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

Active Publication Date: 2017-02-01
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
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  • Application Information

AI Technical Summary

Problems solved by technology

However, this method can only enter the follow-up incineration system to continue processing when the exhaust gas concentration is lower than 1 / 4 of the explosion limit, and it is only suitable for the treatment of lower concentration organic waste gas
For high-concentration organic waste gas, since the lower explosion limit of most organic substances is 20,000-50,000 mg / m 3 , because the exhaust gas concentration must be controlled to be lower than 1 / 4 of the explosion limit before it can enter the subsequent incineration treatment, that is, the total hydrocarbon concentration of the exhaust gas is higher than 12500 mg / m3 3 The exhaust gas will be discharged directly from the emergency discharge port, which will not achieve the purpose of treatment
In addition, this device also needs to be equipped with a special air volume balance treatment, and the absorption device in this process only pre-treats impurities, particles and acidic substances in the exhaust gas, and cannot recover hydrocarbons in the exhaust gas, resulting in a large amount of waste of hydrocarbon resources. , poor economy

Method used

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  • High concentration organic waste gas treatment method and high concentration organic waste gas treatment apparatus

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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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Abstract

The invention discloses a high concentration organic waste gas treatment method, which comprises that (1) high concentration organic waste gas enters a diesel oil absorption device, such that the organic matter concentration in the waste gas is stabilized at 5000-35000 mg / m<3> after treatment; (2) by examining and calculating the waste gas emission amount and the organic matter concentration in the step (1), the existing heating furnace having an appropriate wind distribution amount is selected, such that the organic matter concentration is less than 200 mg / m<3> and the oxygen consumption amount of the oxidation pollutant is less than 0.05% after the waste gas and the heating furnace wind distribution air are mixed; (3) under the premise of the step (2), the absorbed waste gas in the step (1) is introduced into a gas mixer according to a certain ratio, and is mixed with the heating furnace wind distribution air; and (4) the mixed gas is conveyed into the heating furnace to burn, and the purified gas achieves the emission standard. According to the present invention, the diesel oil is used to absorb the organic matter in the waste gas and stabilize the organic matter concentration, and the existing suitable heating furnace is selected according to the concentration, such that the normal running of the heating furnace and the wind distribution fan cannot be interfered, and the explosion risk and the insecurity hidden danger do not exist.

Description

Technical field [0001] The invention relates to the technical field of environmentally friendly waste gas treatment, in particular to a method and device for treating high-concentration organic waste gas. Background technique [0002] Light oil products such as gasoline contain a large amount of light hydrocarbon components, which are highly volatile and easy to volatilize during storage, transportation and storage. On the one hand, it produces huge energy waste and economic losses, on the other hand, it brings various hazards to production and the environment, such as easily causing fire and explosion, polluting the environment, and chronic or acute poisoning after human inhalation. Therefore, oil and gas emission reduction and recovery technologies have always been key research topics in the fields of petroleum storage and transportation engineering, environmental engineering, and chemical engineering at home and abroad. At the same time, as relevant environmental protection l...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/18B01D53/72F23G7/06
Inventor 廖昌建方向晨刘忠生王海波王新赵磊
Owner CHINA PETROLEUM & CHEM CORP
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