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Fine treatment system suitable for offshore oilfield production water and treatment method thereof

A technology for offshore oil fields and treatment systems, applied in mining wastewater treatment, multi-stage water treatment, water/sewage multi-stage treatment, etc. To achieve the effect of simple operation and maintenance, good impact resistance and small footprint

Pending Publication Date: 2022-05-10
CNOOC ENERGY TECH & SERVICES
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The present invention overcomes the deficiencies in the prior art. The existing offshore oilfield production water membrane treatment process has problems such as rapid decline in membrane flux, high cost, short membrane life, large floor space, complicated maintenance, and poor impact resistance. Provides a fine treatment system and treatment method suitable for production water in offshore oilfields. The invention realizes fine treatment of production water in offshore oilfields, and the production water after treatment can reach the index of reinjection water in low-permeability oilfields

Method used

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  • Fine treatment system suitable for offshore oilfield production water and treatment method thereof
  • Fine treatment system suitable for offshore oilfield production water and treatment method thereof
  • Fine treatment system suitable for offshore oilfield production water and treatment method thereof

Examples

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Effect test

Embodiment 1

[0025] A fine treatment system for offshore oilfield production water, including a water treatment system and a backwash system,

[0026] The water treatment system includes micro-bubble air flotation V1, dual media filter V2, high-speed cyclone filter V3, nano-ceramic fine filter V4 and backwash water separation tank T1. Oilfield production water and nitrogen in the nitrogen tank V5 pass through the air flotation The pump P1 mixes and produces tiny bubbles that enter the micro-bubble air flotation V1 from the water phase inlet of the micro-bubble air flotation V1, and the oil phase separated by the micro-bubble air flotation V1 flows into the backwash water separation from the oil phase outlet of the micro-bubble air flotation V1 In the tank T1, the gas separated from the microbubble air flotation V1 is discharged from the gas phase outlet of the microbubble air flotation V1 through the venting system V6, and the water phase separated from the microbubble air flotation V1 is i...

Embodiment 2

[0029] On the basis of Example 1, the micro-bubble air flotation V1 is arranged in a vertical container structure, and the micro-bubble air flotation V1 is generated by a multiphase flow dissolved air pump. The micro-bubble air flotation V1 can reduce the oil content in the oilfield production water to 30% -60mg / L; reduce suspended solids in oilfield production water to 20-50mg / L.

[0030] In the dual-media filter V2, the filter medium is quartz sand and anthracite, the oil content in the water discharged from the dual-media filter V2 is reduced to 10-20mg / L, and the suspended solids in the discharged water are reduced to 10-20mg / L.

[0031] In the high-speed cyclone filter V3, the filter medium is made of aluminum silicate particles, and the filter adopts a tangential water inlet method. The filtration rate is 2-3 times that of the ordinary filter. The content is reduced to 6-10mg / L, the suspended matter content in the discharged water is 2-5mg / L, and the median particle size...

Embodiment 3

[0033]On the basis of Example 2, in the nano-ceramic fine filter V4, the filter medium adopts modified porous nano-ceramic particles, the filter medium adopts the method of random packing, the filter adopts the tangential swirl water inlet method, and the nano-ceramic fine The oil content in the water discharged from the filter V4 is reduced to 3-6mg / L, the suspended matter content in the discharged water is 0.4-1.5mg / L, and the median particle size is 0.8-1.3μm.

[0034] The backwash water separation tank T1 adopts an upper and lower combined structure. The upper part of the backwash water separation tank T1 adopts a corrugated plate packing structure to separate larger solid particles in the water. The lower part of the backwash water separation tank T1 adopts a floating oil collector to collect Oil slick in water.

[0035] The sludge dewatering device T2 adopts a decanter centrifuge, and the moisture content of the sludge after being treated by the sludge dewatering device ...

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Abstract

The invention provides a fine treatment system suitable for offshore oilfield production water and a treatment method thereof. The oilfield production water and nitrogen in a nitrogen tank are mixed through an air floatation pump to generate micro bubbles which enter a micro-bubble air floatation device from a water phase inlet of the micro-bubble air floatation device; an oil phase separated by the micro-bubble air floatation flows into a backwashing water separation tank from an oil phase outlet of the micro-bubble air floatation, gas separated by the micro-bubble air floatation is discharged from a gas phase outlet of the micro-bubble air floatation through an emptying system, and a water phase separated by the micro-bubble air floatation is pressurized by a booster pump from a water phase outlet of the micro-bubble air floatation; after the water phase sequentially enters the double-medium filter, the high-speed cyclone filter and the nano ceramic fine filter, part of suspended solids and oil drops in the water phase are filtered and removed, and the treated water phase enters the buffer tank to be stored. According to the invention, fine treatment of the production water in the offshore oilfield is realized, and the treated production water can reach the reinjection water index of the low-permeability oilfield.

Description

technical field [0001] The invention relates to the technical field of oily sewage treatment, and more specifically relates to a fine treatment system and treatment method suitable for offshore oilfield production water. Background technique [0002] With the increase of the production life of oilfields, some oilfields have entered the medium-high water-cut production period, and the production water treatment volume has increased year by year. Waterflooding is a key technology to maintain reservoir energy, and has achieved obvious economic benefits. According to "Recommended Injection Water Quality Index and Analysis Method for Clastic Reservoirs SY / T 5329-2012", the current average air permeability of the injection layer is >0.05μ㎡, and the water quality control index can be achieved by using traditional water treatment processes. [0003] The average air permeability of the injection layer is less than or equal to 0.05μ㎡, and the water quality control index can only b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/02C02F11/127C02F103/10
CPCC02F9/00C02F11/127C02F2103/10C02F1/24C02F1/001C02F1/38C02F2301/08C02F1/40
Inventor 李永丰孔德钰张绪强范琳波牟楠刘权升卢大艳张金鹏白俊陈飞
Owner CNOOC ENERGY TECH & SERVICES