Method and device for purifying and separating methyl mercaptan
A technology for purification and separation of methyl mercaptan, applied in chemical instruments and methods, organic chemistry, preparation of organic compounds, etc., can solve the problems of hydrogen sulfide affecting the yield and achieve the effect of improving separation efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0032] The purification and separation device of embodiment 1 methyl mercaptan
[0033] Such as figure 1 Shown in, the purification and separation device of methyl mercaptan comprises dehydrogen sulfide tower 1, evaporation tower 2, water absorption tower 3, absorption liquid absorption tower 4 and distillation-condensation tower 5;
[0034] The bottom of the dehydrogenation tower 1 is provided with an organic phase inlet, the top of the desulfurization tower 1 is provided with an H2S outlet, the bottom of the dehydrogenation tower 1 is connected to the bottom of the evaporation tower 2, and the desulfurization The top of the hydrogen tower 1 communicates with the bottom of the water absorption tower 3, and a circulating spray system 7 is provided between the bottom and the top of the water absorption tower 3, and the circulating spray system 7 includes a The shower head in the tower 3 and the circulation pipeline that is connected with the bottom of the water absorption towe...
Embodiment 2
[0035] The purification separation method of embodiment 2 methyl mercaptan
[0036]The mixed gas coming out of the methyl mercaptan reactor is heat-exchanged, the temperature is reduced from 300-400°C to 110-130°C, the pressure is 8-10bar, and the mixed gas is condensed into an aqueous phase and an organic phase. In the condensed organic phase, the content of methylmercaptan>80wt%, the content of methanol is 1-8wt%, the content of hydrogen sulfide is 1-15wt%, and the content of dimethyl sulfide is 0.3-3wt%. ~14bar, the temperature at the top of the tower is 25~30°C to distill hydrogen sulfide until the content of hydrogen sulfide in the organic phase is less than 1wt%; dehydrogen sulfide tower 1 uses trays or packing or tubes, and the tray style, packing method and tubes are not used limit;
[0037] The organic phase of the tower kettle of the dehydrogenation tower 1 is transferred to the evaporation tower 2. The purpose of the evaporation tower 2 is to gasify the methyl merc...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
