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    • 4. 发明专利
    • PRODUCTION OF OXIDIZED OLEFINS
    • CA2839904A1
    • 2013-01-24
    • CA2839904
    • 2012-06-22
    • DOW TECHNOLOGY INVESTMENTS LLC
    • NEWMAN KENT EOSBORNE BERNIE BSZUL JOHN F
    • B01J8/06B01J19/00
    • The present disclosure includes a system and method for the pro¬ duction of oxidized olefins. Two or more reactors include a number of reaction tubes each having a first surface defining a first side and a second surface defining a second of each of the tubes side are provided. A catalyst for catalytic oxidation of olefins can be located on the first side of the number of reaction tubes is included. A com¬ mon supply line supplies inlets to each reactor that provide a mixture comprising olefins and oxygen to the catalyst. Product outlet streams of each reactor receive at least the oxidized olefin product and are joined to a single product stream. Coolant fluid passes through the re¬ actors to remove heat from the number of reaction tubes and flows into a single coolant drum connected to the two or more reactors. The single coolant drum receives the coolant fluid from a number of coolant fluid outlet streams of each of the reactors. The single coolant drum supplies the coolant fluid at a common temperature to a num¬ ber of coolant fluid inlet streams of each reactor.
    • 5. 发明专利
    • PRODUCTION OF OXIDIZED OLEFINS
    • CA2839904C
    • 2020-09-01
    • CA2839904
    • 2012-06-22
    • DOW TECHNOLOGY INVESTMENTS LLC
    • NEWMAN KENT EOSBORNE BERNIE BSZUL JOHN F
    • B01J8/06B01J19/00
    • The present disclosure includes a system and method for the pro¬ duction of oxidized olefins. Two or more reactors include a number of reaction tubes each having a first surface defining a first side and a second surface defining a second of each of the tubes side are provided. A catalyst for catalytic oxidation of olefins can be located on the first side of the number of reaction tubes is included. A com¬ mon supply line supplies inlets to each reactor that provide a mixture comprising olefins and oxygen to the catalyst. Product outlet streams of each reactor receive at least the oxidized olefin product and are joined to a single product stream. Coolant fluid passes through the re¬ actors to remove heat from the number of reaction tubes and flows into a single coolant drum connected to the two or more reactors. The single coolant drum receives the coolant fluid from a number of coolant fluid outlet streams of each of the reactors. The single coolant drum supplies the coolant fluid at a common temperature to a num¬ ber of coolant fluid inlet streams of each reactor.