Catalyst for prepn. of m-dimethyl amino benzoic acid
A technology of m-dimethylaminobenzene and catalyst, which is applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem of unstable catalyst reaction activity and product yield. And the purity is not ideal and other problems, to achieve good economic benefits, improve reaction stability, reduce production costs.
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Embodiment 2
[0024] Catalysts were prepared under the same conditions as in Example 1, except that the types and weight percentages of the catalyst components were changed to prepare catalysts B, C, D, and E respectively. The catalyst composition is shown in Table 1.
[0025] Example
[0026] Catalysts A, B, C, D, and E prepared in Examples 1 to 2 are used in m-nitrobenzoic acid reduction-alkylation under different reaction conditions to prepare m-dimethylaminobenzoic acid, wherein the m-nitrobenzoic acid is fixed Benzoic acid amount 0.1 mole, catalyst consumption, acetic acid amount are based on 0.1 mole (16.7 grams) m-nitrobenzoic acid, and other reaction process conditions are listed in Table 2, and concrete reaction process is as follows:
[0027] With 0.1 mole (16.7 grams) m-nitrobenzoic acid (chemically pure), methyl alcohol (chemically pure), acetic acid (chemically pure) and catalyzer, add in the autoclave, feed the air in the nitrogen displacement reactor 2 times, then F...
Embodiment 1
[0030] Catalyst A life test prepared in Example 1.
[0031]Catalyst A is used for the reaction of preparing m-dimethylaminobenzoic acid, wherein 0.1 mole of m-nitrobenzoic acid is fixed, and acetic acid and catalyst consumption are based on 0.1 mole (16.7 grams) m-nitrobenzoic acid, and the amount of acetic acid is 1%, specifically The reaction process is the same as in Example 3, and other different process conditions and product yields are shown in Table 4. After the first reaction finishes, the catalyst is filtered out for the next reaction; or for intermittent and continuous reactions, catalyst A is preserved in methanol solution In , the catalyst was filtered out when it was used again, and it was directly put into the reactor for use without regeneration treatment. Catalyst A was recycled 50 times in total.
[0032] Catalyst heavy
[0033] It can be seen from the reaction results in Table 4 that after the catalyst A was recycled 50 times, it still showed good r...
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