High concentration organic waste gas treatment method and high concentration organic waste gas treatment apparatus
A technology of organic waste gas and treatment method, applied in combustion methods, separation methods, chemical instruments and methods, etc., can solve the problems of inability to recover hydrocarbon substances, failure to achieve the purpose of treatment, waste of hydrocarbon resources, etc., so as to achieve no unsafe hazards. , Enhance stability and safety, and ensure the effect of safe combustion
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Embodiment 1
[0032] Using the invention attached figure 1 The process of handling the escaped oil and gas from the petrol loading of a small crane tube train in a refinery. The emission of the escaped gas is 300m 3 / h, the total hydrocarbon concentration of the gas is 300-413g / m 3 , Fugitive gas is absorbed by normal third-line gas oil, and the absorbed liquid-gas ratio is 100L / m 3 , The absorption temperature is 35℃, the absorption pressure is 100kPa, so that the total hydrocarbon concentration of the exhaust gas after absorption is 25000-30000mg / m 3 about. The selected air distribution air volume is 90000m 3 The heating furnace above / h burns the gas after diesel absorption, and the total hydrocarbon concentration of the gas after the organic waste gas is mixed with the distribution air is less than 100mg / m 3 , Oxygen consumption of oxidized pollutants is less than 0.028%. After being absorbed and incinerated, the fugitive oil and gas from gasoline loading can reach the standard emission, ...
Embodiment 2
[0034] Using the invention attached figure 1 The process of handling the escaped oil and gas from gasoline loading on a large crane tube train in a refinery, and the emission of the escaped gas is 500m 3 / h, the total hydrocarbon concentration of the gas is 200-450g / m 3 , Fugitive gas is absorbed by normal third-line gas oil, and the absorbed liquid-gas ratio is 100L / m 3 , The absorption temperature is 35℃, the absorption pressure is 150kPa, so that the total hydrocarbon concentration of the exhaust gas after absorption is 20000-26000mg / m 3 . The selected air distribution air volume is 130000m 3 The heating furnace above / h burns the gas after diesel absorption, and the total hydrocarbon concentration of the gas after the organic waste gas is mixed with the distribution air is less than 100mg / m 3 , Oxygen consumption of oxidized pollutants is less than 0.028%. After being absorbed and incinerated, the fugitive oil and gas from gasoline loading can reach the standard emission, an...
Embodiment 3
[0036] Using the invention attached figure 1 The process of handling the escaped oil and gas from gasoline loading on a large crane tube train in a refinery, and the emission of the escaped gas is 500m 3 / h, the total hydrocarbon concentration of the gas is 200-450g / m 3 , Fugitive gas is absorbed by normal third-line gas oil, and the absorbed liquid-gas ratio is 80L / m 3 , The absorption temperature is 10℃, the absorption pressure is 80kPa, so that the total hydrocarbon concentration of the exhaust gas after absorption is 15000-20000mg / m 3 . The selected air distribution air volume is 100000Nm 3 The heating furnace above / h burns the gas after diesel absorption, and the total hydrocarbon concentration of the gas after the organic waste gas is mixed with the distribution air is less than 100mg / m 3 , Oxygen consumption of oxidized pollutants is less than 0.028%. After being absorbed and incinerated, the fugitive oil and gas from gasoline loading can reach the standard emission, and...
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