CN1724422A - Process of flowing multistage chemical thermo-dynamic for cleaning mud oil-containing - Google Patents

Process of flowing multistage chemical thermo-dynamic for cleaning mud oil-containing Download PDF

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CN1724422A
CN1724422A CNA2005100466271A CN200510046627A CN1724422A CN 1724422 A CN1724422 A CN 1724422A CN A2005100466271 A CNA2005100466271 A CN A2005100466271A CN 200510046627 A CN200510046627 A CN 200510046627A CN 1724422 A CN1724422 A CN 1724422A
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water
oil
washing trough
oily sludge
charging
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CNA2005100466271A
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CN1304309C (en
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王栋
林海英
曾宏德
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大连理工大学
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Abstract

A flowing-type multi-stage chemicothermal method for reclaiming the oily sludge includes such steps as pre-treating by flushing the oily sludge with high-pressure circulating hot water to fluidize it, washing in the serially connected multiple washing pools containing different chemicals, and water treating to recover crude oil.

Description

Process of flowing multistage chemical thermo-dynamic for cleaning mud oil-containing
Technical field
The present invention relates to a kind of at the crude oil recovery of oily sludge, the comprehensive processing technological process of environment protection.
Background technology
Oil field, petroleum refinery's oil movement and storage system be normal to produce and lands greasy filth, the heavy mud in jar end, and refinery factory oil-containing " three mud (oil trap bed mud, dissolved air floatation scum silica frost and accident are revealed sump oil) " etc., and they are referred to as oily sludge.Material foul smellings such as the benzene series thing that contains in these mud, phenols, anthracene flavor and toxicity if directly enter in the physical environment, can cause bigger pollution to surrounding soil, water body and vegetation, have also wasted a large amount of petroleum resources simultaneously.Therefore, no matter be to consider from environment protection or from the angle that reclaims the energy, all must handle oily sludge.But the character of oily sludge is special, and it deals carefully with the disposal technology difficulty big, and the cost height is the environmental protection difficult problem of the domestic and international oil refining industry of puzzlement always.
Oily sludge, composition are extremely complicated, and character has nothing in common with each other, so treatment process also is not quite similar.Tradition greasy filth tupe is: mud modulation-centrifuge dehydration-burning, more French, German petroleum chemical enterprise adopts the mode of burning, lime-ash to be used to repair the roads or imbeds specified lime-ash landfill yard, burns the heat energy that produces and is used for the heat supply generating.At home, what most refinery adopted is burning disposal, as the downflow system rotary incinerator of Jingmen, Hubei petrochemical plant, the employing of Chang Ling petrochemical plant, the fluidized bed incinerator that Yanshan Petrochemical adopts, oily sludge is after burning disposal, and multiple harmful substances is almost all removed, and is respond well; But sludge incineration needs a large amount of diesel oil or sump oil, and heat is not mostly recycled again, and cost is very high, invest also big, in addition in the burning process with serious atmospheric pollution, what have also has a large amount of dusts, the practical efficiency of incinerator is very low.Up to the present, domestic oil field is to the processing of greasy filth and utilize and still be in test and conceptual phase, does not still have technology, technology is reliable, the processing of stable equipment operation with utilize demonstration project.
From the mid-80, developed country such as the U.S., Japan etc. begin to carry out the mud shunting, pay attention to the research efficient low-consume and handle the method and the technology of greasy filth, use composite treatment process such as solvent extraction, hot wash, ultrasonic wave oil removing, thermal desorption to obtain application.Use pyrogen oil flushing jar bed muds to distill again to handle to reach clearly as United States Patent (USP) 6673231 introduction and jar handle two aspect purposes with greasy filth, but because the application places of a large amount of pyrogen oil of arts demand restriction technology, in addition China at present each refinery use to such an extent that distillation tower can not satisfy processing requirement, so this patented technology and be not suitable for China.World patent 92/04424 is introduced and is adopted a series of vaporization/condensation art breading greasy filth for another example, is not suitable for to handle the high greasy filth of oleaginousness.Comprise distillation, complex apparatus such as centrifugal in the technology, technical requirements precision height, the cost of investment of once going is big.Therefore composite treatment process is progressively perfect compared with its treatment facility of centrifuge dehydration separation method and facility, and the energy consumption for the treatment of processes and expense progressively descend and the processing efficiency height, and it is thorough to reclaim resource.As technologies such as ultrasonic wave, thermal desorption reclaim resource more than 99%.But complicated along with treatment process, the raising of automation degree of equipment, construction costs rises significantly, and a lot of methods are not suitable for China's national situation.
Advantages such as it is strong to use the hot water wash separating technology to have a handiness compared with traditional mode, and it is more thorough to reclaim resource, and disposable treatment capacity is big, and strong to the adaptability of raw material, can remedy jar strong shortcoming of bed mud timeliness effectively.Than at present emerging as thermal desorption technology, solvent extraction technology and microwave demulsifying centrifugal separation technique etc., cost investment reduces greatly, and treatment effect also can meet the demands, and every index all can be up to state standards, and technical feasibility is strong.States such as American and Britain, Holland, Canada report useful 70 ℃ thermokalite water and washing composition repetitive scrubbing, be under 2 the condition at liquid-solid ratio, behind the washing 20min, can be with oil-contg 30.0% oily sludge to be washed till residual oil content be 0.3%, again solid is cured landfill after the centrifuge dehydration.But abroad this technology only has been used for handling and has landed greasy filth and oily sediment, and selecting for use of centrifugation apparatus not only improved the cost of handling, and has strengthened power consumption, has also lowered operation stability of equipment simultaneously.
Summary of the invention
The object of the present invention is to provide a kind of economy, process for treating oil-containing sludge effective, applied widely.Adopt chemical heat to wash the stage trapping process synthesis and handle oily sludge (be mainly land greasy filth, jar bed mud and scum silica frost), reach crude oil recovery, the innoxious two aspect purposes of surflaes
Process of flowing multistage chemical thermo-dynamic for cleaning mud oil-containing of the present invention is to adopt chemical agent heat to wash stage trapping comprehensive treating process oily sludge, and whole process technology scheme (seeing accompanying drawing 1) is made up of pretreating zone A, cleaning area B and water treatment zone C; Be provided with raw material storage tank (1), grid (2), transferpump (5) muddy water mixing tank (6), homogenizer (7) and valve (8) in the pretreating zone; Cleaning area has chemicals dosing plant (9), first washing trough (10), spiral heater (11), second washing trough (12), medial launder (13), the 3rd washing trough (14) and oil storage vessel (20); Water treatment zone is provided with pressurized dissolved air flotation device (15) and high-pressure pump (16); The comprehensive processing technique flow process is: at first the oily sludge raw material (3) in the storage tank (1) is fed to above the chain-belt type Movable grid (2) by crawler-tread, experience circulation high-pressure water heating and small amount of supplemental water (4) were with 5~10m/s flow velocity strong flushing 5 minutes, raw material and water ratio are 1: 3~8, fluidised profit mud mixture is delivered to muddy water mixing tank (6) from the grid bottom by transferpump (5), stir 5~10min through brute force, mix, bottom deposit mud is sent raw material tank (1) back to by pump (5), and the top oil-water mixture enters cleaning area through valve (8) gravity flow; Mixture at first enters first washing trough (10), be heated to 60 ℃~90 ℃ by spiral heater (11), add emulsion splitter DL from chemicals dosing plant (9), stir 10~20min by pump (5) circulation hydraulic, the overflow water outlet enters second washing trough (12) through valve, dosing again, gravity settling 20~40min, mixture are divided into three layers in groove, the top oil reservoir is scraped to storage tank (20) by Oil scraper, middle water layer gravity flow enters medial launder (13), the heavy mud in bottom is also delivered to medial launder by pumping, and the water purification that muddy water two-phase and follow-up water treatment zone reflux adds clean-out system or flocculation agent after medial launder mixes, stir 5~10min, water outlet is by being pumped to the 3rd washing trough (14), and layering behind gravity settling 20~40min scrapes the top oil slick together with the fuel-displaced storage tank (20) that enters of second washing trough, bed mud (18) scrapes makes further to dispose final qualified discharge; The middle water layer overflow of the 3rd washing trough (14) enters clean water area pressurized dissolved air flotation device (15), flotation removes deoils and a small amount of suspended substance, and partially purifying water is back to medial launder, and part is delivered to technology through high-pressure pump (16) and washes raw material foremost, if system's water yield is bigger, efflux part water outlet (17).
A.. pretreating zone:
The semi-underground storage of raw material tank position coagulation structure time pond, the edge marks the grid area by baffle plate, and the top, grid area is provided with the chain-belt type Movable grid, and the grid both sides are installed and are put the baffle plate that leaks hunting.Raw material is delivered on the grid through the crawler belt feed system, and the strong flushing of experience cyclicity high-pressure water heating plays and peels off fine particle and make it fluidization and clean bulk solid thing such as cloth and stone etc.Through mechanical tourniquet tool dehydration, ultimate disposal is done in the homologous ray mud extraction to raw material again on the grid; Fluidised mixture directly enters the muddy water mixing tank with slush pump at the bottom of the grid.The muddy water mixing tank is the steel construction tank arrangement that designs voluntarily, and agitator adopts double-layer paddle, high-speed stirring.The heavy mud in bottom can guarantee the thorough mixing of raw material and water by blowback to the grid area.
B. cleaning area:
First washing trough is steel matter body structure, the dosing of washing trough top, when charging when landing greasy filth, regulating the pH value is 7~9, water temperature is 60 ℃~70 ℃; When charging was scum silica frost, dosing was emulsion splitter DL-100100ppm~500ppm, and the pH value is 4~6, and water temperature is 60 ℃~70 ℃; When charging was the jar bed mud, dosing was emulsion splitter DL-4020 100~200ppm, and the pH value is 8~11, and water temperature is 70 ℃~90 ℃.Concrete processing parameter is decided on charging oil length size.For guaranteeing raw material and medicament thorough mixing, establish two rectification walls in the groove respectively, perforate φ 100mm, pitch of holes 300mm, spiral heater is established in the stage casing; Using waterpower to stir flow velocity is 3~5m/h.; End is established overflow weir, the overflow water outlet.
The second washing trough steel matter body structure is established Oil scraper and bucket.Ingress establishes chemicals dosing plant, and regulating the pH value when charging when landing greasy filth is 7~8; Regulating the pH value when charging during for scum silica frost is 7~8; When charging is the jar bed mud, regulate pH value=7~8, leave standstill gravity separation, end is established the overflow weir water outlet.
Medial launder is a concrete structure, stir to adopt two blade agitators, the import dosing, when charging when landing greasy filth, add AEO-9 0~5000ppm; When charging is scum silica frost, addition polymerization iron 100~500ppm, CPAM (molecular weight is more than 1,000,000 grades) 10~50ppm; When charging is the jar bed mud, add AEO-9 2000~5000ppm, discharging is delivered to the 3rd washing trough by slush pump.
The 3rd washing trough is a steel matter body structure, constructs similar to two washing troughs.Do not establish chemicals dosing plant.Profit mud is three phase separation in the 3rd washing trough, and the upper strata oil slick is with the fuel-displaced storage tank of delivering to jointly of second washing trough, and the fuel-displaced refinery that can directly enter recycles; Middle water layer enters the water purification unit; The ultimate disposal of bed mud is looked the difference of discharging character and difference, and being unearthed of greasy filth of landing generally speaking meets the pollutant emission standard of country fully, can be used as the pure land and directly discharges.Being unearthed of jar bed mud and scum silica frost can be burned or brickmaking.
C. clean water area:
Clean water area adopts the pressurized dissolved air flotation method to separate for water, adds water conditioner in case of necessity, and main purpose guarantees the normal operation of cleaning for removing excessive oil slick and impurity in the water.Recirculated water is delivered to origin or beginning through high-pressure pump, and high flow rate is provided, and is finished by many rows nozzle the brute force of raw material on the grid is impacted.
This process characteristic:
1. pretreating zone adopts cycle of higher pressure hot water injection raw material, can reach raw material crushing and fluidization two aspect purposes simultaneously.Adopt the pump circulation not only can guarantee the charging thorough mixing between raw material storage tank and muddy water blend tank, and be difficult for producing silting, the trouble of having exempted flush pot in the blend tank.
2. at cleaning area, the most of employing of technology flow automatically, and alleviated power consumption.Adopt overflow to carry between each washing trough, make that mutual material balance is more or less freely, the coupled processing range of flow process is bigger.The setting of multiple-grooved makes the processing power of this method and the adaptability of former mud change is enhanced in cleaning process.As saving medial launder and three-flute when the slight oily sludge; When the former mud of severe oil-containing and medium size-grade distribution complexity, then give full play to the grading of two grooves and the rinse action of three-flute makes mud obtain mutually purifying more completely.
3. because water adopts Recycle design, the operating mass of system will be weighed and be regulated by the oil-containing situation of the pure land.The oil content of circulation aqueous phase then can be retained in certain degree.So just avoided requirement to water treatment.If when the process feeds water ratio was higher, the unnecessary waste water of generation was incorporated consideration into original water processing establishment, handles together.
4. the inorganic salt enrichment that causes of the circulation of water is that majority helps the generation of bubble and separating of oil phase from liquid phase chemical character.Some inorganic salt may be beneficial to the emulsification of crude oil, but under the mode that recycles, then become the favorable factor that purifies the mud phase.This also is one of this technological design water round-robin reason.
Description of drawings
Shown in the accompanying drawing 1
1-raw material storage tank, 2-grid, the charging of 3-greasy filth, 4-make up water, the 5-transferpump, 6-muddy water mixing tank, 7-homogenizer, 8-valve, the 9-chemicals dosing plant, 10-first washing trough, 11-spiral heater, 12-second washing trough, 13-medial launder, 14-the 3rd washing trough, 15-pressurized dissolved air flotation device, 16-high-pressure pump, the outer draining of 17-, the outer spoil disposal of 18-, the outer oil extraction of 19-, 20-storage tank
Embodiment
Embodiment 1
Land the greasy filth cleaning experiment
The greasy filth that lands is taken from the Liaohe Oil Field refinery, and normal temperature is black solid, interior oil-containing, silt, water etc. down.
Get 100g and land greasy filth water ratio 4.8%, oil content 15.22%, ash content 79.98% (mean value) is in 2 liters of beakers, add warm water 500ml, regulate pH value=9, insert behind the powerful stirring 10min leave standstill 30min in 60 ℃ of water-baths after, put into thermal protective aid, scrape the upper strata oil slick, regulate aqueous pH values=7, leave standstill 30min after 100g/l AEO-94ml stirs 5min to wherein adding.Scrape the upper strata oil slick and mix back its moisture of mensuration and foreign matter content, survey the oil length of bed mud in scraping for the first time thing.
Upper strata oil slick: 21.55g water ratio 38.12% oil length 61.07% impurity 0.81%
Bed mud: 96.42g water ratio 28.85% oil length 0.58% ash content 70.57%
Oil recovery rate 86.47% cleaning rate 96.33% Residual oil leaching yield is below 5%
Embodiment 2
The scum silica frost cleaning experiment
Scum silica frost is the scum silica frost of the generation in oil refining and the sewage purification process from certain waste oil regeneration company.Normal temperature for liquid, includes oil, emulsification, water and small amount of chemical substances down.
Get 100g scum silica frost water ratio 70.04%, oil content 8.29%, ash content 21.67% (mean value) is in 2 liters of beakers, add warm water 300ml, regulate pH value=5, add emulsion splitter DL-100 200ppm, powerful stir insert behind the 5min leave standstill 30min in 60 ℃ of water-baths after, put into thermal protective aid, scrape the upper strata oil slick and measure its foreign matter content, regulate aqueous pH values=7, to wherein adding the poly-iron 5ml of 10g/L, 1g/L CPAM (molecular weight 6,000,000) 2ml stirs and to leave standstill 30min. behind the 5min and scrape the upper strata oil slick and measure its foreign matter content, surveys the oil length of bed mud.
Upper strata oil slick: 9.24g water ratio 46.03% oil length 51.42% impurity 2.55%
Bed mud: 37.47g water ratio 42.15% oil length 1.20% ash content 56.65%
Oil recovery rate: 57.31% cleaning rate, 94.58% Residual oil leaching yield is below 3%
Embodiment 3
Jar bed mud cleaning experiment
Jar bed mud from certain waste oil regeneration company mooring bilge and storage tank at the bottom of clear jar oily rubbish.Normal temperature for the chocolate semisolid, includes oil, silt, iron rust, water and impurity down.
Get 100g jar bed mud water ratio 7.70%, oil content 78.75%, ash content 13.55% (mean value) add warm water 800ml in 2 liters of beakers, add emulsion splitter DL-4020 100ppm, regulate pH value=11, insert behind the powerful stirring 5min leave standstill 30min in 60 ℃ of water-baths after, put into thermal protective aid, scrape the upper strata oil slick and measure its foreign matter content, regulate aqueous pH values=7, after wherein add 100g/L AEO-9 1ml, stirring 5min, leave standstill 30min.Scrape the upper strata oil slick and measure its foreign matter content, survey the oil length of bed mud.
Upper strata oil slick: 79.46g water ratio 12.31% oil length 86.75% impurity 0.94%
Bed mud: 26.78g water ratio 16.59% oil length 35.79% ash content 47.62%
Oil recovery rate: 87.53% cleaning rate, 87.83% Residual oil leaching yield is below 5%
Embodiment 4
The present invention trys out in certain waste oil regeneration company, and every technic index all produces a desired effect.
1. basic data
Handling total amount is 20 ton per days, by 10 hours the working hour/day operation, designed capacity estimates that the processing volume is 20 cubic metres/day for 2 tons/hour, amounts to 2.0 cubic metres/hour
2. feedstock property
(1) the refinery scum silica frost is 5,000 tons/year.
(2) jar bed mud is 1,000 ton/year.
(3) land 1,000 ton/year in greasy filth.
3. processing parameter
(1) landing greasy filth handles (seeing Table 1)
(1) grid spacing 15mm, 2.0 tons/hour of chargings, high pressure water 7m/s, material-water ratio are 1: 5;
(2) muddy water mixing column: churning time is 5 minutes, 12 tons/hour of treatment capacities
(3) first washing troughs: 30 minutes residence time, 12 tons/hour of treatment capacities; 50 ℃~60 ℃ of temperature, pH value 8~9, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa
(4) second washing troughs: 40 minutes residence time, 12 tons/hour of treatment capacities; PH value 7~8, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa
(5) medial launder: churning time 5min, AEO-9 dosage 4%, the concentration 10% of making up a prescription, time of compounding 1d, dosing pressure 0.3Mpa
(6) the 3rd washing troughs: residence time 40min, 15 tons/hour of treatment capacities
(7) air-floating apparatus: residence time 10min, 15 tons/hour of treatment capacities
(2) scum silica frost is handled (seeing Table 2)
(1) grid spacing 15mm, 3.0 tons/hour of chargings, high pressure water 7m/s, material-water ratio are 1: 3;
(2) muddy water mixing column: churning time is 5 minutes, 12 tons/hour of treatment capacities
(3) first washing troughs: 30 minutes residence time, 12 tons/hour of treatment capacities; 60 ℃~70 ℃ of temperature, pH value 3~5, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa; Emulsion splitter DL-100 dosage 2%, the concentration 1% of making up a prescription, time of compounding 1d, dosing pressure 0.3Mpa
(4) second washing troughs: 40 minutes residence time, 12 tons/hour of treatment capacities; PH value 7~8, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa
(5) medial launder: churning time 5min, poly-iron dosage 5%, the concentration 10% of making up a prescription, time of compounding 5h, dosing pressure 0.4Mpa; CPAM (molecular weight 6,000,000) dosage 1%, the concentration 0.1% of making up a prescription, time of compounding 5h, dosing pressure 0.4Mpa
(6) the 3rd washing troughs: residence time 40min, 15 tons/hour of treatment capacities
(7) air-floating apparatus: residence time 10min, 15 tons/hour of treatment capacities
(3) jar bed mud is handled (seeing Table 3)
(1) grid spacing 15mm, 1.3 tons/hour of chargings, high pressure water 8m/s, material-water ratio are 1: 8;
(2) muddy water mixing column: churning time is 5 minutes, 12 tons/hour of treatment capacities
(3) first washing troughs: 30 minutes residence time, 12 tons/hour of treatment capacities; 80 ℃~90 ℃ of temperature, pH value 9~11, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa; Emulsion splitter DL-4020 dosage 1%, the concentration 1% of making up a prescription, time of compounding 1d, dosing pressure 0.3Mpa
(4) second washing troughs: 40 minutes residence time, 12 tons/hour of treatment capacities; PH value 7~8, pH regulator agent time of compounding 30min, dosing pressure: 0.2Mpa
(5) medial launder: churning time 5min, AEO-9 dosage 1%, the concentration 1% of making up a prescription, time of compounding 1d, dosing pressure 0.3Mpa;
(6) the 3rd washing troughs: residence time 40min, 15 tons/hour of treatment capacities
(7) air-floating apparatus: residence time 10min, 15 tons/hour of treatment capacities
Each segment process technical indicator actual measurement table
Table 1. lands oil soil treatment technique index (mean value)
Table 2. scum silica frost treatment process index (mean value)
Oil length ??8.3% ??55.3% ??0.8% ??46.5% ??0.6% ??≤800mg/L ??≤100mg/L
Water ratio ??70.0% ??41.7% ??67.6% ??49.2% ??46.9% ??- ??-
Foreign matter content ??21.7% ??3.1% ??31.6% ??4.3% ??52.6% ??- ??-
??COD ??- ??- ??- ??- ??- ??≤700mg/L ??≤200mg/L
Suspended substance ??- ??- ??- ??- ??- ??≤80mg/L ??≤10mg/L
Table 3. jar bed mud treatment process index (mean value)

Claims (5)

1. the integrated conduct method of an oily sludge is characterized in that this method is to adopt chemical agent heat to wash stage trapping comprehensive treating process oily sludge, and whole technological process is made up of pretreating zone A, cleaning area B and water treatment zone C; Be provided with raw material storage tank (1), grid (2), transferpump (5) muddy water mixing tank (6), homogenizer (7) and valve (8) in the pretreating zone; Cleaning area has chemicals dosing plant (9), first washing trough (10), spiral heater (11), second washing trough (12), medial launder (13), the 3rd washing trough (14) and oil storage vessel (20); Water treatment zone is provided with pressurized dissolved air flotation device (15) and high-pressure pump (16); The comprehensive processing technique flow process is: at first the oily sludge raw material (3) in the storage tank (1) is fed to above the chain-belt type Movable grid (2) by crawler-tread, experience circulation high-pressure water heating and small amount of supplemental water (4) were with 5~10m/s flow velocity strong flushing 5 minutes, raw material and water ratio are 1: 3~8, fluidised profit mud mixture is delivered to muddy water mixing tank (6) from the grid bottom by transferpump (5), stir 5~10min through brute force, mix, bottom deposit mud is sent raw material tank (1) back to by pump (5), and the top oil-water mixture enters cleaning area through valve (8) gravity flow; Mixture at first enters first washing trough (10), be heated to 60 ℃~90 ℃ by spiral heater (11), add emulsion splitter DL from chemicals dosing plant (9), stir 10~20min by pump (5) circulation hydraulic, the overflow water outlet enters second washing trough (12) through valve, dosing again, gravity settling 20~40min, mixture are divided into three layers in groove, the top oil reservoir is scraped to storage tank (20) by Oil scraper, middle water layer gravity flow enters medial launder (13), the heavy mud in bottom is also delivered to medial launder by pumping, and the water purification that muddy water two-phase and follow-up water treatment zone reflux adds clean-out system or flocculation agent after medial launder mixes, stir 5~10min, water outlet is by being pumped to the 3rd washing trough (14), and layering behind gravity settling 20~40min scrapes the top oil slick together with the fuel-displaced storage tank (20) that enters of second washing trough, bed mud (18) scrapes makes further to dispose final qualified discharge; The middle water layer overflow of the 3rd washing trough (14) enters clean water area pressurized dissolved air flotation device (15), flotation removes deoils and a small amount of suspended substance, and partially purifying water is back to medial launder, and part is delivered to technology through high-pressure pump (16) and washes raw material foremost, if system's water yield is bigger, efflux part water outlet (17).
2. according to the integrated conduct method of the described oily sludge of claim 1, it is characterized in that present method is applicable to that the oily sludge of processing is for landing greasy filth, jar bed mud or scum silica frost.
3. according to the integrated conduct method of the described oily sludge of claim 1, it is characterized in that in first washing trough of cleaning area, when charging when landing greasy filth, should regulate pH=7~9, water temperature is 60 ℃~70 ℃; When charging is scum silica frost, pH=4~6, water temperature is 60 ℃~70 ℃, institute's adding medicine is emulsion splitter DL-100100~500ppm; When charging is the jar bed mud, pH=8~11, water temperature is 70 ℃~90 ℃, institute's adding medicine is emulsion splitter DL-4020 100~200ppm; Set up two rectification walls in the groove separately, perforate Φ 100~200mm, pitch of holes 300~600mm, spiral heater is established in the stage casing, and it is 3~5m/h that waterpower stirs flow velocity.
4. according to the integrated conduct method of the described oily sludge of claim 1, it is characterized in that in cleaning area second washing trough, when charging when landing greasy filth, jar bed mud or scum silica frost, regulating pH is 7~8.
5. according to the integrated conduct method of the described oily sludge of claim 1, it is characterized in that in the cleaning area medial launder, when charging when landing greasy filth, institute's adding medicine is clean-out system AEO-9 0~5000ppm; When charging was scum silica frost, institute's adding medicine was the poly-iron 100~500ppm of flocculation agent and flocculation agent CPAM 10~50ppm; When charging was the jar bed mud, institute's adding medicine was clean-out system AEO-9 2000~5000ppm.
CNB2005100466271A 2005-06-07 2005-06-07 Process of flowing multistage chemical thermo-dynamic for cleaning mud oil-containing CN1304309C (en)

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* Cited by examiner, † Cited by third party
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CN101786776B (en) * 2010-02-23 2011-10-19 北京欧泰克石油工程技术有限责任公司 Advanced treatment process of sludge containing oil
CN104276736A (en) * 2013-07-03 2015-01-14 抚顺中海石油化工有限公司 Shale oil sludge treatment technology
CN104773931A (en) * 2015-03-17 2015-07-15 浙江海洋学院 Method utilizing city sewage to process greasy filth
CN111304014A (en) * 2020-04-10 2020-06-19 济南蓝昆新材料科技有限公司 Oil sludge sand cleaning agent, oil sludge sand cleaning method and oil sludge sand cleaning system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4787323A (en) * 1987-08-12 1988-11-29 Atlantic Richfield Company Treating sludges and soil materials contaminated with hydrocarbons
JPH1085794A (en) * 1996-09-17 1998-04-07 Nakazono Eiji Sludge treatment method
CN2552919Y (en) * 2002-06-19 2003-05-28 孙庆伦 Oil-containing sludge treatment and utilization device
CN2635669Y (en) * 2003-06-17 2004-08-25 杨敬民 Oil-containing mud treatment device
CN1245336C (en) * 2003-09-10 2006-03-15 胜利油田胜利工程设计咨询有限责任公司 Oil containing sludge treating apparatus

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Publication number Priority date Publication date Assignee Title
CN101786776B (en) * 2010-02-23 2011-10-19 北京欧泰克石油工程技术有限责任公司 Advanced treatment process of sludge containing oil
CN104276736A (en) * 2013-07-03 2015-01-14 抚顺中海石油化工有限公司 Shale oil sludge treatment technology
CN104276736B (en) * 2013-07-03 2016-04-06 抚顺中海石油化工有限公司 Shale oil soil treatment technique
CN104773931A (en) * 2015-03-17 2015-07-15 浙江海洋学院 Method utilizing city sewage to process greasy filth
CN111304014A (en) * 2020-04-10 2020-06-19 济南蓝昆新材料科技有限公司 Oil sludge sand cleaning agent, oil sludge sand cleaning method and oil sludge sand cleaning system

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