Treatment process of oil-containing sewage in low-permeability oil field

A treatment process and technology for oily sewage, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, mining wastewater treatment, etc. Pollution and other problems, to achieve the effect of chemical cleaning cycle and service life extension, easy on-site management, and reducing the degree of pollution

Active Publication Date: 2012-03-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] First, ordinary physical and chemical processes cannot effectively remove emulsified oil and organic matter. After fiber balls and fiber bundles are polluted by oil and organic matter, regeneration is difficult and the service life is short
[0006] Second, in the biological method + ultrafiltration membrane process, although the free oil, emulsified oil and other organic matter in the oily sewage are effectively removed by microorganisms, which reduces the pollution of the oil to the ultrafiltration membrane, the microorganisms produce a large amount of extracellular Polymers can seriously foul UF membranes
This method has the following disadvantages: ①Use a large amount of coagulant or coagulant, which increases the amount of oily sludge; ②Although microorganisms can effectively degrade crude oil, the extracellular polymer produced by microorganisms has not been effectively removed, which will cause Ultrafiltration membranes cause serious fouling, making membrane regeneration difficult
This method has the following disadvantages: ①The treatment process is too long, and the one-time investment in water treatment is high; ②The coalescence degreasing method can only remove part of the emulsified oil; Membrane causes severe fouling, making membrane regeneration difficult
This method has the following deficiencies: ①The treatment time of oily sewage by the biological pool is too short (3.5h), the oil content in the sewage cannot be effectively removed, which will cause blockage of the filter material of the biofilter; ②Extracellular polymers produced by microorganisms are not obtained Effective removal will also cause pollution and blockage to the filter material of the biofilter and the hollow fiber ultrafiltration membrane at the back end; ③The filter material of the biofilter needs to be backwashed frequently, the workload of flushing and maintenance is heavy, and it is difficult to replace and manage the filter material; ④The patent does not explain the cleaning cycle of the filter material of the biofilter and the pollution of the filter material; ⑤The above methods have no industrial application reports in the field of oilfield sewage treatment

Method used

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  • Treatment process of oil-containing sewage in low-permeability oil field
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  • Treatment process of oil-containing sewage in low-permeability oil field

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Experimental program
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Effect test

Embodiment 1

[0027] Such as figure 1 Shown is the flowchart of the present invention. Using a low-permeability oilfield oily sewage treatment process method of the present invention to carry out oily sewage treatment, the steps are as follows:

[0028] step 1)

[0029] Pretreatment: The oily sewage from the formation first enters the pretreatment tank, the oil content in the oily sewage is ≤300 mg / L, and the sulfide content is ≤50 mg / L. Air aeration devices are installed at the bottom of the pretreatment tank to The influent is aerated, the air-water ratio is 10:1, and the residence time is about 0.5h, so that the sulfides in the oily sewage are fully oxidized. The residence time can be appropriately extended, and the oily sewage with low sulfur content The residence time is short, and the oily sewage with high sulfur content stays for a long time; the purpose of pretreatment is to fully oxidize the reducing sulfide in the oily sewage, which can reduce the impact of sulfide and other red...

Embodiment 2

[0040] On-site application of a sewage treatment station in an oil field, with a daily sewage treatment volume of 500m 3 / d; Utilize the low-permeability oil field oily sewage treatment process method of the present invention, process according to the following steps:

[0041] step 1)

[0042] Pretreatment: The oily sewage from the formation first enters the pretreatment tank, and an air aeration device is installed at the bottom of the pretreatment tank to aerate the incoming water to fully oxidize the sulfide in the oily sewage; the pretreated The purpose is to oxidize the reducing sulfide in the oily sewage, which can reduce the inhibition of sulfide and other reducing substances on the metabolic activity of microorganisms in the degreasing bacteria agent, and ensure that the degradation effect of microorganisms on crude oil and other organic substances will not be reduced; At the same time, part of the slick oil is removed by flotation in the pretreatment tank;

[0043] ...

Embodiment 3

[0056] The invention discloses a low-permeability oilfield oily sewage treatment process, which treats the sewage contained in a certain sewage treatment station in the oilfield, and the daily sewage treatment volume is 240m 3 / d; the working temperature of the system is 20-35°C; the pH is 6-9, and the processing mainly includes the following steps:

[0057] step 1)

[0058] Pretreatment: The oily sewage from the formation first enters the pretreatment tank, and an air aeration device is installed at the bottom of the pretreatment tank to aerate the incoming water to fully oxidize the sulfide in the oily sewage; the pretreated The purpose is to oxidize the reducing sulfide in the oily sewage, which can reduce the inhibition of sulfide and other reducing substances on the metabolic activity of microorganisms in the degreasing bacteria agent, and ensure that the degradation effect of microorganisms on crude oil and other organic substances will not be reduced; At the same time,...

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Abstract

The invention discloses a treatment process of oil-containing sewage in a low-permeability oil field in the technical field of petroleum exploitation. The process comprises the following steps: firstly, carrying out aeration pretreatment to remove sulfide in the oil-containing sewage; then, entering a biological contact oxidation system to degrade crude oil in the oil-containing sewage, wherein the biological contact oxidation system comprises at least two stages of biochemical pools which are connected in series, the biochemical pool is provided with a hydrophilic combined filling material, and the pool bottom of the biochemical pool is provided with an air aeration device; putting an oil-removing microorganism agent in an initial stage of starting in the biochemical pool, and then carrying out efficient aeration sedimentation treatment on extracellular polymers and other biochemically degradable organic substances; and finally, treating by an ultrafiltration membrane filtration system and then injecting into a water tank. The process has the characteristics of small system sludge amount, less oil content in sewage at the membrane inlet, little ultrafiltration membrane pollution,stable membrane flux and long chemical cleaning period of ultrafiltration membrane, and the quality of water at the water outlet of the system reaches the grade A water quality standard of the low-permeability oil field.

Description

technical field [0001] The invention relates to a sewage treatment method, in particular to a treatment method for oily sewage in an oil field. Background technique [0002] Low-permeability oilfields have the characteristics of small reservoir pores, thin throats, high seepage resistance, and poor conductivity, so they have higher requirements for injected water. The Petroleum and Natural Gas Industry Standard SY / T 5329-94 of the People's Republic of China "Recommended Indicators and Analysis Methods for Injection Water Quality in Clastic Reservoirs" stipulates that the suspended solids content in injection water for low-permeability oilfields should be less than 3mg / l, and the median particle size of suspended solids should be less than 3×10 ~3 mm, oil content <8mg / l. [0003] At present, the oil field mainly adopts gravity deoiling + coagulation + coarse filtration + fine filtration process, pressure deoiling (swirl flow, coarse granulation) + coagulation + coarse fi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F103/10
Inventor 薛芸罗江涛徐卫华王彪杨帆庄建全姚峰雷世华
Owner CHINA PETROLEUM & CHEM CORP
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