Method for clearing harmful gas and dust in long tunnel
A harmful gas and dust technology, applied in the field of traffic engineering, can solve the problems of long ventilation time, high equipment damage rate, large pressure loss, etc., to improve air quality, speed up construction progress, and shorten ventilation time.
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Embodiment 1
[0024] The harmful gases CO, CO 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool by the fan. Using centrifugal fan, pressure 8kPa, air volume 2300m 3 / h, the harmful gases CO and CO inhaled in the tunnel 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool, and are reacted or cleaned with alkaline compounds in the degradation pool, preferably the alkaline compound sodium carbonate, and CO, a small amount of NO, and water vapor that are difficult to react with alkaline compounds are filtered through a porous fiber separation membrane After steam. The CO and a small amount of NO filtered from the porous fiber separation membrane, with a pressure of 8kPa, enter the low-temperature pressure swing adsorption tower with a temperature of 10-30°C for adsorption. CO and a small amount of NO are adsorbed in the adsorption tower, and then transported out of the pressure swing adsorption tower Tunnel, the adsorption tower is heated to 80-135°C, preferabl...
Embodiment 2
[0026] The harmful gases CO, CO 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool by the fan. Using centrifugal fan, the air volume is 2700m 3 / h, the harmful gases CO and CO inhaled in the tunnel 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool, and are reacted or cleaned with alkaline compounds in the degradation pool, preferably the alkaline compound sodium carbonate, and CO, a small amount of NO, and water vapor that are difficult to react with alkaline compounds are filtered through a porous fiber separation membrane After steam. The CO and a small amount of NO filtered from the porous fiber separation membrane, with a pressure of 6kPa, enter the low-temperature pressure swing adsorption tower with a temperature of 10-30°C for adsorption. CO and a small amount of NO are adsorbed in the adsorption tower, and then transported out of the pressure swing adsorption tower Tunnel, the adsorption tower is heated to 80-135°C, preferably 120°C,...
Embodiment 3
[0028] The harmful gases CO, CO 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool by the fan. Using centrifugal fan, pressure 4kPa, 2900m 3 / h, the harmful gases CO and CO inhaled in the tunnel 2 , NO, NO 2 , sulfide, and dust are sent to the degradation pool, and are reacted or cleaned with alkaline compounds in the degradation pool, preferably the alkaline compound sodium carbonate, and CO, a small amount of NO, and water vapor that are difficult to react with alkaline compounds are filtered through a porous fiber separation membrane After steam. The CO and a small amount of NO filtered from the porous fiber separation membrane, with a pressure of 4kPa, enter the low-temperature pressure swing adsorption tower with a temperature of 10-30°C for adsorption. CO and a small amount of NO are adsorbed in the adsorption tower, and then transported out of the pressure swing adsorption tower Tunnel, the adsorption tower is heated to 80-135°C, preferably 120°C, th...
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