Catalyst for synthesizing m-phenylenediamine from m-dinitrobenzene by hydrogenation reaction and application thereof
A technology for m-dinitrobenzene and m-phenylenediamine, which is applied in the field of catalysis and achieves the effects of simple preparation process, improved selectivity and high activity
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Embodiment 1
[0019] Embodiment 1: the preparation of catalyst 1
[0020] (1) First prepare the inner core of the catalyst, add platinum dichloride, silver nitrate and zinc chloride into 1000ml pure water according to the molar ratio, fully stir and mix uniformly, and form the active component slurry A, wherein the first component and the second The molar ratio of the elements of the components is 1:3;
[0021] (2) Co-precipitating the active component slurry A to form the inner core slurry of the catalyst, drying at 70° C., molding, and roasting at 300° C. for 8 hours to obtain the inner core of the catalyst;
[0022] (3) Then prepare the outer layer of the catalyst, then add lead nitrate, silver nitrate, zinc chloride and lanthanum chloride into 1000ml pure water according to the molar ratio, fully stir and mix to form the active component slurry B, wherein the first group The element molar ratio of the second component and the third component is 1:3:3;
[0023] (4) Finally, the prepare...
Embodiment 2
[0025] Embodiment 2: the preparation of catalyst 2
[0026] (1) First prepare the inner core of the catalyst, add platinum nitrate, palladium sulfate and copper chloride into 1000ml pure water according to the molar ratio, fully stir and mix to form the active component slurry A, wherein the first component and the second component The molar ratio of the elements is 1:5;
[0027] (2) Co-precipitating the active component slurry A to form the inner core slurry of the catalyst, drying at 70° C., molding, and roasting at 300° C. for 8 hours to obtain the inner core of the catalyst;
[0028] (3) Then prepare the outer layer of the catalyst, then add platinum nitrate, palladium sulfate, copper chloride and lanthanum chloride into 1000ml pure water according to the molar ratio, fully stir and mix uniformly, and form the active component slurry B, wherein the first group The elemental molar ratio of the second component and the third component is 1:5:3;
[0029] (4) Finally, the pr...
Embodiment 3
[0037] Example 3: The performance measurement of using the above-mentioned catalyst in the reaction of methanol dehydration to prepare dimethyl ether. Using a fixed bed reactor, the reaction temperature is 200°C, the pressure is 1Mpa, the weight hourly space velocity is 5h-1, and industrial sewage ethanol is used as the reaction raw material to investigate the performance of the above catalyst in the reaction of methanol to dimethyl ether. The results are listed below Table 1 and Table 2.
[0038] The reaction performance of table 1 catalyst
[0039] Application example
[0040] The stability of table 2 catalyst 1
[0041] operation hours
[0042] (h)
[0043] As can be seen from the above results, compared with the prior art, the reaction performance and stability of the catalyst prepared by the present invention have been greatly improved. After 400 hours of continuous reaction, the activity of the catalyst is still very high without significa...
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