Low-temperature crude benzene hydrogenation process
A crude benzene and low temperature technology, applied in the field of crude benzene low temperature hydrogenation process, can solve the problems of low added value, large loss of aromatic compounds, environmental pollution, etc., and achieve the effect of improving processing quality and reducing processing technology.
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Embodiment 1
[0022] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:
[0023] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;
[0024] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 80°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;
[0025] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 160°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;
[0026] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main cataly...
Embodiment 2
[0037] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:
[0038] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;
[0039] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 90°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;
[0040] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 170°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;
[0041] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main cataly...
Embodiment 3
[0052] A kind of crude benzene low-temperature hydrogenation process is proposed in this embodiment, comprising the following steps:
[0053] S1: Preliminary distillation: the crude benzene raw material enters the distillation mechanism after being filtered, and the crude benzene component is separated at the top of the distillation mechanism;
[0054] S2: liquid-phase catalytic prehydrogenation: the crude benzene component in S1 is mixed with hydrogen and heated to 100°C under the condition of Co-Mo as catalyst and hydrogen oil to obtain the first product;
[0055] S3: gas-phase catalytic prehydrogenation step: heating the first product obtained by liquid-phase catalytic pre-hydrogenation in S2 to 180°C under the condition of NiW as catalyst and hydrogen oil to obtain the second product;
[0056] S4: The main catalytic hydrogenation reaction, the second product obtained in S3 is subjected to the main catalytic hydrogenation reaction, the reaction temperature of the main catal...
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