Dehydration process and dehydration device for crude aniline
A technology of crude aniline and crude aniline tank, which is applied in the field of dehydration process and dehydration device of crude aniline, which can solve the problems that the expected effect cannot be achieved, the excellent level cannot be achieved, and the market competitiveness is weak, so as to improve efficiency and reduce the moisture content of aniline , to ensure the effect of safe operation
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Embodiment 1
[0039] A dehydration process of crude aniline consisting of the following steps:
[0040] a) Crude aniline is produced in reactor 1, and the lateral line temperature of reactor 1 is 210 °C;
[0041] b) Crude aniline through the air cooler 2 and water cooler 3 respectively for air cooling cooling and water cooling cooling, wherein the air cooler 2 power is fully open, the water cooler 3 circulating water is fully open, after the crude aniline decanting tank 4 to obtain crude dehydrated crude aniline, into the crude aniline tank 5; the crude aniline decanting tank 4 and crude aniline tank 5 tank temperature 34 ° C;
[0042] c) the crude dehydrated crude aniline is fed into the catalyst thickener 6 and the dehydration tower 8, after thickening dehydration, that is, obtained; the catalyst thickener 6 and the dehydration tower 8 of the kinetic equipment sealing liquid medium is aniline, the catalyst thickener 6 sealed water flow is 40L / h; the dehydration tower 8 negative pressure is ...
Embodiment 2
[0051] A dehydration process of crude aniline consisting of the following steps:
[0052] a) Crude aniline is produced in reactor 1, and the lateral line temperature of reactor 1 is 213 °C;
[0053] b) Crude aniline through the air cooler 2 and water cooler 3 respectively for air cooling cooling and water cooling cooling, wherein the air cooler 2 power fully open, water cooler 3 circulating water fully open, through the crude aniline decanting tank 4 to obtain crude dehydrated crude aniline, into the crude aniline tank 5; the crude aniline decanting tank 4 and crude aniline tank 5 tank temperature 32 ° C;
[0054] c) The crude dehydrated crude aniline is fed into the catalyst thickener 6 and the dehydration column 8, after thickening dehydration, that is, obtained; the catalyst thickener 6 and the kinetic equipment sealing liquid medium of the dehydration tower 8 is aniline, the sealing water flow of the catalyst thickener 6 is 50L / h; the negative pressure of the dehydration tow...
Embodiment 3
[0056] A dehydration process of crude aniline consisting of the following steps:
[0057] a) Crude aniline is produced in reactor 1, and the lateral line temperature of reactor 1 is 214 °C;
[0058] b) Crude aniline through the air cooler 2 and water cooler 3 respectively for air cooling cooling and water cooling cooling, wherein the air cooler 2 power fully open, water cooler 3 circulating water fully open, after the crude aniline decanting tank 4 to obtain crude dehydrated crude aniline, into the crude aniline tank 5; the crude aniline decanting tank 4 and crude aniline tank 5 tanks temperature 38 ° C;
[0059] a) the crude dehydrated crude aniline is fed into the catalyst thickener 6 and the dehydration tower 8, after thickening dehydration, that is, obtained; the catalyst thickener 6 and the dehydration tower 8 of the kinetic equipment sealing liquid medium is aniline, the catalyst thickener 6 sealed water flow is 55L / h; the dehydration tower 8 negative pressure is 40.8kPa, t...
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