Hydrogen bromide purifying device and method
A purification method, hydrogen bromide technology, applied in directions such as hydrogen bromide, bromine/hydrogen bromide, etc., can solve problems such as difficulty in realizing industrialized continuous production, adsorbent desorption, difficulty in recovery, and no more than 2 ppm, etc. Small investment, reduced corrosion resistance requirements, and the effect of reducing dosage
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Embodiment 1
[0043] In this embodiment, the weight removal tower 1 and the light removal tower 2 are packed towers, the weight removal tower 1 is 8m high, 0.5mm in diameter, 40 theoretical plates, and has a built-in diameter of 5mm θ ring packing. Among them, the light removal tower 2 is 8m high, 0.5mm in diameter, 30 theoretical plates, and has a built-in 5mm diameter θ ring packing. The feed pipeline and de-weight tower 1 are made of Hastelloy, and the de-light tower 2, product collector 3 and filling bottle 6 are made of stainless steel. Filling pump 5 adopts diaphragm pump.
[0044] The hydrogen bromide crude product flow rate is 30L / min.
[0045] The parameters of weight removal column 1 are set as follows: column temperature -15°C, pressure 0.9MPa, reflux ratio 20. In this state, the hydrogen bromide vaporizes and rises, and the heavy components such as water condense and collect in the bottom of the de-weighting tower in liquid or solid form to realize the removal of heavy compone...
Embodiment 2
[0049] In this embodiment, the weight removal tower 1 is 14 mm high, 1 m in diameter, 60 theoretical plates, and has a built-in Pall ring packing with a diameter of 25 mm. Light removal tower 2 is 14m high, 1m in diameter, 60 theoretical plates, and has a built-in Raschig ring packing with a diameter of 25mm. The feed pipeline and weight removal tower 1 are made of Hastelloy. Bottling 6 is in stainless steel. Filling pump 5 adopts diaphragm pump.
[0050] The hydrogen bromide crude product flow rate is 30L / min.
[0051] The parameters of weight removal tower 1 are set as follows: column temperature -64°C, pressure 0 MPa, reflux ratio 80.
[0052] The parameters of light removal tower 2 are set as follows: column temperature -70°C, pressure 0 MPa, reflux ratio 200.
[0053] After testing, the main components and contents of hydrogen bromide after purification are shown in Table 2.
Embodiment 3
[0055] In this embodiment, the weight removal tower 1 is 6 mm high, 0.1 m in diameter, 40 theoretical plates, and has a built-in Pall ring packing with a diameter of 3 mm. Light removal tower 2 is 6m high, 0.1m in diameter, 30 theoretical plates, and has a built-in Raschig ring packing with a diameter of 3mm. The filling bottle 6 is made of stainless steel. Filling pump 5 adopts diaphragm pump.
[0056] The hydrogen bromide crude product flow rate is 30L / min.
[0057] The parameters of weight removal tower 1 are set as follows: column temperature 30°C, pressure 2.3MPa, reflux ratio 80.
[0058] The parameters of light removal tower 2 are set as follows: column temperature 20°C, pressure 2.3MPa, reflux ratio 280.
[0059] After testing, the main components and contents of hydrogen bromide after purification are shown in Table 2.
[0060] Table 2
[0061]
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