CN204111548U - A kind of oily sludge decrement Integrated Processing Unit - Google Patents

A kind of oily sludge decrement Integrated Processing Unit Download PDF

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Publication number
CN204111548U
CN204111548U CN201420410227.9U CN201420410227U CN204111548U CN 204111548 U CN204111548 U CN 204111548U CN 201420410227 U CN201420410227 U CN 201420410227U CN 204111548 U CN204111548 U CN 204111548U
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China
Prior art keywords
unit
emulsion
breakdown
outlet
oil
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Expired - Fee Related
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CN201420410227.9U
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Chinese (zh)
Inventor
张启民
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100 Mima (tianjin) Co Ltd
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100 Mima (tianjin) Co Ltd
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Priority to CN201420410227.9U priority Critical patent/CN204111548U/en
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Abstract

The utility model provides a kind of oily sludge decrement Integrated Processing Unit efficiently, comprise containing dirt pond, oil sump, physically screening unit, breakdown of emulsion oxidation unit, three phase separation unit etc., the described rear end containing dirt pond is logical to be connected with physically screening unit, the rear end of described physically screening unit is connected with breakdown of emulsion oxidation unit, three phase separation unit from front to back in turn, described physically screening unit, three phase separation unit are connected with compressed moulding unit, described three phase separation unit is connected with oil sump, and described three phase separation unit is connected with containing dirt pond.The utility model adopts high-frequency impulse technology to carry out effective breakdown of emulsion to oily sludge, oil is effectively separated from mud, high-frequency impulse breakdown of emulsion is physics breakdown of emulsion, do not produce secondary pollution, utilize catalytic oxidation technologies to process the organic matter in sewage simultaneously, greatly reduce the content of the oil and the organic matter's in mud, significantly reduce follow-up processing load and processing costs.

Description

A kind of oily sludge decrement Integrated Processing Unit
Technical field
The utility model relates to field of sludge treatment, particularly relates to a kind of oily sludge decrement Integrated Processing Unit.
Background technology
Oily sludge is the oily solid sludge produced in oil production, transport, refining and oily water treatment process, along with continuing to increase of underground Oil extraction dynamics, the continuous reorganization and expansion of Petrochemical Enterprises, the quantum of output of oily sludge increases gradually, if oily sludge is not processed, not only contaminate environment, and the serious waste causing petroleum resources.The final purpose of disposal of oily sludge is with resource utilization, innoxious, decrement turns to principle, at present the treatment process that oily sludge is conventional is had: solvent extration, burning method, biological process, pyrogenic process, oily sludge comprehensive utilization etc., but due to oily sludge complicated, often kind for the treatment of process has respective relative merits and the scope of application, all types of oily sludge can be processed without any a kind for the treatment of process, these methods all do not have to get on to deal with problems from source, invent a kind of device carrying out decrement treatment before disposal of oily sludge, could by innoxious, resource utilization, with minimizing The Gift of Being the Best You Can Be.
Summary of the invention
According to above technical problem, the utility model provides a kind of oily sludge decrement Integrated Processing Unit efficiently, it is characterized in that: comprise containing dirt pond, oil sump, physically screening unit, breakdown of emulsion oxidation unit, three phase separation unit, compressed moulding unit, transferpump, recycle pump, greasy dirt water pipe, the described rear end containing dirt pond is connected with physically screening unit by transferpump by greasy dirt water pipe, the rear end of described physically screening unit is connected with breakdown of emulsion oxidation unit by greasy dirt water pipe from front to back successively, three phase separation unit, described physically screening unit, three phase separation unit is connected with compressed moulding unit by greasy dirt water pipe, described three phase separation unit is connected with oil sump by greasy dirt water pipe, described three phase separation unit is connected with containing dirt pond by recycle pump by greasy dirt water pipe, described physically screening unit comprises frame, A fluid inlet, separator box, vibratory screening apparatus, particle outlet, A liquid outlet, described separator box is arranged in frame, the upper end of described separator box is provided with A fluid inlet, the rear end of described separator box is provided with particle outlet, the lower end of described separator box is provided with liquid outlet, the upper end of described liquid outlet is provided with vibratory screening apparatus, and described A fluid inlet is connected with containing dirt pond, and described particle outlet is connected with compressed moulding unit by greasy dirt water pipe, described breakdown of emulsion oxidation unit comprises B fluid inlet, breakdown of emulsion medicament chamber, high frequency breakdown of emulsion room, catalysis medicament chamber, catalyzed oxidation room, B liquid outlet, described high frequency breakdown of emulsion room offers B fluid inlet, the upper end of described high frequency breakdown of emulsion room is provided with breakdown of emulsion medicament chamber, described catalyzed oxidation room offers B liquid outlet, the upper end of described catalyzed oxidation room is provided with catalysis medicament chamber, described high frequency breakdown of emulsion room is connected with catalyzed oxidation room, and described B fluid inlet is connected with A liquid outlet, described three phase separation unit comprises C fluid inlet, Mud Sepa Machine, oil-water separation tank, C liquid outlet, oil outlet, sludge outlet, described Mud Sepa Machine offers C fluid inlet, sludge outlet, described oil-water separation tank offers oil outlet, C liquid outlet, described oil-water separation tank is arranged on the lower end of Mud Sepa Machine, described C fluid inlet is connected with B liquid outlet, described sludge outlet is connected with compressed moulding unit by greasy dirt water pipe, described oil outlet is connected with oil sump by greasy dirt water pipe, described C liquid outlet is connected with containing dirt pond by recycle pump by greasy dirt water pipe.
Described separator box is obliquely installed.
Described vibratory screening apparatus is identical with particle outlet height.
Described high frequency breakdown of emulsion room is high-frequency impulse breakdown of emulsion structure.
The beneficial effects of the utility model are: the utility model adopts high-frequency impulse technology to carry out effective breakdown of emulsion to oily sludge, oil is effectively separated from mud, high-frequency impulse breakdown of emulsion is physics breakdown of emulsion, do not use pharmaceutical chemicals, only need use a small amount of emulsion splitter when Special Circumstances, do not produce secondary pollution, utilize catalytic oxidation technologies to process the organic matter in sewage simultaneously, greatly reduce the content of the oil and the organic matter's in mud, and promote solid liquid phase sharp separation, make process after mud in oil-contg lower than 2%, the easy compressed moulding of mud after process, thus significantly reduce the total amount of oily sludge, significantly reduce follow-up processing load and processing costs, the oil reclaimed in mud improves the economic benefit of enterprise simultaneously.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is the structural representation of physically screening unit;
Fig. 3 is the structural representation of breakdown of emulsion oxidation unit;
Fig. 4 is the structural representation of three phase separation unit.
Embodiment
According to Fig. 1, Fig. 2, Fig. 3, Fig. 4, the utility model is further described:
As Fig. 1, Fig. 2, Fig. 3, Fig. 4, containing dirt pond-1, oil sump-2, physically screening unit-3, breakdown of emulsion oxidation unit-4, three phase separation unit-5, compressed moulding unit-6, transferpump-7, recycle pump-8, greasy dirt water pipe-9, frame-31, A fluid inlet-32, separator box-33, vibratory screening apparatus-34, particle outlet-35, A liquid outlet-36, B fluid inlet-41, breakdown of emulsion medicament chamber-42, high frequency breakdown of emulsion room-43, catalysis medicament chamber-44, catalyzed oxidation room-45, B liquid outlet-46, C fluid inlet-51, Mud Sepa Machine-52, oil-water separation tank-53, C liquid outlet-54, oil outlet-55, sludge outlet-56.
Embodiment 1
This practicality comprises containing dirt pond 1, oil sump 2, physically screening unit 3, breakdown of emulsion oxidation unit 4, three phase separation unit 5, compressed moulding unit 6, transferpump 7, recycle pump 8, greasy dirt water pipe 9, first be connected with physically screening unit 3 by transferpump 7 by greasy dirt water pipe 9 in the rear end containing dirt pond 1, then breakdown of emulsion oxidation unit 4 is connected by greasy dirt water pipe 9 successively from front to back in the rear end of physically screening unit 3, three phase separation unit 5, again by physically screening unit 3, three phase separation unit 5 is connected with compressed moulding unit 6 by greasy dirt water pipe 9, finally by three phase separation unit 5 by greasy dirt water pipe 9 respectively with oil sump 2, connect containing dirt pond 1, and recycle pump 8 is arranged on greasy dirt water pipe 9 that three phase separation unit 5 is connected with containing dirt pond 1,
Wherein, physically screening unit 3 comprises frame 31, A fluid inlet 32, separator box 33, vibratory screening apparatus 34, particle outlet 35, A liquid outlet 36, first A fluid inlet 32 is offered in the upper end of separator box 33, particle outlet 35 is offered in the rear end of separator box 33, liquid outlet is offered in the lower end of separator box 33, then vibratory screening apparatus 34 is arranged on the upper end of liquid outlet, again separator box 33 is arranged in frame 31, finally A fluid inlet 32 is connected with containing dirt pond 1, particle outlet 35 is connected with compressed moulding unit 6 by greasy dirt water pipe 9;
Breakdown of emulsion oxidation unit 4 comprises B fluid inlet 41, breakdown of emulsion medicament chamber 42, high frequency breakdown of emulsion room 43, catalysis medicament chamber 44, catalyzed oxidation room 45, B liquid outlet 46, first on high frequency breakdown of emulsion room 43, B fluid inlet 41 is offered, catalyzed oxidation room 45 is offered B liquid outlet 46, then breakdown of emulsion medicament chamber 42, catalysis medicament chamber 44 are arranged on respectively the upper end of high frequency breakdown of emulsion room 43, catalyzed oxidation room 45, finally high frequency breakdown of emulsion room 43 is connected with catalyzed oxidation room 45, B fluid inlet 41 is connected with A liquid outlet 36;
Three phase separation unit 5 comprises C fluid inlet 51, Mud Sepa Machine 52, oil-water separation tank 53, C liquid outlet 54, oil outlet 55, sludge outlet 56, first on Mud Sepa Machine 52, C fluid inlet 51 is offered, sludge outlet 56, oil-water separation tank 53 sets out hydraulic fluid port 55, C liquid outlet 54, then oil-water separation tank 53 is arranged on the lower end of Mud Sepa Machine 52, finally C fluid inlet 51 is connected with B liquid outlet 46, sludge outlet 56 is connected with compressed moulding unit 6 by greasy dirt water pipe 9, oil outlet 55 is connected with oil sump 2 by greasy dirt water pipe 9, C liquid outlet 54 is connected with containing dirt pond 1 by recycle pump 8 by greasy dirt water pipe 9.
Embodiment 2
During use, containing the oily sludge in dirt pond 1 by transferpump 7, separator box 33 is entered from A fluid inlet 32 through greasy dirt water pipe 9, physically screening is carried out by vibratory screening apparatus 34, particle particle diameter being greater than 30mm is separated from liquid, compressed moulding unit 6 is drained into from particle outlet 35, the liquid separated flows out from A liquid outlet 36, enter high frequency breakdown of emulsion room 43 from B fluid inlet 41 and carry out the process of high-frequency impulse breakdown of emulsion, enter catalyzed oxidation room 45 again and carry out catalytic oxidation treatment, liquid after process flows out from B liquid outlet 46, enter into Mud Sepa Machine 52 from C fluid inlet 51 and carry out solid-liquid separation, sludge residue after separation enters compressed moulding unit 6 from sludge outlet 56 by greasy dirt water pipe 9, after liquid flows into oil-water separation tank 53 stratification, sewage is recycled into containing dirt pond 1 from C liquid outlet 54 by recycle pump 8, sump oil is injected oil sump 2 from oil outlet 55.
Embodiment 3
Treatment capacity 2 tons/hour, when not adding any medicament, realize greasy filth water sharp separation and Impurity removal, by test: when sewage temperature 29 ~ 31 DEG C, Average oil concentration 15692mg/L (most high-content 57160mg/L), average suspended solids content 59.4mg/L (the highest 146mg/L), after process, average oil content reaches 232.6mg/L, after press filtration drying forming, volume reduces 80%, shorten the treatment time, simplify treatment scheme and reduce working cost.
The above is only preferred implementation of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model principle; can also make some improvement, these improvement also should be considered as protection domain of the present utility model.

Claims (4)

1. an oily sludge decrement Integrated Processing Unit, it is characterized in that: comprise containing dirt pond, oil sump, physically screening unit, breakdown of emulsion oxidation unit, three phase separation unit, compressed moulding unit, transferpump, recycle pump, greasy dirt water pipe, the described rear end containing dirt pond is connected with physically screening unit by transferpump by greasy dirt water pipe, the rear end of described physically screening unit is connected with breakdown of emulsion oxidation unit by greasy dirt water pipe from front to back successively, three phase separation unit, described physically screening unit, three phase separation unit is connected with compressed moulding unit by greasy dirt water pipe, described three phase separation unit is connected with oil sump by greasy dirt water pipe, described three phase separation unit is connected with containing dirt pond by recycle pump by greasy dirt water pipe, described physically screening unit comprises frame, A fluid inlet, separator box, vibratory screening apparatus, particle outlet, A liquid outlet, described separator box is arranged in frame, the upper end of described separator box is provided with A fluid inlet, the rear end of described separator box is provided with particle outlet, the lower end of described separator box is provided with liquid outlet, the upper end of described liquid outlet is provided with vibratory screening apparatus, and described A fluid inlet is connected with containing dirt pond, and described particle outlet is connected with compressed moulding unit by greasy dirt water pipe, described breakdown of emulsion oxidation unit comprises B fluid inlet, breakdown of emulsion medicament chamber, high frequency breakdown of emulsion room, catalysis medicament chamber, catalyzed oxidation room, B liquid outlet, described high frequency breakdown of emulsion room offers B fluid inlet, the upper end of described high frequency breakdown of emulsion room is provided with breakdown of emulsion medicament chamber, described catalyzed oxidation room offers B liquid outlet, the upper end of described catalyzed oxidation room is provided with catalysis medicament chamber, described high frequency breakdown of emulsion room is connected with catalyzed oxidation room, and described B fluid inlet is connected with A liquid outlet, described three phase separation unit comprises C fluid inlet, Mud Sepa Machine, oil-water separation tank, C liquid outlet, oil outlet, sludge outlet, described Mud Sepa Machine offers C fluid inlet, sludge outlet, described oil-water separation tank offers oil outlet, C liquid outlet, described oil-water separation tank is arranged on the lower end of Mud Sepa Machine, described C fluid inlet is connected with B liquid outlet, described sludge outlet is connected with compressed moulding unit by greasy dirt water pipe, described oil outlet is connected with oil sump by greasy dirt water pipe, described C liquid outlet is connected with containing dirt pond by recycle pump by greasy dirt water pipe.
2., according to oily sludge decrement Integrated Processing Unit according to claim 1, it is characterized in that: described separator box is obliquely installed.
3., according to oily sludge decrement Integrated Processing Unit according to claim 1, it is characterized in that: described vibratory screening apparatus is identical with particle outlet height.
4. according to oily sludge decrement Integrated Processing Unit according to claim 1, it is characterized in that: described high frequency breakdown of emulsion room is high-frequency impulse breakdown of emulsion structure.
CN201420410227.9U 2014-07-24 2014-07-24 A kind of oily sludge decrement Integrated Processing Unit Expired - Fee Related CN204111548U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420410227.9U CN204111548U (en) 2014-07-24 2014-07-24 A kind of oily sludge decrement Integrated Processing Unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420410227.9U CN204111548U (en) 2014-07-24 2014-07-24 A kind of oily sludge decrement Integrated Processing Unit

Publications (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110563287A (en) * 2019-08-30 2019-12-13 南京庞瑞科技有限公司 Greasy dirt processing system based on internet of things

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110563287A (en) * 2019-08-30 2019-12-13 南京庞瑞科技有限公司 Greasy dirt processing system based on internet of things

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150121

Termination date: 20200724