日[1974年10月11日]标题C5E [也在B1分部中]使用以下催化剂转化烃类进料:(i)载体; (ii)铂; (iii)至少一种选自铱,铑和钌的金属; (iv)钴; (v)至少一种选自铜,锰,银或金的金属; (vi)0-1-10%wt。 (基于载体)结合形式的卤素。该催化剂特别适合于生产芳族烃,例如芳烃。汽油中的苯,甲苯或二甲苯通过脱氢从环烷烃中蒸汽裂解或重整汽油;或通过脱氢环化从石蜡中提取。例如,可以首先将包含二烯烃和单烯烃的不饱和进料进行氢化步骤,以将二烯烃转化为单烯烃,并将烯基芳族化合物转化为烷基芳族化合物;然后可以在加氢加氢脱硫步骤中处理进料,以将单烯烃转化为链烷烃并从硫中释放出进料;最后,可以在氢气存在下用本发明的催化剂处理进料,以形成芳族化合物,例如芳族化合物。在300-600℃下,压力为1-60 kg./cm.2,LHSV为0‑1-10。该步骤可以在多个阶段中进行,例如使用催化剂在400-600℃下进行的第一阶段,其中该催化剂是中性的并且比表面积小于100m。 2 / G。第二阶段,其中催化剂具有相对较高的表面积并且是酸性的。催化剂可以是固定床,移动床或流化形式。实施例描述了处理含有戊烷,己烷,庚烷,环戊烷,甲基环戊烷,环己烷,C 7和C 8环烷以及一些苯和甲苯的进料,得到苯和甲苯含量增加的产物。

著录项

  • 公开/公告号GB1502625A

    专利类型

  • 公开/公告日1978-03-01

    原文格式PDF

  • 申请/专利权人

    申请/专利号GB19750041261

  • 发明设计人

    申请日1975-10-08

  • 分类号B01J23/74;

  • 国家 GB

  • 入库时间 2022-08-22 21:39:26

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