首页> 外国专利> Production of acrolein, useful as intermediate for glutardialdehyde, methionine, folic acid and acrylic acid, by catalytic oxidation of propene uses 2 consecutive reactors operating outside explosion range

Production of acrolein, useful as intermediate for glutardialdehyde, methionine, folic acid and acrylic acid, by catalytic oxidation of propene uses 2 consecutive reactors operating outside explosion range

机译:通过丙烯的催化氧化生产丙烯醛(用作戊二醛,蛋氨酸,叶酸和丙烯酸的中间体),使用了两个在爆炸范围之外运行的连续反应器

摘要

A mixture containing propene and oxygen (O2) is passed at elevated temperature through: (i) a zone containing a first catalyst in the solid aggregate state to oxidize part of the propene to acrolein at a propene/O2 molar ratio of over 1 and (ii) other zone(s) with solid catalyst, with addition of O2, so that = 90 mole-% of the propene reacts with - 80 mole-% selectivity to acrolein. In the production of acrolein by gas phase partial oxidation of propene with oxygen (O2) over a heterogeneous catalyst in the solid aggregate state: (i) a mixture containing propene and O2 in over 1:1 molar ratio is passed at elevated temperature through a first reaction zone containing a first catalyst in the solid aggregate state to oxidize part of the propene to acrolein, then (ii) the reaction mixture is passed at elevated temperature through other reaction zone(s) with a solid catalyst charge, with addition of (gas containing) O2 in at least one of the later zones to increase the O2/propene molar ratio, so that = 90 mole-% of the propene fed to zone I reacts with - 80 mole-% selectivity to acrolein. Independent claims are also included for (a) the production of acrylic acid from propene, including this process; (b) apparatus for the gas phase oxidation of propene to acrolein; (c) apparatus for the gas phase oxidation of propene to acrolein and then of acrolein to acrylic acid.
机译:含有丙烯和氧气(O2)的混合物在高温下通过:(i)含有固态聚集态第一催化剂的区域,以丙烯/ O2摩尔比超过1的方式将部分丙烯氧化为丙烯醛;和ii)添加了O 2的带有固体催化剂的其他区域,使得≥90摩尔%的丙烯以约80摩尔%的选择性与丙烯醛反应。在固态聚集体非均相催化剂上用氧气(O2)气相部分氧化丙烯进行丙烯醛生产中:(i)含丙烯和O2摩尔比超过1:1的混合物在高温下通过包含固态聚集态的第一催化剂的第一反应区,以将部分丙烯氧化为丙烯醛,然后(ii)使反应混合物在高温下通过带有固体催化剂进料的其他反应区,并添加(在至少一个随后的区域中添加氧气以增加O2 /丙烯的摩尔比,从而使进给到区域I的丙烯中的== 90摩尔%以上对丙烯醛的选择性为80摩尔%。还包括以下方面的独立权利要求:(a)由丙烯生产丙烯酸,包括该方法; (b)将丙烯气相氧化为丙烯醛的设备; (c)将丙烯气相氧化成丙烯醛,然后将丙烯醛气相氧化成丙烯酸的设备。

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