Whole liquid phase isothermal urea synthesis method and its special equipment
A synthesis method and urea technology, applied in chemical instruments and methods, preparation of organic compounds, preparation of urea derivatives, etc., can solve problems such as low conversion rate of carbon dioxide, easy corrosion of urea synthesis tower, high energy consumption, etc., and achieve increased The effect of increasing the liquid phase reaction area, increasing the utilization of effective space, and increasing the reaction rate
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Embodiment 1
[0014] Example 1, see figure 1 , 2 , processed into a tower body 1, a liquid ammonia inlet 5, a carbon dioxide inlet 6 and a liquid A inlet 7 are opened at the bottom of the tower body 1, a discharge port 8 is opened at the top, and a liquid atomization reactor 2 is installed inside the tower body 1 , the liquid atomization reactor 2 is communicated with the liquid ammonia inlet 5, the carbon dioxide inlet 6 and the first liquid inlet 7, and then the high-efficiency tray 4 is installed on the inner side wall of the upper middle part of the tower body 1, and the high-efficiency tray 4 is multi-layered. A heat exchange pipe 3 is installed on the high-efficiency tray 4, and the heat exchange pipe 3 can be "U" type or "S" type, and the heat exchange pipe 3 communicates with the liquid atomization reactor 2; the liquid atomization reactor 2, The heat exchange pipe 3 and the high-efficiency tray 4 are made of urea grade 316Lmod, TA2, and zirconium materials.
[0015] Then add liqu...
Embodiment 2
[0016] Embodiment 2, the urea synthesis tower is the same as embodiment 1, the difference is that liquid ammonia, carbon dioxide and a liquid ammonia are added to the corresponding feed port in the tower, and the feed NH 3 / CO 2 Molecular number ratio 4.0, H 2 O / CO 2 Molecular number ratio is 1.0; liquid ammonia and first liquid react with carbon dioxide instantly and thoroughly after atomization in the liquid atomization reactor to generate ammonium carbamate solution, which first enters the heat exchange pipe and enters the urea synthesis from the other end of the heat exchange pipe At the bottom of the tower, the temperature in the tower is 190°C and the pressure is 19MPa; the ammonium carbamate solution completes the dehydration reaction in the urea synthesis tower to generate urea, which is discharged from the discharge port, and the conversion rate of carbon dioxide is detected to be 75%.
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