CN105541063A - Integrated oil sludge treatment systems and use method thereof - Google Patents
Integrated oil sludge treatment systems and use method thereof Download PDFInfo
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- CN105541063A CN105541063A CN201610008427.5A CN201610008427A CN105541063A CN 105541063 A CN105541063 A CN 105541063A CN 201610008427 A CN201610008427 A CN 201610008427A CN 105541063 A CN105541063 A CN 105541063A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
Abstract
The invention relates to the field of petro-chemical, in particular to integrated oil sludge treatment systems and a use method thereof, wherein the integrated oil sludge treatment systems are used for drilling cutting oil sludge generated by oil extraction, oil sludge accumulated at the bottom of a crude oil storage tank, oily sludge, aging oil sludge and the like. According to the integrated oil sludge treatment systems and the use method thereof, container type assembly is adopted, and container modules can be increased or decreased according to actual situations of handling capacity; washing water can be recycled, pollution is reduced, reheating is avoided, energy is saved, and the environment is protected; each integrated oil sludge treatment system comprises a cleaning reaction lever and a control and water treatment lever. The invention further provides the use method of the two types of integrated oil sludge treatment systems; the soil oil content of a treated product is smaller than 0.5-1%, and the PH is 6-9; the emission standard is reached after water treatment, ACOD is smaller than or equal to 100, BOD is smaller than or equal to 20, SS is smaller than or equal to 70, and PH is 6-9.
Description
Technical field
The present invention relates to a kind of petrochemical field, particularly relate to a kind of drilling cuttings greasy filth for Oil extraction, Plates of Oil Storage Tank prodelta clay greasy filth, ground sludge, the integrated oil mud treatment system of aging greasy filth etc. and using method thereof.
Background technology
Oil is a kind of thickness, Vandyke brown liquid.There is oil storing upper crustal some areas.Main component is the mixture of various alkane, naphthenic hydrocarbon, aromatic hydrocarbon.The composition of crude oil mainly contains: oil (this is its main component), colloid (a kind of semi-solid material of viscosity), bituminous matter (dun or black brittle solid material), carbonaceous (a kind of nonhydrocarbon).Oil is main mixing by hydrocarbon polymer, that have special odor, coloured flammable oleaginous fluid.
The drilling cuttings greasy filth of Oil extraction, Plates of Oil Storage Tank prodelta clay greasy filth, ground sludge, aging greasy filth.Greasy filth on market after general device process, after process, greasy filth oleaginousness is 5-6%, and efficiency is low, is unable to catch up with greasy filth and produces, and untreated greasy filth oil is piled into the phenomenon on mountain.To environment.
Summary of the invention
The object of the invention is to overcome shortcoming of the prior art, provide a kind of integrated oil mud treatment system and using method thereof, adopt container-type assembling, treatment capacity can increase and decrease freight container module according to practical situation.Rinse water recycling capable of circulation, decreasing pollution, avoids reheating, energy-conserving and environment-protective.
Integrated oil mud treatment system, comprises cleaning reaction sled and controls and water treatment sled,
Described cleaning reaction is provided with air compressor machine A7 on prizing and stirred pot A1 is cleaned with spiral pump A8 in lower end, the water feed inlet of cleaning stirred pot A1 is connected with volume pump A4, cleaning stirred pot A1 upper inlet is connected with the charging machine A10 for inputting greasy filth, the middle lower exit port handoff impeller pump A9 of cleaning stirred pot A1, is connected with chemicals feeder A6 and floating-oil collector A2 above cleaning stirred pot A1;
Described control and water treatment sled comprise connect successively sleeping spiral shell separator B1, minibuffer water tank B2, impeller pump B3, large buffer tank B4 and rotary gas separator B6, described rotary gas separator B6 is provided with the overflow port for oil extraction;
The upper impeller pump A5 of described cleaning reaction sled is connected with the sleeping spiral shell separator B1 that control and water treatment are prized, and described large buffer tank B4 is connected with volume pump A4, and described transfer impeller pump A9 is connected with swirler B6.
Preferably, described cleaning reaction sled is also provided with cleaning stirred pot A3, cleaning stirred pot A3 upper inlet is connected with the charging machine A10 for inputting greasy filth, the water feed inlet of cleaning stirred pot A3 is connected with volume pump A4, the lower end outlet of cleaning stirred pot A3 is connected with spiral pump A5, is connected with chemicals feeder A6 and floating-oil collector A2 above cleaning stirred pot A1; Described volume pump A4 respectively and cleaning stirred pot A1 and clean between stirred pot A3 and be provided with valve.
Preferably, described spiral pump A8 and spiral pump A5 is provided with operated pneumatic valve.
Preferably, described volume pump A4 and transfer impeller pump A9 is provided with operated pneumatic valve.
Preferably, described control and water treatment sled are also provided with porcelain filter B7 and the intercepting type filter B 8 of connection, and described porcelain filter B7 is connected with swirler B6 by T-valve.
In addition, present invention also offers the using method of integrated oil mud treatment system.
Integrated oil mud treatment system obtains using method, comprises the steps:
1) open air compressor machine A7, prepare to control operated pneumatic valve;
2) add water with volume pump A4 in cleaning stirred pot A1;
3) by A10 feeder, add greasy filth to A1, open the agitator of cleaning stirred pot A1, slowly accelerate;
4) open chemicals feeder A6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2, collects cleaning stirred pot A1 upper strata oil slick;
6) stop floating-oil collector A2, open valve open cleaning stirred pot A1 at the middle and upper levels peaceful water deliver to swirler B6 by transfer impeller pump A9, then it is for subsequent use to arrive minibuffer water tank B2, the oil extraction of swirler B6 overflow port;
7) after peaceful water discharges, open reactor A 1 agitator, open horizontal screw centrifuge B1 in sled B simultaneously, Deng rotating speed normal after, open spiral pump A8 while stirring, after transfer cleaning, greasy filth is to horizontal screw centrifuge B1, primary water is to minibuffer tank B2, minibuffer tank B2, to certain liquid level, automatically opens impeller pump B3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge.
Preferably, the weight adding water and greasy filth in described cleaning stirred pot is: 5:1.
Preferably, described step 4) cleaning stirred pot at the temperature stirring and washing 15min of about 90 DEG C, after stop the peaceful 15min of stirrer.
Preferably, described step 6) swirler B6 lower end overflow port access B7 ceramic filtration device, lease strainer to B8, then discharge after MBR water treatment B5.
Present invention also offers the using method of another kind of integrated oil mud treatment system.
Integrated oil mud treatment system obtains using method, comprises the steps:
1) open air compressor machine A7, prepare to control operated pneumatic valve;
2) in cleaning stirred pot A1,5 tons are added water with volume pump A4;
3) by A10 feeder, add 1 ton, greasy filth to A1, open the agitator of cleaning stirred pot A1, slowly accelerate;
4) open chemicals feeder A6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2, collects cleaning stirred pot A1 upper strata oil slick;
6) stop floating-oil collector A2, open valve open cleaning stirred pot A1 at the middle and upper levels peaceful water deliver to swirler B6 by transfer impeller pump A9, then it is for subsequent use to arrive minibuffer water tank B2, the oil extraction of swirler B6 overflow port;
7) after peaceful water discharges, open reactor A 1 agitator, open B1 horizontal screw centrifuge in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1, primary water is to minibuffer tank B2, B2, to certain liquid level, automatically opens impeller pump B3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge;
8) A1 is in step 3) start after, switch pneumavalve, volume pump starts to add water to A3.
9) A9 feeder is to getting back to A3 position, adds greasy filth to A3, opens cleaning reactor.
10) open chemicals feeder A6 dosing to A3 adding medicine, open steam heating;
11) circulation step 4)-9).
Preferably, the weight adding water and greasy filth in described cleaning stirred pot is: 5:1.
Preferably, described step 4) cleaning stirred pot at the temperature stirring and washing 15min of about 90 DEG C, after stop the peaceful 15min of stirrer.
Preferably, described step 6) swirler B6 lower end overflow port access B7 ceramic filtration device, lease strainer to B8, then discharge after MBR water treatment B5.
After product treatment of the present invention, soil oleaginousness is less than 0.5-1%, PH:6-9; Emission standard is reached, ACOD≤100, BOD≤20, SS≤70, PH6-9 after water treatment.
Mud cleaning sled A structure
In mud cleaning sled A freight container, A1 is fixed on both sides, A3 cleans stirred pot, below two cleaning stirred pots, A8 is installed, A5, spiral pump, air butterfly valve is installed therebetween, in the middle of two cleaning stirred pots, automatic medicament feeding machine A6 is installed, is fixed on sled A base plate and opens, directly over floating-oil collector A2 is installed, in addition volume pump A4 is installed, outlet is whereabouts two stirred tank respectively, and in retort, operated pneumatic valve also will be installed in upper position therebetween, transfer impeller pump A9, import connects upper/lower positions in two stirred tank respectively, installs operated pneumatic valve therebetween.Pipeline, pump, valve respective flange connects.
2, control and water treatment sled B structure
Mud cleaning sled B freight container horizontal screw centrifuge B1, raises its base, is arranged in sled B, surge tank B2 is installed in below, packs up horizontal screw centrifuge B1 and is separated rear liquid, then meet impeller pump B3, be transferred to large buffer tank B4, large buffer tank B4 water receiving pipe only prizes the volume pump A4 import of A.
The transfer impeller pump A9 filler pipe of sled A meets the swirler B6 of sled B, swirler overflow port connects the large buffer tank of threeway one termination, one termination pottery formula filter B 7 import, the outlet of pottery formula filter B 7 connects intercepting type filter B 8 import, and intercepting type filter B 8 connects MBR microbial film water treating pond.
Sludge treatment system technical process
1, open air compressor machine A7, prepare to control operated pneumatic valve.
1, in A1 cleaning reaction still, 5 tons are added water with volume pump A4.
2, by A10 feeder, add 1 ton, greasy filth to A1, open cleaning reaction agitator, slowly accelerate.
3, open chemicals feeder A6 dosing, before chemical feeding quantity has, experimental result setting, opens steam heating, and keeps the temperature of about 90 DEG C.
4, stirring and washing 15min, after stop the peaceful 15min of stirrer.
5, valve transfer, to reactor 1, opens floating-oil collector A2, collects reactor upper strata oil slick, 2min
6, stop floating-oil collector A2, open a cleaning reaction still A1 at the middle and upper levels peaceful water by A9 shift centrifugal pumping to B6 swirler, then to buffer tank for subsequent use, the oil extraction of swirler overflow port.Or cyclone lower end overflow port access B7 ceramic filtration device, lease strainer to B8, then discharge after MBR water treatment B5.
7, after peaceful water discharges, open reactor A 1 agitator, open B1 horizontal screw centrifuge in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1, primary water is to minibuffer tank B2, B2, to certain liquid level, automatically opens impeller pump B3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge.
8, A1 is after 3 steps start, and switch pneumavalve, volume pump starts to add 5 tons of water to A3.
9, A9 feeder is to getting back to A3 position, adds 1 ton, greasy filth to A3, opens cleaning reactor.
10, to A3 adding medicine, steam heating is opened.
11, start 4-7 and walk symmetric content.
The application adopts container-type to assemble, and treatment capacity can increase and decrease freight container module according to practical situation.Rinse water recycling capable of circulation, decreasing pollution, avoids reheating, energy-conserving and environment-protective.After this product treatment, soil oleaginousness is less than 0.5-1%, PH:6-9.Emission standard is reached, ACOD≤100, BOD≤20, SS≤70, PH6-9 after water treatment.
Accompanying drawing explanation
Fig. 1 is the structural representation of mud of the present invention cleaning sled A.
Fig. 2 is the main TV structure schematic diagram of Fig. 1.
Fig. 3 is the attached TV structure schematic diagram of Fig. 1.
Fig. 4 is Fig. 1 side structure schematic diagram.
Fig. 5 is control of the present invention and water treatment sled B structural representation.
Fig. 6 is the main TV structure schematic diagram of Fig. 5.
The attached TV structure schematic diagram of Fig. 7 Fig. 5.
Embodiment
Below in conjunction with accompanying drawing, technical scheme of the present invention is further described, but the present invention is not limited to the scope of these embodiments.
Integrated oil mud treatment system, comprises cleaning reaction sled and controls and water treatment sled,
Described cleaning reaction is provided with air compressor machine A7Q7 on prizing and stirred pot A1Q1 is cleaned with spiral pump A8Q8 in lower end, the water feed inlet of cleaning stirred pot A1Q1 is connected with volume pump A4Q4, cleaning stirred pot A1Q1 upper inlet is connected with the charging machine A10Q10 for inputting greasy filth, the middle lower exit port handoff impeller pump A9Q9 of cleaning stirred pot A1Q1, is connected with chemicals feeder A6Q6 and floating-oil collector A2Q2 above cleaning stirred pot A1Q1;
Described control and water treatment sled comprise connect successively sleeping spiral shell separator B1S1, minibuffer water tank B2S2, impeller pump B3S3, large buffer tank B4S4 and rotary gas separator B6S6, described rotary gas separator B6S6 is provided with the overflow port for oil extraction;
The upper impeller pump A5Q5 of described cleaning reaction sled is connected with the sleeping spiral shell separator B1S1 that control and water treatment are prized, and described large buffer tank B4S4 is connected with volume pump A4Q4, and described transfer impeller pump A9Q9 is connected with swirler B6S6.
Preferably, described cleaning reaction sled is also provided with cleaning stirred pot A3Q3, cleaning stirred pot A3Q3 upper inlet is connected with the charging machine A10Q10 for inputting greasy filth, the water feed inlet of cleaning stirred pot A3Q3 is connected with volume pump A4Q4, the lower end outlet of cleaning stirred pot A3Q3 is connected with spiral pump A5Q5, is connected with chemicals feeder A6Q6 and floating-oil collector A2Q2 above cleaning stirred pot A1Q1; Described volume pump A4Q4 respectively and cleaning stirred pot A1Q1 and clean between stirred pot A3Q3 and be provided with valve.
Preferably, described spiral pump A8Q8 and spiral pump A5Q5 is provided with operated pneumatic valve.
Preferably, described volume pump A4Q4 and transfer impeller pump A9Q9 is provided with operated pneumatic valve.
Preferably, described control and water treatment sled are also provided with porcelain filter B7S7 and the intercepting type filter B 8S8 of connection, and described porcelain filter B7S7 is connected with swirler B6S6 by T-valve.
In addition, present invention also offers the using method of integrated oil mud treatment system.
Integrated oil mud treatment system obtains using method, comprises the steps:
1) open air compressor machine A7Q7, prepare to control operated pneumatic valve;
2) add water with volume pump A4Q4 in cleaning stirred pot A1Q1;
3) by A10Q10 feeder, add greasy filth to A1Q1, open the agitator of cleaning stirred pot A1Q1, slowly accelerate;
4) open chemicals feeder A6Q6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2Q2, collects cleaning stirred pot A1Q1 upper strata oil slick;
6) stop floating-oil collector A2Q2, open valve open cleaning stirred pot A1Q1 at the middle and upper levels peaceful water deliver to swirler B6S6 by transfer impeller pump A9Q9, then it is for subsequent use to arrive minibuffer water tank B2S2, the oil extraction of swirler B6S6 overflow port;
7) after peaceful water discharges, open reactor A 1Q1 agitator, open B1S1 horizontal screw centrifuge in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8Q8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1S1, primary water is to minibuffer tank B2S2, B2S2, to certain liquid level, automatically opens impeller pump B3S3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge.
Preferably, the weight adding water and greasy filth in described cleaning stirred pot is: 5:1.
Preferably, described step 4 cleans stirred pot at the temperature stirring and washing 15min of about 90 DEG C, after stop the peaceful 15min of stirrer.
Preferably, described step 6 swirler B6S6 lower end overflow port access B7S7 ceramic filtration device, leases strainer to B8S8, then discharges after MBR water treatment B5S5.
Present invention also offers the using method of another kind of integrated oil mud treatment system.
Integrated oil mud treatment system obtains using method, comprises the steps:
1) open air compressor machine A7Q7, prepare to control operated pneumatic valve;
2) in cleaning stirred pot A1Q1,5 tons are added water with volume pump A4Q4;
3) by A10Q10 feeder, add 1 ton, greasy filth to A1Q1, open the agitator of cleaning stirred pot A1Q1, slowly accelerate;
4) open chemicals feeder A6Q6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2Q2, collects cleaning stirred pot A1Q1 upper strata oil slick;
6) stop floating-oil collector A2Q2, open valve open cleaning stirred pot A1Q1 at the middle and upper levels peaceful water deliver to swirler B6S6 by transfer impeller pump A9Q9, then it is for subsequent use to arrive minibuffer water tank B2S2, the oil extraction of swirler B6S6 overflow port;
7) after peaceful water discharges, open reactor A 1Q1 agitator, open B1S1 horizontal screw centrifuge in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8Q8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1S1, primary water is to minibuffer tank B2S2, B2S2, to certain liquid level, automatically opens impeller pump B3S3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge;
8) A1Q1 is after step 3 starts, and switch pneumavalve, volume pump starts to add water to A3Q3.
9) A9Q9 feeder is to getting back to A3Q3 position, adds greasy filth to A3Q3, opens cleaning reactor.
10) open chemicals feeder A6Q6 dosing to A3Q3 adding medicine, open steam heating;
11) circulation step 4-9.
Preferably, the weight adding water and greasy filth in described cleaning stirred pot is: 5:1.
Preferably, described step 4 cleans stirred pot at the temperature stirring and washing 15min of about 90 DEG C, after stop the peaceful 15min of stirrer.
Preferably, described step 6 swirler B6S6 lower end overflow port access B7S7 ceramic filtration device, leases strainer to B8S8, then discharges after MBR water treatment B5S5.
Claims (10)
1. integrated oil mud treatment system, is characterized in that: comprise cleaning reaction sled and control and water treatment sled,
Described cleaning reaction is provided with air compressor machine A7 on prizing and stirred pot A1 is cleaned with spiral pump A8 in lower end, the water feed inlet of cleaning stirred pot A1 is connected with volume pump A4, cleaning stirred pot A1 upper inlet is connected with the charging machine A10 for inputting greasy filth, the middle lower exit port handoff impeller pump A9 of cleaning stirred pot A1, is connected with chemicals feeder A6 and floating-oil collector A2 above cleaning stirred pot A1;
Described control and water treatment sled comprise connect successively sleeping spiral shell separator B1, minibuffer water tank B2, impeller pump B3, large buffer tank B4 and rotary gas separator B6, described rotary gas separator B6 is provided with the overflow port for oil extraction;
The upper impeller pump A5 of described cleaning reaction sled is connected with the sleeping spiral shell separator B1 that control and water treatment are prized, and described large buffer tank B4 is connected with volume pump A4, and described transfer impeller pump A9 is connected with swirler B6.
2. integrated oil mud treatment system according to claim 1, it is characterized in that: described cleaning reaction sled is also provided with cleaning stirred pot A3, cleaning stirred pot A3 upper inlet is connected with the charging machine A10 for inputting greasy filth, the water feed inlet of cleaning stirred pot A3 is connected with volume pump A4, the lower end outlet of cleaning stirred pot A3 is connected with spiral pump A5, is connected with chemicals feeder A6 and floating-oil collector A2 above cleaning stirred pot A1; Described volume pump A4 respectively and cleaning stirred pot A1 and clean between stirred pot A3 and be provided with valve.
3. integrated oil mud treatment system according to claim 2, is characterized in that: described spiral pump A8 and spiral pump A5 is provided with air butterfly valve.
4. integrated oil mud treatment system according to claim 1 and 2, is characterized in that: described volume pump A4 and transfer impeller pump A9 is provided with air door.
5. integrated oil mud treatment system according to claim 1 and 2, is characterized in that: described control and water treatment sled are also provided with porcelain filter B7 and the intercepting type filter B 8 of connection, and described porcelain filter B7 is connected with swirler B6 by T-valve.
6. integrated oil mud treatment system according to claim 1 and 2, is characterized in that: described control and water treatment sled are provided with MBR water treatment device.
7. integrated oil mud treatment system according to claim 1 obtains using method, it is characterized in that: comprise the steps:
1) open air compressor machine A7, prepare to control operated pneumatic valve;
2) add water with volume pump A4 in cleaning stirred pot A1;
3) by A10 feeder, add greasy filth to A1, open the agitator of cleaning stirred pot A1, slowly accelerate;
4) open chemicals feeder A6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2, collects cleaning stirred pot A1 upper strata oil slick;
6) stop floating-oil collector A2, open valve open cleaning stirred pot A1 at the middle and upper levels peaceful water deliver to swirler B6 by transfer impeller pump A9, then it is for subsequent use to arrive minibuffer water tank B2, the oil extraction of swirler B6 overflow port;
7) after peaceful water discharges, open reactor A 1 agitator, open horizontal screw centrifuge B1 in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1, primary water is to minibuffer tank B2, minibuffer tank B2, to certain liquid level, automatically opens impeller pump B3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge.
8. integrated oil mud treatment system according to claim 1 obtains using method, it is characterized in that: comprise the steps:
1) open air compressor machine A7, prepare to control operated pneumatic valve;
2) in cleaning stirred pot A1,5 tons are added water with volume pump A4;
3) by A10 feeder, add 1 ton, greasy filth to A1, open the agitator of cleaning stirred pot A1, slowly accelerate;
4) open chemicals feeder A6 dosing, open steam heating and carry out stirring and washing, after stop stirrer calmness;
5) valve transfer is to reactor 1, opens floating-oil collector A2, collects cleaning stirred pot A1 upper strata oil slick;
6) stop floating-oil collector A2, open valve open cleaning stirred pot A1 at the middle and upper levels peaceful water deliver to swirler B6 by transfer impeller pump A9, then it is for subsequent use to arrive minibuffer water tank B2, the oil extraction of swirler B6 overflow port;
7) after peaceful water discharges, open reactor A 1 agitator, open horizontal screw centrifuge B1 in sled B simultaneously, Deng rotating speed normal after, Z1 opens spiral pump A8 while stirring, and after transfer cleaning, greasy filth is to horizontal screw centrifuge B1, primary water is to minibuffer tank B2, B2, to certain liquid level, automatically opens impeller pump B3, clear liquor is delivered to baffle-box.The dry mud outlet of horizontal screw centrifuge then loads dolly discharge;
8) A1 is in step 3) start after, switch pneumavalve, volume pump starts to add water to A3.
9) A9 feeder is to getting back to A3 position, adds greasy filth to A3, opens cleaning reactor.
10) open chemicals feeder A6 dosing to A3 adding medicine, open steam heating;
11) circulation step 4)-9).
9. the method according to claim 6 or 7, is characterized in that: the weight adding water and greasy filth in described cleaning stirred pot is: 5:1.
10. the method according to claim 6 or 7, is characterized in that: described step 4) cleaning stirred pot at the temperature stirring and washing 15min of about 90 DEG C, after stop the peaceful 15min of stirrer; Described step 6) swirler B6 lower end overflow port access B7 ceramic filtration device, lease strainer to B8, then discharge after MBR water treatment B5.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109592283A (en) * | 2018-11-29 | 2019-04-09 | 浙江海洋大学 | Super long type underground petroleum cave depot bottom deposit sludge treatment system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1232804A2 (en) * | 2001-02-20 | 2002-08-21 | SK Corporation | Method for removing sludge in crude oil tank and recovering oil therefrom |
| CN203346238U (en) * | 2013-07-20 | 2013-12-18 | 杨庆辉 | Vehicle-mounted oily sludge treatment device |
| CN203382621U (en) * | 2013-07-15 | 2014-01-08 | 北京纬纶华业环保科技股份有限公司 | Resourceful treatment system of oily sludge |
| CN205313342U (en) * | 2016-01-05 | 2016-06-15 | 杭州造品科技有限公司 | Integration sludge treatment system |
-
2016
- 2016-01-05 CN CN201610008427.5A patent/CN105541063A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1232804A2 (en) * | 2001-02-20 | 2002-08-21 | SK Corporation | Method for removing sludge in crude oil tank and recovering oil therefrom |
| CN203382621U (en) * | 2013-07-15 | 2014-01-08 | 北京纬纶华业环保科技股份有限公司 | Resourceful treatment system of oily sludge |
| CN203346238U (en) * | 2013-07-20 | 2013-12-18 | 杨庆辉 | Vehicle-mounted oily sludge treatment device |
| CN205313342U (en) * | 2016-01-05 | 2016-06-15 | 杭州造品科技有限公司 | Integration sludge treatment system |
Non-Patent Citations (1)
| Title |
|---|
| 张维: ""油罐清洗与罐底泥处理技术研究及应用"", 《油气田环境保护》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109592283A (en) * | 2018-11-29 | 2019-04-09 | 浙江海洋大学 | Super long type underground petroleum cave depot bottom deposit sludge treatment system |
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Application publication date: 20160504 |