Resource treatment method of oil-containing sludge

A treatment method and technology of a sewage treatment plant are applied in the field of resource treatment of oily sludge, which can solve the problems of increased sewage discharge burden of enterprises, difficult treatment technology of oily sludge, and complicated equipment, so as to achieve harmless treatment and resource utilization. Chemical utilization, superior solubility, and low energy consumption

Active Publication Date: 2014-04-02
PETROCHINA CO LTD
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  • Application Information

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Problems solved by technology

The harmless resource utilization of waste solids has been listed as an important work content for building a conservation-minded society. According to new regulations and standards, many enterprises are difficult to meet the requirements for the disposal of oily sludge, resulting in increased pollution burden for enterprises and environmental pollution. Prominent hidden danger
[0003] In the past 20 years, although there have been a variety of research reports on oily sludge, and the treatment technologies for oily sludge are also varied, each method has its own advantages and disadvantages and the scope of application. Nowadays, the treatment technology of oily sludge is difficult Be popularized and applied to form industrialized production
At present, the problem of oily sludge treatment has been difficult to solve economically and rationally, and it is often treated by open-air stacking or landfill. These sludges generally contain hydrocarbons, benzene series, phenols, and anthracene, accompanied by stench and Toxicity, if it comes into direct contact with the natural environment, it will cause serious pollution to soil, water and vegetation, and also cause a waste of petroleum resources
This technology uses only one extractant in the extraction process, which has great limitations in compatibility with petroleum substances with complex structures in oily sludge, and the extraction effect is limited.
[0005] CN1O1823824B, CN200910079177.4 proposed that in the oily sludge treatment process, the extractant is C 4 ~C 20 One of the medium hydrocarbons, the compatibility with petroleum substances with complex structures in oily sludge has great limitations, and the extraction effect is limited
[0006] CN1526797A proposes a method for extracting oily sludge. The extraction agent is light coal tar (boiling point 45°C-90°C under normal pressure), petroleum ether, light oil or C 5 , only one extraction agent is used, and the oil extraction is not easy to complete after the oily sludge is extracted
This method has long process flow, complex equipment, harsh operating conditions and high energy consumption.
In addition, some patent documents also involve the treatment of oily sludge, but the oily sludge treatment technologies involved in these patent documents have high energy consumption, complicated process flow, harsh operating conditions, or insufficient treatment of oily sludge. inadequacies of

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  • Resource treatment method of oil-containing sludge

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Experimental program
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Effect test

Embodiment 1

[0040]The solvent formula is as follows: distillate oil with a boiling range of naphtha in the boiling range of 110-125°C is selected as the main agent of the extraction solvent, accounting for 85%; It is a distillate oil at 80-100°C, accounting for 5.0%, forming a composite extractant. After mechanical dehydration, the oily sludge produced by a refinery sewage treatment plant has a water content of 65.0wt% and an oil content of 20.0wt%. The mass ratio of the extractant to the oily sludge is 1:1. The oily sludge is sent to the extraction tank. At 120°C, the pressure is 0.20 MPa and the extractant is mixed for extraction. The extraction time is 20 minutes. After the extraction is completed, the solid-liquid The mixture is sent to the centrifugal separator, the separated liquid phase directly enters the crude oil processing system device, and the solid phase enters the paddle-type sludge dryer, and is dried at a temperature of 180°C and a pressure of 80KPa (absolute pressure) fo...

Embodiment 2

[0044] The solvent formula is as follows: distillate oil with a boiling range of naphtha with a boiling range of 110-125°C is selected as the main agent of the extraction solvent, accounting for 90%; distillate oil with a boiling range of 140-150°C is selected as an auxiliary agent, accounting for 5%; It is a distillate oil at 80-100°C, accounting for 5.0%, forming a composite extractant. The oily sludge produced by a refinery sewage treatment plant has a water content of 75.0wt% and an oil content of 15.0wt% after mechanical dehydration. The mass ratio of the extractant to the oily sludge is 5:1. The oily sludge is sent to the extraction tank. At 140°C, the pressure is 0.40MPa and the extractant is mixed for extraction. The extraction time is 40min. After the extraction is completed, the solid-liquid The mixture is sent to the centrifugal separator, the separated liquid phase directly enters the crude oil processing system device, and the solid phase enters the paddle-type sl...

Embodiment 3

[0048] The solvent formula is as follows: distillate oil with a boiling range of naphtha with a boiling range of 110-125°C is selected as the main agent of the extraction solvent, accounting for 95%; distillate oil with a boiling range of 140-150°C is selected as an auxiliary agent, accounting for 2.5%; It is a distillate oil at 80-100°C, accounting for 2.5%, forming a composite extractant. The oily sludge produced by a refinery sewage treatment plant has a water content of 85.0wt% and an oil content of 9.0wt% after mechanical dehydration. The mass ratio of the extractant to the oily sludge is 15:1. The oily sludge is sent to the extraction tank. At 160°C, the pressure is 0.50 MPa and the extractant is mixed for extraction. The extraction time is 60 minutes. After the extraction is completed, the solid-liquid The mixture is sent to the centrifugal separator, the separated liquid phase directly enters the crude oil processing system device, and the solid phase enters the paddle...

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Abstract

The invention relates to a resource treatment method of oil-containing sludge, and especially discloses a composite extracting agent for treating the oil-containing sludge produced in a wastewater treating process of an oil refinery. Oil-containing sludge having higher water content after centrifugal dehydration is mixed with the composite extracting agent under a condition of higher temperature to destroy a water, oil and solid stabilizing system of the oil-containing sludge, extraction treatment is carried out, the extracted mixture is subjected to solid-liquid separation, the separated solid phase is dried, the formed solid residue is mixed with coal and can be used as fuel of a coal-fired boiler, the separated-out oil and the extracting agent directly go into a crude oil processing system for recycling, and wastewater generated in the process can reach standards after biochemical treatment and is discharged. The treatment method is mainly characterized by having high extracting efficiency, short device procedures, and low equipment investment.

Description

technical field [0001] The invention relates to an extraction treatment method of oily sludge, in particular to a harmless and resourceful treatment process for oily sludge produced by oil refineries and oil refinery sewage treatment plants. Background technique [0002] Refining and chemical enterprises produce a large amount of oily sludge in the process of petroleum refining and wastewater treatment, which mainly come from grease traps, flotation tanks, biologically activated sludge, crude oil dehydration tanks, oil storage tanks and waste oil tanks. These sludges are complex in composition and belong to a relatively stable multi-phase system. They are generally composed of oil-in-water, water-in-oil and suspended solids. They are fully emulsified and have a high viscosity. The solid phase is difficult to settle completely, and the treatment is difficult. At present, in my country's petrochemical industry, an average of 800,000 tons of oily sludge is produced every year. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/00C02F11/12
Inventor 杨岳刘发强刘光利巫树锋李常青江岩王军梁宝锋曹凤霞荣树茂
Owner PETROCHINA CO LTD
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