Treatment method for gas containing high-concentration benzene
A treatment method and high-concentration technology, applied in gas treatment, separation methods, chemical instruments and methods, etc., can solve the problems of large heat release, high investment and operating costs, and large equipment.
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Embodiment 1
[0061] Benzene is loaded to produce benzene-containing gas, and nitrogen is used as protective gas. The main component of the benzene-containing gas produced is nitrogen, and the benzene concentration can reach up to 4vol% (about 139g / Nm 3 ). Capacity 500m 3 / h. Firstly, it is absorbed with a supergravity absorber, the absorbent is ethylbenzene, and the flow rate is 2m 3 / h, the number of theoretical plates for mass transfer in the absorber is 9. Then pressurize 15kPa by the fan, and the absorbed gas enters the condenser, and the lowest condensation temperature is -45°C. Then it enters the activated carbon adsorption tower, and the two towers are switched to use. Each tower is filled with 4 tons of activated carbon adsorbent. The adsorption time was 10 minutes. The vacuum desorption time is 8 minutes. The adsorption cycle is 10 minutes, and the maximum vacuum is 5kPa absolute pressure. The desorbed gas is returned to the inlet of the condenser. The liquid produced by...
Embodiment 2
[0063] The benzene storage tank produces benzene-containing gas, and nitrogen is used as the protective gas. The main component of the benzene-containing gas produced is nitrogen, and the benzene concentration can reach up to 4vol% (about 139g / Nm 3 ). Capacity 200m 3 / h. Firstly, it is absorbed with a supergravity absorber, the absorbent is a mixture of xylene and ethylbenzene, and the flow rate is 1m 3 / h, the number of theoretical plates for mass transfer in the absorber is 10. The absorbed gas enters the condenser, and the condensation temperature is as low as -25°C. Then it enters the adsorption tower, and the two towers are switched to use. Each tower is filled with 3 tons of activated carbon adsorbent and 1 ton of hydrophobic zeolite adsorbent. The adsorption time was 8 minutes. The vacuum desorption time is 6 minutes. The adsorption cycle is 8 minutes, and the maximum vacuum is 3kPa absolute pressure. The desorbed gas is returned to the inlet of the condenser. ...
Embodiment 3
[0065] When benzene is unloaded, benzene-containing gas is generated, and nitrogen is used as protective gas. The main component of the benzene-containing gas produced is nitrogen, and the benzene concentration can reach up to 4.5vol% (about 157g / Nm 3 ). Capacity 600m 3 / h. First use a packed absorption tower for absorption, the absorbent is a mixture of toluene, xylene and ethylbenzene, wherein toluene is 10%, xylene is 15%, ethylbenzene is 75%, and the flow rate is 4m 3 / h, the number of theoretical plates for mass transfer in the absorber is 10. The absorbed gas enters the condenser, and the condensation temperature is as low as -20°C. Then enter the hydrophobic silica gel adsorption tower, and switch between the two towers. Each tower is filled with 7 tons of silica gel adsorbent. The adsorption time was 5 minutes. The vacuum desorption time is 4 minutes, and the maximum vacuum degree is an absolute pressure of 8kPa. The adsorption cycle is 5 minutes. The desorbed...
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