Pretreatment device and treatment process for fixed bed catalytic hydrogenation
A pretreatment device and catalytic hydrogenation technology, applied in organic chemistry, hydrogenation hydrocarbon production, etc., can solve problems such as uneven distribution of catalyst beds, uneven gas-liquid mixing, etc., to reduce production costs, increase conversion rate, and increase production capacity Effect
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Embodiment 1
[0028] A pretreatment device for catalytic hydrogenation, the hydrogen pipeline 8 is connected with the top of the hydrogen preheater 1, the steam pipeline 9 is connected with the upper part of the hydrogen preheater 1; the bottom of the hydrogen preheater 1 is connected with the falling film steamer 2, and the falling film The steamer 2 is connected to the hydrogenation reactor 3, and the hydrogenation reactor 3 is connected to the recovery system.
[0029] The organic material pipeline 7 is connected to the upper part of the falling film steamer 2; the heat transfer oil system 4 is connected to the lower part of the shell side of the falling film steamer 2 through the pipeline, and the upper part of the shell layer of the falling film steamer 2 is connected to the hydrogenation reactor 3 through the pipeline. .
[0030] The falling film steamer 2 is provided with a plurality of tubes 5, and the tubes 5 extend above the baffle 6 and exceed the organic material inlet.
[0031...
Embodiment 2
[0033] The raw hydrogen is transported into the hydrogen preheater through pipelines, and the hydrogen flow is controlled to 280m 3 / h, 0.8MPa saturated steam is introduced into the hydrogen preheater to ensure that the hydrogen temperature in the preheater is controlled at 120°C, the raw material o-cresol is pumped from the metering tank to the falling film evaporator, and the o-cresol feed is controlled At this time, the set temperature of the shell-side heat transfer oil of the falling film evaporator is 180 °C, and the hydrogen and o-cresol are fully mixed into the fixed-bed hydrogenation reactor. The operating pressure inside the reactor is 0.4 MPa, obtaining O-methylcyclohexanol, the hydrogenation conversion rate is 90.7%.
Embodiment 3
[0035] The specific process operation is shown in Example 2, and the feed hydrogen is 250 m 3 / h, the o-cresol feed is 150L / h, the operating temperature in the hydrogenation reactor is 155°C, the operating pressure is 0.4MPa, the set temperature of the heat transfer oil is 160°C, and the vapor pressure of the hydrogen preheater is 0.78MPa. After the raw material was pretreated, the hydroconversion rate was 81.6%.
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