Method for preparing DCB reduzate through continuous catalytic hydrogenation reduction
A catalytic hydrogenation and catalyst technology, which is applied in the preparation of hydrazine, chemical recovery, organic chemistry, etc., can solve the problems of unstable reaction control, toluene-containing waste gas emission, and large volume of the reactor, so as to achieve internal recycling and reduce by-products Fewer, more selective effects
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Embodiment 1
[0032] Add 600g of adjacent reactors to 3 2L continuous reactors connected in series (divided into the first-stage reactor / reactor, the second-stage reactor / reactor, and the third-stage reactor / reactor according to the order in series) Nitrochlorobenzene, 720g toluene, 250g 30% liquid caustic soda, 204g desalinated water and 6g 1% Pt / C catalyst, replace the air with nitrogen twice, and then replace the nitrogen with hydrogen twice, start stirring, and heat the reaction mass to 90 ℃, continuously feed hydrogen, control the hydrogen pressure at 1MPa, control the reaction temperature at 90-95 ℃, until all the three reactors react without absorbing hydrogen, the first stage of the intermittent reaction ends, and the substrate preparation for the continuous reaction is completed;
[0033] After the completion of the first step reaction, open the overflow feed valves of 3 kettle-type reactors, and pump o-nitrochlorobenzene, toluene, 30% liquid caustic soda and For desalted water, th...
Embodiment 2
[0038] 600g of o-nitrochlorobenzene, 720g of toluene, 250g of 30% liquid caustic soda, 204g of desalinated water and 4g of 1% Pt / C catalyst were added to three series-connected 2L kettle-type continuous reactors respectively, and the air was replaced with nitrogen for two times. After replacing the nitrogen with hydrogen twice, start stirring, heat the reaction mass to 90°C, continuously feed hydrogen, control the hydrogen pressure at 1.5MPa, and control the reaction temperature at 90-95°C until all the three reactors react without absorbing hydrogen. , the first stage of the batch reaction ends, and the substrate preparation of the continuous reaction is completed;
[0039]After the completion of the first step reaction, open the overflow feed valves of 3 kettle-type reactors, and pump o-nitrochlorobenzene, toluene, 30% liquid caustic soda and For desalted water, the feed rate of o-nitrochlorobenzene is 100g / h, the feed rate of toluene solvent is 120g / h, the feed rate of 30% ...
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