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KATALIZOER TERKIBI VE BUNUN DOYMAMIS NITTIL'LERIN IMALINE VE OLEFIN'LERIN OKSIDASYONUNA TATBIKI

机译:无催化剂及其未饱和腈的制备和烯烃的氧化

摘要

1355004 Unsaturated aldehydes and nitriles SNAM PROGETTI SpA 25 Jan 1972 [25 Jan 1971] 3529/72 Heading C2C [Also in Division B1] Unsaturated nitrile or unsaturated aldehyde is prepared from olefin by a process wherein a gaseous mixture comprising olefin, molecular oxygen, ammonia (when the desired product is nitrile) and, optionally, steam is contacted with catalyst which comprises, in oxygen-containing compound form, uranium and tellurium and molybdenum in the form of a composition containing, per atom of uranium, from 1 to 8 atoms of tellurium and at least 0À1 but less than 1 atom of molybdenum. The composition also may comprise, in oxygen-containing compound form, at least one "activator" element selected from the elements of Groups Ib, IIa, IIb, IIIa, IIIb (other than uranium), IVa, Va, Vb, VIb (other than molybdenum), VIIb and VIII, for example in an amount of up to 5 atoms of "activator" element(s) per atom of uranium; exemplified "activator" elements are boron, phosphorus, arsenic and antimony. The catalyst also may comprise carrier material, for example silica or titania, which may constitute from 5 to 95 weight per cent of the catalyst. Contacting may be effected at a temperature of from 300‹ to 550‹ C. (when the desired product is nitrile) or from 350‹ to 550‹ C. (when the desired product is aldehyde) and at a pressure which is at or slightly higher than atmospheric pressure; the catalyst may be in the form of a fixed bed or a fluidized bed. Examples prepare acrylonitrile and acrolein.
机译:1355004不饱和醛和腈SNAM PROGETTI SpA 1972年1月25日[1971年1月25日]标题C2C [Also in Division B1]不饱和腈或不饱和醛是由烯烃通过以下方法制得的:其中的气体混合物包括烯烃,分子氧,氨(当所需产物为腈时),并任选使蒸汽与催化剂接触,该催化剂包含以含氧化合物形式存在的铀,碲和钼,其组成形式为每原子铀含1至8个原子碲和至少0-1,但少于1个钼原子。该组合物还可以包含含氧化合物形式的至少一种选自以下的元素的“活化剂”元素:Ib,IIa,IIb,IIIa,IIIb(铀除外),IVa,Va,Vb,VIb(其他) (例如钼),b和,的量,例如每个铀原子最多含5个“活化剂”元素原子;示例性的“活化剂”元素是硼,磷,砷和锑。催化剂还可以包含载体材料,例如二氧化硅或二氧化钛,其可以占催化剂的5至95重量%。接触可以在300℃至550℃的温度下(当所需产物是腈时)或在350℃至550℃的温度下(当所需产物是醛时)并且在等于或稍高的压力下进行。高于大气压力;催化剂可以是固定床或流化床的形式。实例制备丙烯腈和丙烯醛。

著录项

  • 公开/公告号RO61401A

    专利类型

  • 公开/公告日1977-07-15

    原文格式PDF

  • 申请/专利权人

    申请/专利号RO19720069525

  • 发明设计人

    申请日1972-01-25

  • 分类号B01J23/76;

  • 国家 RO

  • 入库时间 2022-08-23 00:45:05

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