Catalytic combustion treatment device and treatment method for organic waste gases
A catalytic combustion and organic waste gas technology, applied in the direction of combustion method, combustion type, incinerator, etc., can solve the problems of affecting the service life of the catalyst, troublesome manufacturing and processing, and increasing investment costs, so as to improve the comprehensive utilization effect and avoid life reduction. The effect of reducing operating costs
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[0018] The following describes the implementation of the method of the present invention in conjunction with the accompanying drawings:
[0019] Such as figure 1 As shown, the organic waste gas catalytic combustion treatment device of the present invention is composed of two catalyst beds A and B, regulating valves A and B, control system 8, exhaust gas online analysis equipment 7 and connecting pipelines connected in series. When the target gas concentration or the processed gas volume in the exhaust gas entering the device is low, the target gas concentration in the main exhaust line 2 is at a low level, that is, below the set value, due to the sufficient reaction. At this time, the control system opens the regulating valve 5 At the same time, the regulating valve 6 is closed, and only the catalyst bed layer A participates in the catalytic combustion reaction of exhaust gas; when the target gas concentration in the intake pipeline increases or the amount of exhaust gas increase...
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[0021] Example
[0022] The organic waste gas discharged from the grease trap, flotation tank, and oily sewage tank of a sewage treatment plant is treated with a catalytic combustion device. Under normal operating conditions, the concentration of non-methane total hydrocarbons in the exhaust gas discharged from grease traps, flotation tanks and oily sewage tanks is 2000~5000mg / Nm 3 , But during the big breathing period of the oily sewage tank, the concentration of non-methane total hydrocarbons in the mixed exhaust gas is 4000~8000mg / Nm 3 . Main operating conditions: The entire device consists of two catalyst beds. Under normal operating conditions, the exhaust gas passes through one bed. During the oily sewage tank, the exhaust gas passes through the two catalyst beds. The exhaust gas enters the catalyst bed at a temperature of 350℃. Reaction space velocity 8000h -1 .
[0023] After treatment, the concentration of non-methane total hydrocarbons in the exhaust gas is purified 3 . ...
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