CN104058526A - Flushing fluid purification treatment process - Google Patents

Flushing fluid purification treatment process Download PDF

Info

Publication number
CN104058526A
CN104058526A CN201410319329.4A CN201410319329A CN104058526A CN 104058526 A CN104058526 A CN 104058526A CN 201410319329 A CN201410319329 A CN 201410319329A CN 104058526 A CN104058526 A CN 104058526A
Authority
CN
China
Prior art keywords
oil
sand
water
well
flushing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201410319329.4A
Other languages
Chinese (zh)
Inventor
周英杰
温志刚
杨卫华
任琦
王刚
孙顶熠
高云娥
余芳
任辉
孔令乐
李庆安
王远
刘胜利
钱哨
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dongying City Hua Feng Environmental Protection Technology Co Ltd
Shengli Oil Field Lu Sheng Oil Development LLC
Original Assignee
Dongying City Hua Feng Environmental Protection Technology Co Ltd
Shengli Oil Field Lu Sheng Oil Development LLC
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dongying City Hua Feng Environmental Protection Technology Co Ltd, Shengli Oil Field Lu Sheng Oil Development LLC filed Critical Dongying City Hua Feng Environmental Protection Technology Co Ltd
Priority to CN201410319329.4A priority Critical patent/CN104058526A/en
Publication of CN104058526A publication Critical patent/CN104058526A/en
Pending legal-status Critical Current

Links

Landscapes

  • Physical Water Treatments (AREA)

Abstract

The invention provides a flushing fluid purification treatment process. The flushing fluid purification treatment process includes the steps that waste water is drained from a well head and firstly enters a sand setting oil separator, so that oil slick and sand are preliminarily removed; sewage drained from the sand setting oil separator is pumped into a cyclone separator, sand and oil dirt are further separated, sewage drained from the cyclone separator is pumped into a buffer tank, substances with opposite charges are added, and then intermediate water is well purified; intermediate water directly enters a filter for filtration; filtered water enters a purification tank for standby; residual well flushing sand cleaning fluid is reinjected or brought back to a working site to continue to be used; solid-liquid separation is conducted on oil dirt and sand, and sand is made into cakes. The flushing fluid purification treatment process has the advantages that the quality of treated water can reach an oil well reinjection water standard, well flushing quality and efficiency are improved, and transport cost is saved.

Description

Flushing fluid purification process technique
Technical field
The present invention relates to a kind of sewage treatment process, especially a kind of oil field flushing liquor treating process.
Background technology
When Oil/gas Well clean-out service, with swiftly flowing liquid, silt is stopped up in shaft bottom and break up, and use the carrying capacity of returning in the circulation of liquid stream, the foundry loam sand breaking up is taken out of to ground and effectively prevented silt blocking hydrocarbon zone, guarantee Oil/gas Well stable yields.
When clean-out service return the husky oil-containing of well liquid band, turbidity is very high, the each well difference of duration of well flushing, several hours at least, more than ten hour at most.Because the each well in oil field disperses, often wash a bite well and must organize many tank cars to draw in clean water, pull out and return well liquid.Sometimes because waterhead area is far away, can affect the continuity of clean-out service.
Existing oil field flushing liquor treating process adopts special well-washing truck, its process using cyclonic separator desanding, again with after strainer oil removal for circulation well cleanup water, water quality can not reach oil field working fluid technological standard.
Summary of the invention
The object of the invention is to avoid prior art and a kind of flushing fluid purification process technique is provided.
Technical scheme of the present invention is: flushing fluid purification process technique, comprise sand setting, micro-electrolysis, dissolved air flotation, frizing, filtering separation, and concrete steps are:
1) first waste water enter sand setting oil trap oil slick and sand grains carried out to preliminary Transformatin from well head is discharged; Sand setting oil trap adopts highly different baffle combination, realizes sand setting step by step, and utilizes profit density difference, and most of oil slick is scraped in sand setting oil trap;
2) pump into cyclone separator from sand setting oil trap sewage out, further separate sand grains and greasy dirt, pump inlet fills 40~80 object filter screens, controls the sand grains particle diameter that enters treatment unit, reduces sand content in water;
3) pump into surge tank from cyclone separator sewage out, add with opposite charges material, make solubilized suspended substance class material in flushing fluid lose relative stability, make its mutual collision and fusion through stirring, reach coagulation, flco increase, the direct bridging of solubilized suspended substance class material in liquid, part silt particle sinks, flco floats to water surface by suspension, and middle water body is purified preferably;
4) in the middle of, water body directly enters strainer filtration;
5) the profit liquid that most silts are removed in step 3) middle and upper part pumps into flotation cell, bottom spirt pressurized air, by the dissolving nozzle in air supporting sedimenting system, Xiang Shuizhong carries a large amount of micro-bubbles, water-insoluble small oil droplet is attached on micro-bubble, increase the buoyancy of small oil droplet, it is floated rapidly, thereby make oil in water emulsion in liquid and the major part of dispersed oil become oil slick, trapped removal by the floating oil collecting device arranging in gas-floating chamber again, bottom water body enters strainer and filters; The frizing blade at flotation cell top scrapes off the oil on liquid level and impurity, finally scrapes into sump;
6) water after filtration enters purification water pool, stand-by; Remain well-flushing sand cleaning fluid re-injection or take back operation field and continue to use; Sump oil silt particle is carried out solid-liquid separation, makes silt particle and becomes cake.
Compared with prior art, advantage of the present invention is: water quality after treatment can reach oil field reinjection water standard, has not only improved well-flushing quality and efficiency, and saves roping cost.
Brief description of the drawings
Fig. 1 is process flow sheet of the present invention.
In figure: 1, sand setting oil trap, 2 is cyclone separator, and 3 is surge tank, and 4 is flotation cell, and 5 is strainer, 6 is purification water pool.
Embodiment
Describe embodiments of the invention in detail below in conjunction with accompanying drawing.
Flushing fluid purification process technique, comprises sand setting, micro-electrolysis, dissolved air flotation, frizing, filtering separation, and concrete steps are:
1) first waste water enter sand setting oil trap 1 oil slick and sand grains carried out to preliminary Transformatin from well head is discharged; Sand setting oil trap 1 adopts highly different baffle combination, realizes sand setting step by step, and utilizes profit density difference, and most of oil slick is scraped in sand setting oil trap 1;
2) pump into cyclone separator 2 from sand setting oil trap 1 sewage out, further separate sand grains and greasy dirt, pump inlet fills 40~80 object filter screens, controls the sand grains particle diameter that enters treatment unit, reduces sand content in water;
3) pump into surge tank 3 from cyclone separator 2 sewage out, add with opposite charges material, make solubilized suspended substance class material in flushing fluid lose relative stability, make its mutual collision and fusion through stirring, reach coagulation, flco increase, the direct bridging of solubilized suspended substance class material in liquid, part silt particle sinks, flco floats to water surface by suspension, and middle water body is purified preferably;
4) in the middle of, water body directly enters strainer 5 and filters;
5) the profit liquid that most silts are removed in step 3) middle and upper part pumps into flotation cell 4, bottom spirt pressurized air, by the dissolving nozzle in air supporting sedimenting system, Xiang Shuizhong carries a large amount of micro-bubbles, water-insoluble small oil droplet is attached on micro-bubble, increase the buoyancy of small oil droplet, it is floated rapidly, thereby make oil in water emulsion in liquid and the major part of dispersed oil become oil slick, trapped removal by the floating oil collecting device arranging in gas-floating chamber again, bottom water body enters strainer 5 and filters; The frizing blade at flotation cell top scrapes off the oil on liquid level and impurity, finally scrapes into sump;
6) water after filtration enters purification water pool 6, stand-by; Remain well-flushing sand cleaning fluid re-injection or take back operation field and continue to use; Sump oil silt particle is carried out solid-liquid separation, makes silt particle and becomes cake.
The present invention is directed to flushing fluid containing abrasive band oil, feature that turbidity is higher, the purification process technique that adopts chemical method and Physical to combine.By adding quantitative flotation agent, according to " coalescence " theory, mainly to use with the group of positive electricity (bearing) property to neutralize in some water and be electrically difficult to some particles that separate or make particle reduce its electromotive force with negative (just), it is played pendulum, and utilize its aggregation property that these particles are concentrated, and separate by method for floating.
Flotation process is mainly divided into 2 types according to the mode and the Air Bubble Size that form bubble in water, i.e. vane type By Bubble-floating Method and injection type gas floating method.The synergistic effect of its two kinds of methods improves decontamination effect improving.
1) vane type By Bubble-floating Method: turbine air flotation method is to rely on the impeller of high speed rotating to produce small bubble.Bubble is formed to returning in well liquid by mechanically mixing, and the residence time is short, and oil removal rate is high, and cost is low, adapts to the variation of water oleaginousness.
2) jet flotation process: jet flotation process is to utilize the principle of squirt pump, adopts and returns well liquid for spraying fluid, in the time that water sprays at a high speed from nozzle, suction chamber at nozzle forms negative pressure, gas is inhaled people's suction chamber, and when water passes through mixing section at a high speed, the gas carrying is sheared into micro bubble; At flotation cell, bubble floating, and be attached on oil droplet and solid particulate, bring it into the water surface.
Flushing fluid processing operation testing data sees the following form
Water quality detection reports the result 1
Water quality detection reports the result 2

Claims (1)

1. flushing fluid purification process technique, comprises sand setting, micro-electrolysis, dissolved air flotation, frizing, filtering separation, it is characterized in that concrete steps are:
1) first waste water enter sand setting oil trap oil slick and sand grains carried out to preliminary Transformatin from well head is discharged; Sand setting oil trap adopts highly different baffle combination, realizes sand setting step by step, and utilizes profit density difference, and most of oil slick is scraped in sand setting oil trap;
2) pump into cyclone separator from sand setting oil trap sewage out, further separate sand grains and greasy dirt, pump inlet fills 40~80 object filter screens, controls the sand grains particle diameter that enters treatment unit, reduces sand content in water;
3) pump into surge tank from cyclone separator sewage out, add with opposite charges material, make solubilized suspended substance class material in flushing fluid lose relative stability, make its mutual collision and fusion through stirring, reach coagulation, flco increase, the direct bridging of solubilized suspended substance class material in liquid, part silt particle sinks, flco floats to water surface by suspension, and middle water body is purified preferably;
4) in the middle of, water body directly enters strainer filtration;
5) the profit liquid that most silts are removed in step 3) middle and upper part pumps into flotation cell, bottom spirt pressurized air, by the dissolving nozzle in air supporting sedimenting system, Xiang Shuizhong carries a large amount of micro-bubbles, water-insoluble small oil droplet is attached on micro-bubble, increase the buoyancy of small oil droplet, it is floated rapidly, thereby make oil in water emulsion in liquid and the major part of dispersed oil become oil slick, trapped removal by the floating oil collecting device arranging in gas-floating chamber again, bottom water body enters strainer and filters; The frizing blade at flotation cell top scrapes off the oil on liquid level and impurity, finally scrapes into sump;
6) water after filtration enters purification water pool, stand-by; Remain well-flushing sand cleaning fluid re-injection or take back operation field and continue to use; Sump oil silt particle is carried out solid-liquid separation, makes silt particle and becomes cake.
CN201410319329.4A 2014-07-07 2014-07-07 Flushing fluid purification treatment process Pending CN104058526A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410319329.4A CN104058526A (en) 2014-07-07 2014-07-07 Flushing fluid purification treatment process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410319329.4A CN104058526A (en) 2014-07-07 2014-07-07 Flushing fluid purification treatment process

Publications (1)

Publication Number Publication Date
CN104058526A true CN104058526A (en) 2014-09-24

Family

ID=51546504

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410319329.4A Pending CN104058526A (en) 2014-07-07 2014-07-07 Flushing fluid purification treatment process

Country Status (1)

Country Link
CN (1) CN104058526A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104998465A (en) * 2015-08-10 2015-10-28 华北理工大学 Hydraulic flushing slime water downhole treatment circulating device
CN107975349A (en) * 2016-10-21 2018-05-01 中国石油化工股份有限公司 Oil field jet flow sand washing de-plugging fracturing wastewater processing unit and method
CN108222867A (en) * 2017-12-06 2018-06-29 王建东 A kind of packaged type flushing fluid purifying processing device
CN108706789A (en) * 2018-05-17 2018-10-26 山西华仕低碳技术研究院有限公司 A kind of coal chemical industrial waste water processing demulsification air-float degreasing device
CN110759588A (en) * 2019-10-14 2020-02-07 石礼军 Oil field well-flushing tank car cleaning tank filters edulcoration equipment
CN113464094A (en) * 2021-08-20 2021-10-01 中国石油化工股份有限公司 Polymer injection well washing device and well washing method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6656251B1 (en) * 1999-07-20 2003-12-02 Abb As Process and a plant for purifying of a liquid
CN101319607A (en) * 2008-07-22 2008-12-10 濮阳市天地人环保工程技术有限公司 Method for no-grounding treatment and comprehensive utilization of oil-gas field downhole operation output solution
CN102807291A (en) * 2011-06-02 2012-12-05 中国科学院生态环境研究中心 Treatment method and equipment for oilfield produced water

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6656251B1 (en) * 1999-07-20 2003-12-02 Abb As Process and a plant for purifying of a liquid
CN101319607A (en) * 2008-07-22 2008-12-10 濮阳市天地人环保工程技术有限公司 Method for no-grounding treatment and comprehensive utilization of oil-gas field downhole operation output solution
CN102807291A (en) * 2011-06-02 2012-12-05 中国科学院生态环境研究中心 Treatment method and equipment for oilfield produced water

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张一等: "采油污水深度处理技术进展", 《广东化工》 *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104998465A (en) * 2015-08-10 2015-10-28 华北理工大学 Hydraulic flushing slime water downhole treatment circulating device
CN107975349A (en) * 2016-10-21 2018-05-01 中国石油化工股份有限公司 Oil field jet flow sand washing de-plugging fracturing wastewater processing unit and method
CN107975349B (en) * 2016-10-21 2023-09-29 中国石油化工股份有限公司 Oil field jet sand-washing blocking-removing operation waste liquid treatment device and method
CN108222867A (en) * 2017-12-06 2018-06-29 王建东 A kind of packaged type flushing fluid purifying processing device
CN108706789A (en) * 2018-05-17 2018-10-26 山西华仕低碳技术研究院有限公司 A kind of coal chemical industrial waste water processing demulsification air-float degreasing device
CN108706789B (en) * 2018-05-17 2020-09-29 山西华仕低碳技术研究院有限公司 Coal chemical wastewater treatment breakdown of emulsion air supporting deoiling device
CN110759588A (en) * 2019-10-14 2020-02-07 石礼军 Oil field well-flushing tank car cleaning tank filters edulcoration equipment
CN113464094A (en) * 2021-08-20 2021-10-01 中国石油化工股份有限公司 Polymer injection well washing device and well washing method

Similar Documents

Publication Publication Date Title
CN104058526A (en) Flushing fluid purification treatment process
JP6309090B2 (en) Pressure levitation device
JPWO2015137484A1 (en) Ultrafine bubble cleaning method using liquid containing ultrafine bubbles, apparatus and pressurized flotation device
CN203754514U (en) Progressive air flotation device
JP6381412B2 (en) Seawater desalination apparatus and method
JPWO2014181583A1 (en) Seawater desalination apparatus and method
CN110078273A (en) A kind of oil field ternary drives and infuses poly- sewage physical processing apparatus and processing method
CN2936380Y (en) Unpowered waste water filtering and sterilizing treating device
JP2001020318A (en) Waters purifying method and waters purifying system and dam soil discharging system
CN110228859A (en) A kind of integrated high efficiency low pollution treatment process suitable for a variety of oily wastewaters
CN103754986B (en) A kind of Oil stain mixture separation system
CN204400653U (en) A kind of integration air-float oil eliminator
CN201070558Y (en) Cavitation air floation device
CN107117763A (en) Oil, water, mud separator
CN212151802U (en) Pretreatment equipment for grinding oil stains and SS in wastewater
CN215365170U (en) Car washing sewage recycling system
CN103086455A (en) Oilfield sewage treatment apparatus
CN205850312U (en) Oil-water separation processing system
JP6496931B2 (en) Processing fluid treatment system
CN208218448U (en) A kind of spraying waste water air-floating processing apparatus
CN113501555A (en) Car washing sewage recycling system
CN209128193U (en) A kind of high speed degreasing unit and rapidly and efficiently oil removing Airfloat filtering pond
CN203890156U (en) Platform sewage purification device
CN207726866U (en) A kind of oil-containing sewage treatment system
CN206308159U (en) A kind of skid-mounted system for oily waste water treatment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20140924