Production method of p-aminophenol
A technology of p-aminophenol and its production method, which is applied in chemical instruments and methods, preparation of amino hydroxyl compounds, preparation of organic compounds, etc., can solve problems such as pollution yield, and achieve the effect of high yield and low cost
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Embodiment 1
[0050] First, 60% methanol and p-nitrophenol with a molar ratio of 1:0.6 are mixed and dissolved by an in-line mixer. The dissolved material is metered into the hydrogenation unit through the pump according to the flow rate of 5000L / h, and the modified Raney nickel catalyst is added, the main body is Ni, and the additive is Mo or Cr or Ti or Fe or Co or Cu or Mn or Ba metal One or more types of salt.
[0051] Open the hydrogen valve and the heated steam valve of the hydrogenation kettle, heat and feed hydrogen, keep the reaction temperature at 60-180°C, and the reaction pressure at 0.5-2.0MPa; carry out continuous hydrogenation reaction in the presence of a catalyst. After 6-8 hours of reaction, the qualified hydrogenation liquid enters the catalyst settler, and the catalyst separated in the settler returns to the hydrogenation system. After decompression, the supernatant liquid from the settler enters the ceramic membrane filtration system to remove the catalyst. The clear l...
Embodiment 2
[0055]Basically the same as Example 1, the difference is the modified Raney nickel catalyst, the main body is Ni, and the additives are Mo, Cr or Mo, Ti or Mo, Fe or Mo, Co or Mo, Cu or Mo, Mn or Mo, Ba Or Mo, Cr, Ti or Mo, Cr, Fe or Mo, Cr, Co or Mo, Cr, Cu or Mo, Cr, Mn or Mo, Cr, Ba or Mo, Cr, Ti, Fe or Mo, Cr, Ti , Co or Mo, Cr, Ti, Cu or Mo, Cr, Ti, Mn or Mo, Cr, Ti, Ba or Mo, Cr, Ti, Fe, Co or Mo, Cr, Ti, Fe, Cu or Mo, Cr , Ti, Fe, Mn or Mo, Cr, Ti, Fe, Ba or Mo, Cr, Ti, Fe, Co, Cu or Mo, Cr, Ti, Fe, Co, Mn or Mo, Cr, Ti, Fe, Co , Ba or Mo, Cr, Ti, Fe, Co, Cu, Mn or Mo, Cr, Ti, Fe, Co, Cu, Ba or Mo, Cr, Ti, Fe, Co, Cu, Mn, Ba metal salts.
[0056] Features of the invention
[0057] In the production of p-aminophenol in the present invention, the catalyst can be recycled in the production process.
[0058] Methanol used in the reaction process can also be recycled.
[0059] The hydrogenation reaction is carried out continuously during the reaction process.
[0060] T...
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