Separation equipment and separation process for HF (Hydrogen Fluoride) in difluoromethane reaction gas
A technology for difluoromethane and separation equipment, which is applied in the field of separation equipment for HF in difluoromethane reaction gas, can solve the problems of increased equipment and energy consumption, increased production cost of difluoromethane, environmental pollution and the like, and achieves simple structure and high energy efficiency. The effect of low consumption and waste reduction
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Embodiment 1
[0027] Pass the difluoromethane reaction gas passing through the reflux tower into the hydrogen fluoride absorption tower. The high-level tank mass concentration 98% concentrated sulfuric acid enters from the top of the hydrogen fluoride absorption tower. The temperature of the hydrogen fluoride absorption tower is controlled at 20℃, the pressure is controlled at 1.0MPa, and it is absorbed by hydrogen fluoride. The mixed gas after absorption by the tower enters the falling film absorber, the falling film absorber absorbs most of the hydrogen chloride gas in the mixed gas, and then the mixed gas enters the washing tower for washing, the concentration of hydrochloric acid is recycled to about 32% for collection, and the hydrogen fluoride absorption tower is concentrated. Sulfuric acid is recycled to the anhydrous hydrogen fluoride production unit. When detecting different concentrations of hydrogen fluoride extracted by concentrated sulfuric acid, the content of fluoride ion in hy...
Embodiment 2
[0032] Pass the difluoromethane reaction gas passing through the reflux tower into the hydrogen fluoride absorption tower, the high-level tank mass concentration 98% concentrated sulfuric acid enters from the top of the hydrogen fluoride absorption tower, the temperature of the hydrogen fluoride absorption tower is controlled at 10-40℃, and the pressure is controlled at 1.0MPa. The mixed gas absorbed by the hydrogen fluoride absorption tower enters the falling film absorber, and the falling film absorber absorbs most of the hydrogen chloride gas in the mixed gas, and then the mixed gas enters the washing tower for washing, the hydrochloric acid concentration is recycled to about 32% for collection, and the hydrogen fluoride absorption tower The concentrated sulfuric acid in the kettle is recycled to the anhydrous hydrogen fluoride production unit. When the content of hydrogen fluoride extracted by concentrated sulfuric acid is 0.1 (wt)%, the content of fluoride ion in hydrochlor...
Embodiment 3
[0038] Hydrogen fluoride absorption tower pressure (MPa) 32% hydrochloric acid fluoride ion content (ppm) 0.121.6 0.514.2 1.08.7 1.55.9
[0039] From Example 3, it can be found that as the pressure of the hydrogen fluoride absorption tower increases, the fluoride ion content of 32% hydrochloric acid by mass concentration decreases accordingly. The pressure is preferably controlled at 1.0 to 1.5 MPa, but the reflux tower pressure is generally used as the standard, and is generally controlled at A slightly lower pressure than the reflux tower is better.
[0040] In the process of preparing difluoromethane with methylene chloride and anhydrous hydrogen fluoride, the present invention solves how to effectively separate the hydrogen fluoride contained in the reaction gas. The reaction gas mainly includes difluoromethane, monofluoro-chloromethane, hydrogen fluoride and hydrogen chloride. Based on the built-up anhydrous hydrogen fluoride production device, the 98% concentrated sulf...
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