Continuous producing process of anti-aging agent 4020
A production process and anti-aging agent technology, which is applied in the continuous production process of anti-aging agent 4020, can solve the problems of affecting catalyst life and single-pass output, large consumption of methyl isobutyl ketone, and catalyst activation is easy to over-temperature deactivation, etc., to achieve easy Disassembly, low cost, good sealing effect
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Embodiment 1
[0022] Such as figure 1 As shown, the gas-liquid-solid three-phase fixed-bed hydrogenation reactor used in the continuous production process of antioxidant 4020 of this embodiment includes a main container, namely a cylinder, a discharge port, a discharge port, a feed pre-distributor, The upper head, the lower head, the upper support, the lower support and the temperature measuring port. The main container is a cylinder with a height of 14.6m and a diameter of 1200mm. The feed pre-distributor is a tube-type pre-distributor , Installed in the lower part of the reactor and surrounded by ceramic balls, the nozzle of the tube-type pre-distributor faces downwards, the upper head is an oval head, the lower head is an oval head, and the main container is The bottom of the catalyst layer is provided with a manhole, which makes the replacement of the catalyst more convenient. The main body of the reactor is made of stainless steel composite plates. The annual output of this reactor can r...
Embodiment 2
[0025] The gas-liquid-solid three-phase fixed-bed hydrogenation reactor used in this example is the same as that in example 1.
[0026] Such as figure 2 As shown, when 4020 is produced, the ratio of ketone to amine is 2:1, and the ratio of hydrogen to oil is 2000:1. The raw materials 4-aminodiphenylamine, hydrogen and methyl isobutyl ketone first enter the jacketed sleeve heated by heat transfer oil. The static mixer composed of the preheater E101 is preheated to 150°C. After part of the raw materials are vaporized, they enter the static mixer H101, and then the materials enter the reactor R101 together through the tube-type pre-distributor. The liquid material fills the reactor, and hydrogen is bubbled in the liquid material. Under the action of the nickel catalyst, the reaction temperature is 165℃ and the pressure is 6MPa, and it gradually reacts with the raw materials. The reacted materials are discharged through the discharge port and reacted. The conversion rate can reach ...
Embodiment 3
[0028] The gas-liquid-solid three-phase fixed-bed hydrogenation reactor used in this example is the same as that in example 1.
[0029] Such as figure 2 As shown, when 4020 is produced, the ratio of ketone to amine is 4:1, and the ratio of hydrogen to oil is 5000:1. The raw materials 4-aminodiphenylamine, hydrogen and methyl isobutyl ketone first enter the jacketed casing heated by heat transfer oil. The static mixer composed of the preheater E101 is preheated to 220°C. After part of the raw materials are vaporized, they enter the static mixer H101, and then the materials enter the reactor R101 together through the tube-type pre-distributor. The liquid material fills the reactor, and hydrogen is bubbled in the liquid material. Under the action of the nickel catalyst, the reaction temperature is 230°C and the pressure is 5.8MPa, and gradually reacts with the raw materials. The reacted materials are discharged through the discharge port. The reaction conversion rate can reach 97%...
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