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Method for treating high-temperature oil sludge waste gas

A high-temperature oil and waste gas technology, applied in separation methods, chemical instruments and methods, and dispersed particle separation, can solve the problems of ineffective treatment of oil sludge waste gas, unsuitable promotion of oil sludge waste gas, and affecting equipment stability, etc., to improve energy utilization Efficiency, low cost, and the effect of improving utilization efficiency

Inactive Publication Date: 2020-02-04
鞍钢集团众元产业发展有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, for high-temperature exhaust gas, there are not many options for treatment devices. Usually, filter treatment technology is required to meet the emission concentration of particulate matter less than 10mg / Nm 3 However, the oil contained in this kind of exhaust gas can easily cause the filter material of the filter dust collector to be clogged and compacted. Under high humidity conditions, the tiny particles in the exhaust gas are easy to adhere to the surface of the filter medium, resulting in excessive resistance of the dust removal system and affecting the equipment. The stability of the operation, and it is easy to cause damage to the dust collector, so the conventional single filter dust removal technology cannot effectively deal with this kind of sludge waste gas
In addition, the technologies such as direct incineration, activated carbon adsorption and analysis, and RTO, which are conventionally used for VOC waste gas treatment, are not suitable to be extended to the treatment of this kind of sludge waste gas.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] For a set of oil sludge with a rolling mill output of 3t / d, the indirect distillation method is used to make the oil with a certain boiling point rise with the air flow, and then collected by condensation, and the amount of sludge waste gas produced is 100m 3 / h, the temperature is 300°C, the humidity is 14%, and the exhaust gas contains a small amount of volatile organic pollutants and fine particles.

[0026] The method of treating high-temperature sludge waste gas: firstly capture the sludge waste gas and send it into the flue, mix 200-300 mesh calcium carbonate and calcium oxide according to the mass ratio of 4:1 to prepare the treatment powder, preheat the treatment powder to 260°C and use 0.35kg / The amount of h is sprayed into the sludge waste gas, and after being fully mixed, the sludge waste gas is sent to the gravity settling chamber for 5 to 10 seconds, and then sent to the film-coated filter tube dust collector. The selected filter tube specification is Φ×H×δ...

Embodiment 2

[0028] A kind of oilfield oil sludge is treated by high-temperature steam gasification, and the amount of sludge waste gas produced is 3000m 3 / h, the temperature is 380°C, the humidity is 18% to 20%, and a small amount of dust is entrained in the exhaust gas.

[0029]The method of treating high-temperature sludge waste gas: firstly capture the sludge waste gas and send it into the flue, mix 200-300 mesh calcium oxide and diatomaceous earth according to the mass ratio of 3:1 to prepare the treatment powder, preheat to 340°C, and use two stages, The amount of 15kg / h in each stage is sprayed into the sludge waste gas, and after being fully mixed, the sludge waste gas is sent to the gravity cyclone dust collector for treatment, and then sent to the film-coated filter tube dust collector. The selected filter tube specification is Φ×H×δ=150×3000 ×20mm, discharged after filtering. The concentration of particulate matter in the exhaust gas is 6mg / Nm 3 , the removal rate of non-meth...

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Abstract

The invention relates to a method for treating high-temperature oil sludge waste gas. The method comprises the following steps: firstly, the unstructured oil sludge waste gas in the production processis captured to form structured flue gas, the flue gas is sent to a flue, at the same time, preheated treatment powder is sprayed into the flue to make the powder be in full contact with the oil sludge waste gas to form mixed gas, solid particles with a particle size of 10 [mu]m or more in the mixed gas are firstly removed by a gravity dust collector to preliminarily reduce the solid particle content, and finally, the waste gas is sent to a high-temperature filter type dust collector to further remove fine particles, wherein the high-temperature filter type dust collector adopts a high-temperature resistant film-coated filter tube or film-coated filter bag. The method has the following advantages: the method is suitable for treatment of the oil sludge waste gas with a small emission, a high flue temperature, high humidity and a high methane total hydrocarbon concentration, and can guarantee the treatment effect under the condition that the temperature loss of the oil sludge waste gas is minimized, and the treated waste gas can enter waste-heat utilization in a subsequent process, so that the energy utilization efficiency is improved.

Description

technical field [0001] The invention relates to a method for treating high-temperature oil sludge waste gas. Background technique [0002] Iron and steel, petrochemical, organic chemical and other industries will produce a large amount of sludge mixture containing organic matter with different carbon chain lengths. In order to recover the valuable components, direct or indirect high-temperature steam distillation is usually used to separate the long and short carbon chain organic matter entrained in the sludge. During the separation process, exhaust gas will be discharged, which generally refers to such exhaust gas as sludge exhaust gas . [0003] This kind of sludge waste gas is usually discharged in a low amount, about 50m3 / h~30000m 3 / h, the temperature can reach above 350°C, and the water content is greater than 10%. The exhaust gas contains a variety of oil components with different carbon chain structures such as straight and ring, and the total non-methane hydrocarb...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D50/00
CPCB01D50/20
Inventor 朱雪松王丽英马晨赵明涛刘忠斌
Owner 鞍钢集团众元产业发展有限公司