首页> 外国专利> Preparation of acrolein or acrylic acid involves conducting starting reaction gas mixture having propylene and molecular oxygen reactants and inert molecular nitrogen and propane diluent gasses through fixed catalyst bed

Preparation of acrolein or acrylic acid involves conducting starting reaction gas mixture having propylene and molecular oxygen reactants and inert molecular nitrogen and propane diluent gasses through fixed catalyst bed

机译:丙烯醛或丙烯酸的制备涉及将具有丙烯和分子氧反应物以及惰性分子氮和丙烷稀释剂气体的起始反应气体混合物通过固定的催化剂床

摘要

Acrolein or acrylic acid is prepared by catalyzing partial gas phase oxidation of propene, where a starting reaction gas mixture having propylene and molecular oxygen reactants and inert molecular nitrogen and propane diluent gasses is conducted at elevated temperature through a fixed catalyst bed whose active composition is a multimetal oxide having molybdenum, iron and bismuth. Preparation of acrolein or acrylic acid involves catalyzing partial gas phase oxidation of propene, where a starting reaction gas mixture having propylene and molecular oxygen reactants and the inert molecular nitrogen and propane diluent gasses and having the molecular oxygen and the propylene in a molar oxygen;C 3H 6 ratio of =1 is conducted at elevated temperature through a fixed catalyst bed whose active composition is a multimetal oxide having molybdenum, iron and bismuth based on its total volume of 6-9 vol.% propylene, 8-18 vol.% molecular oxygen. 6-30 vol.% propane and 32-72 vol.% molecular nitrogen. The molar ratio V 1 of propane in starting reaction gas mixture to propylene in starting reaction gas mixture is 1-4. The molar V 2 of molecular nitrogen present in starting reaction gas mixture to molecular oxygen in starting reaction the mixture is 2-6, and the molar ratio of the molecular oxygen in starting reaction gas mixture to propylene in starting reaction mixture is 1.3-2.4.
机译:通过催化丙烯的部分气相氧化来制备丙烯醛或丙烯酸,其中具有丙烯和分子氧反应物以及惰性分子氮和丙烷稀释剂气体的起始反应气体混合物在高温下通过固定的催化剂床进行,该催化剂床的活性成分为具有钼,铁和铋的多金属氧化物。丙烯醛或丙烯酸的制备涉及催化丙烯的部分气相氧化,其中起始反应气体混合物具有丙烯和分子氧反应物以及惰性分子氮和丙烷稀释剂气体,且分子氧和丙烯的摩尔氧含量; C > 1的3H 6比在升高的温度下通过固定的催化剂床进行,该催化剂床的活性成分是基于钼的总体积为6-9%(体积),丙烯的8-18%(体积)的钼,铁和铋的多金属氧化物。分子氧。 6-30%(体积)的丙烷和32-72%(体积)的分子氮。起始反应气体混合物中丙烷与起始反应气体混合物中丙烯的摩尔比V 1为1-4。存在于起始反应气体混合物中的分子氮与起始混合物中的分子氧的摩尔V 2为2-6,起始反应气体混合物中的分子氧与起始反应混合物中的丙烯的摩尔比为1.3-2.4。

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