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Co-processing method for oil depot cleaning waste liquor

A co-processing and waste liquid technology, applied in the direction of combustion method, combustion type, incinerator, etc., can solve the problems of technical and cost infeasibility, no recycling value, waste liquid impossible to landfill, etc., to achieve low cost, The effect of low disposal cost and large disposal volume

Inactive Publication Date: 2017-12-29
重庆利特环保工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] 1. The petroleum and COD in the waste liquid are very high. If it is treated as waste water, it will be difficult and costly to dispose of
For example, CN105152492A discloses a process and system for treating oily sewage in a product oil depot, the process is complicated and the cost is high
[0004] 2. If it is used as incineration alone, most of it will be water, which will consume a lot of heat, which is not feasible technically and costly
[0005] 3. It is impossible to landfill waste liquid
[0006] 4. No recycling value

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] A method for co-processing oil depot cleaning waste liquid, which is disposed according to the following steps:

[0024] 1) Add emulsifier op-10 to the oil depot cleaning waste liquid. The amount of emulsifier added is 0.1% of the mass of the oil depot cleaning waste liquid. Stir evenly and let stand to form a stable emulsion. Improve the flash point and reduce the volatility of gasoline and diesel.

[0025] 2) Mix the emulsion with sludge with a water content of 65%, and stir to obtain a slurry material. The sludge is organic sludge or oily sludge or their mixture, the mass ratio of sludge to emulsion is 2:1, and the viscosity of slurry material is about 30000 centipoise.

[0026] 3) The slurry material is transported to the cement kiln decomposition furnace through the plunger pump for incineration.

Embodiment 2

[0028] A method for co-processing oil depot cleaning waste liquid, which is disposed according to the following steps:

[0029] 1) Add emulsifier op-10 to the oil depot cleaning waste liquid. The amount of emulsifier added is 0.3% of the mass of the oil depot cleaning waste liquid. Stir evenly and let stand to form a stable emulsion. Improve the flash point and reduce the volatility of gasoline and diesel.

[0030] 2) Mix the emulsion with sludge with a water content of 75%, and stir to obtain a slurry material. The sludge is organic sludge or oily sludge or their mixture, the mass ratio of sludge to emulsion is 4:1, and the viscosity of slurry material is about 30000 centipoise.

[0031] 3) The slurry material is transported to the cement kiln decomposition furnace through the plunger pump for incineration.

Embodiment 3

[0033] A method for co-processing oil depot cleaning waste liquid, which is disposed according to the following steps:

[0034] 1) Add emulsifier op-10 to the oil depot cleaning waste liquid. The amount of emulsifier added is 0.2% of the mass of the oil depot cleaning waste liquid. Stir evenly and let stand to form a stable emulsion. Improve the flash point and reduce the volatility of gasoline and diesel.

[0035] 2) Mix the emulsion with sludge with a water content of 70%, and stir to obtain a slurry material. The sludge is organic sludge or oily sludge or their mixture, the mass ratio of sludge to emulsion is 3:1, and the viscosity of slurry material is about 30000 centipoise.

[0036] 3) The slurry material is transported to the cement kiln decomposition furnace through the plunger pump for incineration.

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Abstract

The invention discloses a co-processing method for oil depot cleaning waste liquor. The co-processing method comprises the following steps of: 1) adding an emulsifier into oil depot cleaning waste liquor, uniformly mixing, and standing, thereby forming a stable emulsified liquid; 2) mixing the emulsified liquid with sludge with moisture content of 65-75%, and mixing to obtain a slurry material, wherein the sludge is organic sludge or oil-containing sludge or a mixture thereof; and 3) conveying the slurry material into a cement kiln decomposition furnace through a plunger pump to perform incineration treatment. According to the co-processing method for the oil depot cleaning waste liquor disclosed by the invention, cement kiln incineration is utilized to perform innocent treatment on sludge and oil depot cleaning waste liquor, so that secondary pollution is not generated, treatment cost is low, process is simple, and stable and industrial production is easily performed. Cement enterprises are distributed over the country, and can be technically improved slightly to meet national co-processing requirements, so that compared with a newly-built common solid waste incineration production line, the co-processing method is lower in cost, is easier to implement, is great in processing amount, is low in energy consumption, is low in cost, and is a more environmentally-friendly processing mode.

Description

technical field [0001] The invention relates to a co-processing method for oil depot cleaning waste liquid, which belongs to the field of three wastes treatment. Background technique [0002] Gas stations and oil depots have a large amount of cleaning waste liquid, which contains a large amount of gasoline and diesel, solvents and cleaning agents. Currently facing the following processing difficulties: [0003] 1. The petroleum and COD in the waste liquid are very high. If it is treated as waste water, the disposal will be difficult and costly. For example, CN105152492A discloses a process and system for treating oily sewage in a product oil depot, the process is complicated and the cost is high. [0004] 2. If it is treated as incineration alone, most of it is water, which consumes a lot of heat, and is technically and costly unfeasible. [0005] 3. It is impossible to landfill the waste liquid. [0006] 4. No recycling value. [0007] In the face of the above disposal...

Claims

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Application Information

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IPC IPC(8): F23G7/04
CPCF23G7/04
Inventor 梁宗唐进张桂罗张雷甘述萍
Owner 重庆利特环保工程有限公司