CN110479686A - A kind of solid-liquid separating method for oily sediment recovery processing - Google Patents
A kind of solid-liquid separating method for oily sediment recovery processing Download PDFInfo
- Publication number
- CN110479686A CN110479686A CN201910802731.0A CN201910802731A CN110479686A CN 110479686 A CN110479686 A CN 110479686A CN 201910802731 A CN201910802731 A CN 201910802731A CN 110479686 A CN110479686 A CN 110479686A
- Authority
- CN
- China
- Prior art keywords
- filter plate
- solid
- oily sediment
- feeding device
- cage
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/04—Stationary flat screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/42—Drive mechanisms, regulating or controlling devices, or balancing devices, specially adapted for screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/46—Constructional details of screens in general; Cleaning or heating of screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B13/00—Accessories or details of general applicability for machines or apparatus for cleaning
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/02—Cleaning by the force of jets or sprays
- B08B3/022—Cleaning travelling work
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B3/00—Cleaning by methods involving the use or presence of liquid or steam
- B08B3/04—Cleaning involving contact with liquid
- B08B3/06—Cleaning involving contact with liquid using perforated drums in which the article or material is placed
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B2201/00—Details applicable to machines for screening using sieves or gratings
- B07B2201/04—Multiple deck screening devices comprising one or more superimposed screens
Abstract
The invention discloses a kind of solid-liquid separating methods for oily sediment recovery processing, belong to resource environment protection recycling field, a kind of solid-liquid separating method for oily sediment recovery processing, staff can pass through remote control stripper plate, oily sediment is resolved into the graininess of certain diameter by feeding device, convenient for the progress of subsequent rinse work, after the completion of oily sediment is cleaned, staff passes through control electric telescopic rod, the position of second filter plate and third filter plate in the vertical direction is adjusted, to carry out separate collection processing to the solid silt within the scope of different-diameter, rotation simultaneously picks up cage and passes through Stirring, leach the silt after rinsing more fully, the present invention is in cleaning, impurity in oily sediment can be classified according to diameter, later period sorting personnel are greatly reduced to waste recovery In operation, chance with hazardous waste close contact improves the safety of relevant staff.
Description
Technical field
The present invention relates to resource environment protection recycling field, more specifically to a kind of for oily sediment recovery processing
Solid-liquid separating method.
Background technique
Oil-containing mud sand is the major pollutants that Petroleum & Petrochemical Enterprises generate in oil exploitation, storage and transportation and refining process
One of, (for dry weight oil content generally 10% or more, majority also contains higher other organic matters up to 20%-30%)
And the poisonous and harmful substances such as metal inorganic salt.Many polycyclic hydrocarbon (PAH) have teratogenesis, mutagenicity and carcinogenic in oily sediment
Property, serious damage is brought to human health by directly or indirectly approach.Polycyclic aromatic hydrocarbon can mainly cause cutaneum carcinoma, lung cancer and
Gastric cancer, the main harm position to human body are respiratory tract and skin, and people are chronically in polycyclic aromatic hydrocarbons contaminated environment, can
Cause acute or chronic injury.It after certain harmful substances enter farmland, is absorbed by crops, people and dynamic plant is entered by food chain
In object, causes various diseases to occur, threaten the health of the mankind.Not only being made containing poly- waste air storage in oily sediment simultaneously
At the waste of resource, and contaminated soil and atmosphere, the more seriously migration infiltration of petroleum hydrocarbon in the soil, to underground water
It pollutes, aquatic ecosystem is made to wreck.
Therefore it is necessary to the processing recycling operation of oily sediment, in the prior art to the place of oily sediment
Reason step divides quinquepartite: separation of solid and liquid, water-oil separating, high press-dehydrating, broken simultaneously pyrocondensation granulating, the cigarette of rinsing of Recyclable are starched back
It receives and dedusting is discharged.The operating procedure being wherein separated by solid-liquid separation is general are as follows:
Step 1: upper bricklayer's cuts off big lump waste materials, waste material is manually loaded into hopper, ageing oil is sent into rotation and picked up by elevating hopper
Cage；
Step 2: ageing oil is rinsed out particulate matter on oil, there is sprinkler head flushing in front and back, pushes from front to back, hung by tooth
Play plastics etc.；
Step 3: the water in separation is heated to 80 DEG C -90 DEG C by heating room, the flue dust that heat in waste material is evaporated
Equal gas pollutants discharge, while aerator is picked up to rotation and is aerated in cage, and the oil float in waste material is gone out；
Step 4: the waste material not being recovered after cleaning pours into sorting room, different types of waste material is carried out by sorting personnel
Sorting.
In the existing operation to oily sediment, it is required to manually be operated in step 1 and step 4, and sludge containing
There are more harmful substances in sand, and if things go on like this, it is useless that the staff in step 1 and step 4 will receive oily sediment
It is carcinogenic seriously to can lead to relevant staff for the murder by poisoning of material.
Summary of the invention
1. technical problems to be solved
Aiming at the problems existing in the prior art, the purpose of the present invention is to provide one kind is recycled for oily sediment
Solid-liquid separating method, oily sediment can resolve into one by feeding device by remote control stripper plate by staff
Determine the graininess of diameter, convenient for the progress of subsequent rinse work, after the completion of oily sediment is cleaned, staff passes through control electricity
Dynamic telescopic rod, is adjusted the position of the second filter plate and third filter plate in the vertical direction, thus to different-diameter model
Solid silt in enclosing carries out separate collection processing, while rotation picks up cage by Stirring, fills the silt after rinsing more
The bleeding divided, the middle and later periods needs the mode manually sorted again compared to the prior art, and the present invention is during cleaning
Impurity in oily sediment is classified according to diameter, greatly reduces later period sorting personnel in the operation to waste recovery
In, the chance with hazardous waste close contact improves the safety of relevant staff.
2. technical solution
To solve the above problems, the present invention adopts the following technical scheme that.
A kind of solid-liquid separating method for oily sediment recovery processing, the operating procedure of solid-liquid separating method are as follows:
Step 1: staff first places untreated oily sediment on a moving belt, charging is passed through by conveyer belt
Mouth is moved in feeding device；
Step 2: staff starts stripper plate, oily sediment is pressed through and breaks up plate, the oily sediment of bulk is squeezed
It is pressed into fritter and is pushed to rotation and pick up in cage；
Step 3: staff's starting rotation picks up cage and starts rotary work, the sludge containing in cage is picked up to rotation by water pump
Sand is rinsed；
Step 4: staff controls the switch of electric telescopic rod according to the particle diameter of solid, to the second mistake
Filter plate, third filter plate position be adjusted；
Step 5: carrying out centralized collection to the particulate matter for the different-diameter picked up under dripping in cage from rotation and being discharged from slag notch
And it is discharged from slag notch；
Step 6: the water in separation is heated to 80 DEG C -90 DEG C by heating room, the flue dust that heat in waste material is evaporated
Equal gas pollutants discharge, while aerator is picked up to rotation and is aerated in cage, and the oil float in waste material is gone out；
Step 7: the waste material not being recovered after cleaning pours into sorting room, different types of waste material is carried out by sorting personnel
Sorting.
By aforesaid operations step, staff can be by remote control stripper plate, by feeding device by sludge containing
Sand resolves into the graininess of certain diameter, convenient for the progress of subsequent rinse work, after the completion of oily sediment is cleaned, staff
By controlling electric telescopic rod, the position of the second filter plate and third filter plate in the vertical direction is adjusted, thus right
Solid silt within the scope of different-diameter carries out separate collection processing, while rotation picks up cage by Stirring, makes after rinsing
Silt more fully leaches, and the middle and later periods needs the mode manually sorted again compared to the prior art, and the present invention is in cleaning
In the process, the impurity in oily sediment can be classified according to diameter, greatly reduces later period sorting personnel to waste material
In the operation of recycling, chance with hazardous waste close contact improves the safety of relevant staff.
Further, the stripper plate outer end in the step 2 is electrically connected with controller.
Further, the controller outer end is electrically connected with wireless transport module, the transmission of the wireless transport module
Mode is WIFI signal transmission.
Further, the feed inlet is located at the upper end of feeding device, and the feed inlet is mutually fixed with feeding device, described
Feeding device and water pump are interconnected, and the stripper plate slides in feeding device, can be by feeding under the action of stripper plate
Oily sediment in device, which is pressed through, breaks up plate, converts it into the tiny block convenient for water cleaning.
Further, the feeding device internal screw thread, which is connected with, breaks up plate, and two inner end walls are solid up and down for the feeding device
Surely it is connected with limited block, it is described to break up plate and limited block is mutually matched, plate is broken up with feeding device and is mutually threadedly coupled fixation, just
It is selected in staff according to the pore size that the actual conditions of oily sediment air exercise falls apart, while limited block plays air exercise
The additional reinforcement effect fallen apart.
Further, it is rotatably connected to rotation in the feeding device and picks up cage, the rotation is picked up cage outer end and is electrically connected with
Aerator, the rotation pick up cage and are fixedly connected with plastic block close to one end of feeding device, and the feeding device inner end wall is close
One end of plastic block, which is dug, card slot, and the card slot and plastic block are mutually matched, under the mating reaction of card slot and plastic block, energy
It enough fills up feeding device and gap between cage is picked up in rotation, when preventing from rotation from picking up cage rotating in feeding device, in feeding device
The water of oily sediment of being used to clean flowed out among gap.
Further, the rotation, which is picked up cage lower end and dug, scum hole, and the first filtering is fixedly connected in the scum hole
Plate slidably connects the second filter plate in the scum hole, slidably connects third filter plate, oil-containing in second filter plate
For silt in feeding device after the water cleaning that water pump sprays, rotation picks up cage by rotation further by bulky grain oily sediment
It breaks up, it can be made to pass through scum hole, and can be according to its script diameter to its centralized recovery.
Further, second filter plate and third filter plate upper end are fixedly connected to electric telescopic rod, electronic
Under the telescopic adjustment effect of telescopic rod, the position on the second filter plate and third filter plate vertical direction can be controlled respectively
System, the silt so as to achieve the purpose that different to diameter are collected respectively.
Further, the aperture of first filter plate, the second filter plate and third filter plate is sequentially reduced from bottom to up,
The silt that staff controls small diameter first is leaked out by third filter plate, the second filter plate and the first filter plate, then will
Third filter plate is removed out of second filter plate, and the silt for keeping diameter slightly larger is leaked out by the second filter plate and the first filter plate,
Finally the second filter plate is removed out of scum hole, the silt for keeping diameter bigger leaks out after the first filter plate.
Further, the electric telescopic rod and controller are electrically connected, and staff's air exercise can be made to fall apart and carried out far
Journey operation, reduces a possibility that staff is with oily sediment and its processing unit close contact, reduces staff
A possibility that being influenced by harmful substance in oily sediment.
3. beneficial effect
Compared with the prior art, the present invention has the advantages that
(1) in operation, staff can will be contained by remote control stripper plate by feeding device this programme
Oil sediment resolves into the graininess of certain diameter, convenient for the progress of subsequent rinse work, after the completion of oily sediment is cleaned, and work
Personnel are adjusted the position of the second filter plate and third filter plate in the vertical direction by control electric telescopic rod, from
And separate collection processing is carried out to the solid silt within the scope of different-diameter, while rotation picks up cage by Stirring, make to rinse
Silt afterwards more fully leaches, and the middle and later periods needs the mode manually sorted again compared to the prior art, and the present invention is clear
During washing, the impurity in oily sediment can be classified according to diameter, greatly reduce later period sorting personnel right
In the operation of waste recovery, chance with hazardous waste close contact improves the safety of relevant staff.
(2) the stripper plate outer end in step 2 is electrically connected with controller, and controller outer end is electrically connected with wireless transmission
Module, the transmission mode of wireless transport module are WIFI signal transmission.
(3) feed inlet is located at the upper end of feeding device, and feed inlet is mutually fixed with feeding device, and feeding device is mutual with water pump
Connection, stripper plate slides in feeding device, under the action of stripper plate, can squeeze the oily sediment in feeding device logical
It crosses and breaks up plate, convert it into the tiny block convenient for water cleaning.
(4) feeding device internal screw thread, which is connected with, breaks up plate, and two inner end walls are fixedly connected to limited block to feeding device up and down,
It breaks up plate and limited block is mutually matched, break up plate with feeding device and be mutually threadedly coupled fixation, convenient for staff according to oil-containing
The pore size that the actual conditions air exercise of silt falls apart is selected, while limited block plays the additional reinforcement that air exercise falls apart and makees
With.
(5) it is rotatably connected to rotation in feeding device and picks up cage, rotation picks up cage outer end and is electrically connected with aerator, and cage is picked up in rotation
It is fixedly connected with plastic block close to one end of feeding device, feeding device inner end wall is dug close to one end of plastic block card slot,
Card slot and plastic block are mutually matched, under the mating reaction of card slot and plastic block, can fill up feeding device and rotation pick up cage it
Between gap, when preventing rotation from picking up cage and rotate in feeding device, the water for being used to clean oily sediment in feeding device is from seam
Outflow among gap.
(6) rotation, which is picked up cage lower end and dug, scum hole, and the first filter plate, sliding in scum hole are fixedly connected in scum hole
It is connected with the second filter plate, third filter plate is slidably connected in the second filter plate, oily sediment passes through water in feeding device
After the water cleaning that pump sprays, rotation picks up cage and further breaks up bulky grain oily sediment by rotation, it can be made to pass through
Scum hole, and can be according to its script diameter to its centralized recovery.
(7) second filter plates and third filter plate upper end are fixedly connected to electric telescopic rod, in stretching for electric telescopic rod
Under contracting adjustment effect, the position on the second filter plate and third filter plate vertical direction can be controlled respectively, so as to
Enough achieve the purpose that the silt different to diameter is collected respectively.
The aperture of (8) first filter plates, the second filter plate and third filter plate is sequentially reduced from bottom to up, and staff is first
The silt for first controlling small diameter is leaked out by third filter plate, the second filter plate and the first filter plate, then by third filter plate
It is removed out of second filter plate, the silt for keeping diameter slightly larger is leaked out by the second filter plate and the first filter plate, finally by second
Filter plate is removed out of scum hole, and the silt for keeping diameter bigger leaks out after the first filter plate.
(9) electric telescopic rod and controller are electrically connected, and staff's air exercise can be made to fall apart and remotely operated, reduced
A possibility that staff is with oily sediment and its processing unit close contact, reduces staff by oily sediment
A possibility that interior harmful substance influences.
Detailed description of the invention
Fig. 1 is flow diagram of the invention；
Fig. 2 is the flow diagram of oily sediment recycling in the prior art；
Fig. 3 is the structural schematic diagram of equipment for separating liquid from solid in the prior art；
Fig. 4 is the elevation of feeding device part of the present invention；
Fig. 5 is the sectional front view of feeding device part of the present invention；
Fig. 6 is the structural schematic diagram that the present invention breaks up plate part；
Fig. 7 is the structural schematic diagram that cage part is picked up in present invention rotation；
Fig. 8 is structural schematic diagram at the A of Fig. 7；
Fig. 9 is the lateral sectional view when use of cage part is picked up in present invention rotation；
Figure 10 is the sectional front view when use of cage part is picked up in present invention rotation.
Figure label explanation:
Plate, 103 limited blocks, 104 card slots, 105 stripper plates, 2 transmission belts, 3 water are broken up in 1 feeding device, 101 feed inlets, 102
Cage, 601 plastic blocks, 602 electric telescopic rods, 603 first filter plates, 604 second mistakes are picked up in pump, 4 aerators, 5 heating rooms, 6 rotations
Filter plate, 605 third filter plates, 7 sorting rooms, 8 slag notches.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description；Obviously, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments, is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the instruction such as term " on ", "lower", "inner", "outside", " top/bottom end "
Orientation or positional relationship be based on the orientation or positional relationship shown in the drawings, be merely for convenience of description the present invention and simplification retouch
It states, rather than the device or element of indication or suggestion meaning must have a particular orientation, be constructed and operated in a specific orientation,
Therefore it is not considered as limiting the invention.In addition, term " first ", " second " are used for description purposes only, and cannot understand
For indication or suggestion relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation " " is set
Be equipped with ", " be arranged/connect ", " connection " etc., shall be understood in a broad sense, such as " connection ", may be a fixed connection, be also possible to removable
Connection is unloaded, or is integrally connected, can be mechanical connection, is also possible to be electrically connected, can be directly connected, it can also be in
Between medium be indirectly connected, can be the connection inside two elements, for the ordinary skill in the art, can be specific
Situation understands the concrete meaning of above-mentioned term in the present invention.
Embodiment 1:
A kind of solid-liquid separating method for oily sediment recovery processing, the operating procedure of solid-liquid separating method are as follows:
Step 1: staff first places untreated oily sediment on a moving belt, charging is passed through by conveyer belt
Mouth 101 is moved in feeding device 1；
Step 2: referring to Fig. 4, staff's starting stripper plate 105, oily sediment is pressed through and breaks up plate 102, is incited somebody to action
The oily sediment of bulk, which is squeezed into fritter and is pushed to rotation, to be picked up in cage 6；
Step 3: staff, which starts rotation, picks up the beginning rotary work of cage 6, the oil-containing in cage 6 is picked up by 3 pairs of water pump rotations
Silt is rinsed；
Step 4: staff controls the switch of electric telescopic rod 602 according to the particle diameter of solid, to second
Filter plate 604, third filter plate 605 position be adjusted；
Step 5: to the particulate matter progress centralized collection for picking up different-diameter drip in cage 6 under from rotation and from 8 row of slag notch
Out；
Step 6: the water in separation is heated to 80 DEG C -90 DEG C by heating room 5, the flue dust that heat in waste material is evaporated
Equal gas pollutants discharge, while aerator is picked up to rotation and is aerated in cage, and the oil float in waste material is gone out；
Step 7: the waste material not being recovered after cleaning pours into sorting room 7, different types of waste material is carried out by sorting personnel
Sorting.
By aforesaid operations step, staff can will be contained by remote control stripper plate 105 by feeding device 1
Oil sediment resolves into the graininess of certain diameter, convenient for the progress of subsequent rinse work, after the completion of oily sediment is cleaned, and work
Personnel by control electric telescopic rod 602, to the position of the second filter plate 604 and third filter plate 605 in the vertical direction into
Row is adjusted, to carry out separate collection processing to the solid silt within the scope of different-diameter, while rotation is picked up cage 6 and stirred by rotation
It mixes, leaches the silt after rinsing more fully, the middle and later periods needs the mode manually sorted again compared to the prior art, this
Invention can classify the impurity in oily sediment according to diameter during cleaning, greatly reduce later period sorting
Personnel are in the operation to waste recovery, and chance with hazardous waste close contact improves the safety of relevant staff
Property.
105 outer end of stripper plate in step 2 is electrically connected with controller, and controller outer end is electrically connected with wireless transmission
Module, the transmission mode of wireless transport module are WIFI signal transmission.
Fig. 4-5 is please referred to, feed inlet 101 is located at the upper end of feeding device 1, and feed inlet 101 is fixed with 1 phase of feeding device,
Feeding device 1 and water pump 3 are interconnected, and stripper plate 105 slides in feeding device 1.It, can under the action of stripper plate 105
Oily sediment in feeding device 1 is pressed through and breaks up plate 102, converts it into the tiny block convenient for water cleaning.Please
Refering to Fig. 5-6,1 internal screw thread of feeding device, which is connected with, breaks up plate 102, and about 1 two inner end wall of feeding device is fixedly connected with limited
Position block 103, breaks up plate 102 and limited block 103 is mutually matched.It breaks up plate 102 and is mutually threadedly coupled fixation with feeding device 1, just
It is selected in staff according to fall apart 102 pore size of the actual conditions of oily sediment air exercise, while limited block 103 rises
To air exercise fall apart 102 additional reinforcement effect.
It is rotatably connected to rotation in feeding device 1 and picks up cage 6, rotation picks up 6 outer end of cage and is electrically connected with aerator 4, and rotation is picked up
Cage 6 is fixedly connected with plastic block 601 close to one end of feeding device 1, and 1 inner end wall of feeding device is close to one end of plastic block 601
Cutting has card slot 104, and card slot 104 and plastic block 601 are mutually matched.Under the mating reaction of card slot 104 and plastic block 601, energy
It enough fills up feeding device 1 and gap between cage 6 is picked up in rotation, when preventing from rotation from picking up cage 6 rotating in feeding device 1, feeding dress
The water for being used to clean oily sediment set in 1 flows out among gap.Fig. 7-8 is please referred to, rotation, which picks up 6 lower end of cage and digs to have, slags tap
Hole is fixedly connected with the first filter plate 603 in scum hole, the second filter plate 604, the second filter plate is slidably connected in scum hole
Third filter plate 605 is slidably connected in 604.Oily sediment after the water cleaning that water pump 3 sprays, revolves in feeding device 1
Turn to pick up cage 6 and further break up bulky grain oily sediment by rotation, it can be made to pass through scum hole, and can be according to
Its script diameter is to its centralized recovery.
Second filter plate 604 and 605 upper end of third filter plate are fixedly connected to electric telescopic rod 602.In electric expansion
It, can be respectively to the position on 605 vertical direction of the second filter plate 604 and third filter plate under the telescopic adjustment effect of bar 602
It is controlled, the silt so as to achieve the purpose that different to diameter is collected respectively.First filter plate 603, the second mistake
The aperture of filter plate 604 and third filter plate 605 is sequentially reduced from bottom to up.Staff controls the silt warp of small diameter first
It crosses third filter plate 605, the second filter plate 604 and the first filter plate 603 to leak out, then third filter plate 605 is filtered from second
It is removed in plate 604, the silt for keeping diameter slightly larger is leaked out by the second filter plate 604 and the first filter plate 603, finally by the second mistake
Filter plate 604 is removed out of scum hole, and the silt for keeping diameter bigger leaks out after the filtering of the first filter plate 603.Electric telescopic rod
602 are electrically connected with controller.Staff's air exercise can be made to fall apart 102 to remotely operate, reduce staff and oil-containing
A possibility that silt and its processing unit close contact, reduce staff is influenced by harmful substance in oily sediment
A possibility that.
The foregoing is intended to be a preferred embodiment of the present invention；But scope of protection of the present invention is not limited thereto.
Anyone skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
It improves design and is subject to equivalent substitution or change, should be covered by the scope of protection of the present invention.
Claims (10)
1. a kind of solid-liquid separating method for oily sediment recovery processing, it is characterised in that: the operation of solid-liquid separating method walks
Suddenly are as follows:
Step 1: staff first places untreated oily sediment on a moving belt, feed inlet is passed through by conveyer belt
(101) it is moved in feeding device (1)；
Step 2: staff starts stripper plate (105), oily sediment is pressed through and breaks up plate (102), by the oil-containing of bulk
Silt, which is squeezed into fritter and is pushed to rotation, to be picked up in cage (6)；
Step 3: staff, which starts rotation, picks up cage (6) beginning rotary work, containing in cage (6) is picked up to rotation by water pump (3)
Oil sediment is rinsed；
Step 4: staff controls the switch of electric telescopic rod (602) according to the particle diameter of solid, to the second mistake
Filter plate (604), third filter plate (605) position be adjusted；
Step 5: carrying out centralized collection to the particulate matter for picking up the different-diameter in cage (6) under drip from rotation and being arranged from slag notch (8)
Out；
Step 6: the water in separation is heated to 80 DEG C -90 DEG C by heating room (5), the flue dust etc. that heat in waste material is evaporated
Gas pollutant discharge, while aerator is picked up in cage to rotation and is aerated, and the oil float in waste material is gone out；
Step 7: the waste material not being recovered after cleaning pours into sorting room (7), different types of waste material is divided by sorting personnel
It picks.
2. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 1, it is characterised in that: institute
Stripper plate (105) outer end stated in step 2 is electrically connected with controller.
3. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 2, it is characterised in that: institute
It states controller outer end and is electrically connected with wireless transport module, the transmission mode of the wireless transport module is WIFI signal transmission.
4. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 1, it is characterised in that: institute
State the upper end that feed inlet (101) is located at feeding device (1), the feed inlet (101) is mutually fixed with feeding device (1), it is described on
Expect that device (1) and water pump (3) is interconnected, the stripper plate (105) sliding in feeding device (1).
5. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 4, it is characterised in that: institute
It states feeding device (1) internal screw thread and is connected with and break up plate (102), two inner end walls are fixedly connected to the feeding device (1) up and down
Limited block (103), it is described to break up plate (102) and limited block (103) is mutually matched.
6. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 5, it is characterised in that: institute
It states and is rotatably connected to rotation in feeding device (1) and picks up cage (6), the rotation picks up cage (6) outer end and is electrically connected with aerator (4),
The rotation is picked up cage (6) and is fixedly connected with plastic block (601) close to the one end of feeding device (1), feeding device (1) inner end
Wall is dug close to one end of plastic block (601) to be had card slot (104), and the card slot (104) and plastic block (601) are mutually matched.
7. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 6, it is characterised in that: institute
Stating rotation and picking up cage (6) lower end and dig has scum hole, is fixedly connected in the scum hole the first filter plate (603), described to slag tap
It is slidably connected in hole the second filter plate (604), slidably connects third filter plate (605) in second filter plate (604).
8. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 1, it is characterised in that: institute
It states the second filter plate (604) and third filter plate (605) upper end is fixedly connected to electric telescopic rod (602).
9. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 7, it is characterised in that: institute
The aperture for stating the first filter plate (603), the second filter plate (604) and third filter plate (605) is sequentially reduced from bottom to up.
10. a kind of solid-liquid separating method for oily sediment recovery processing according to claim 1, it is characterised in that:
The electric telescopic rod (602) and controller are electrically connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910802731.0A CN110479686B (en) | 2019-08-28 | 2019-08-28 | Solid-liquid separation method for oil-containing silt recovery treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910802731.0A CN110479686B (en) | 2019-08-28 | 2019-08-28 | Solid-liquid separation method for oil-containing silt recovery treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110479686A true CN110479686A (en) | 2019-11-22 |
| CN110479686B CN110479686B (en) | 2021-06-15 |
Family
ID=68554832
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910802731.0A Active CN110479686B (en) | 2019-08-28 | 2019-08-28 | Solid-liquid separation method for oil-containing silt recovery treatment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110479686B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112024357A (en) * | 2020-07-17 | 2020-12-04 | 深圳市鹏城基业混凝土有限公司 | Polluted recycled aggregate treatment system and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1130021A (en) * | 1965-02-23 | 1968-10-09 | R & H Green And Silley Weir Lt | Methods for removing heavy oil from silt and other solids which collect in heavy oil tanks |
| CN102849906A (en) * | 2012-05-18 | 2013-01-02 | 北京航天试验技术研究所 | Oil sludge separation apparatus and separation method |
| CN206244620U (en) * | 2016-11-10 | 2017-06-13 | 杜远华 | A kind of petrochemical industry oil-sludge treatment device |
| CN109020118A (en) * | 2018-08-30 | 2018-12-18 | 中国石油天然气集团有限公司 | High height containing sand glues oily sludge preprocess method and pretreatment system |
| CN208995443U (en) * | 2018-10-12 | 2019-06-18 | 珠海巨涛海洋石油服务有限公司 | A kind of greasy filth sand separating apparatus |
| CN209052558U (en) * | 2018-10-22 | 2019-07-02 | 盘锦宏博石油科技服务有限公司 | High pressure hot-water cleaning machine is used in a kind of processing of ground sludge |
-
2019
- 2019-08-28 CN CN201910802731.0A patent/CN110479686B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1130021A (en) * | 1965-02-23 | 1968-10-09 | R & H Green And Silley Weir Lt | Methods for removing heavy oil from silt and other solids which collect in heavy oil tanks |
| CN102849906A (en) * | 2012-05-18 | 2013-01-02 | 北京航天试验技术研究所 | Oil sludge separation apparatus and separation method |
| CN206244620U (en) * | 2016-11-10 | 2017-06-13 | 杜远华 | A kind of petrochemical industry oil-sludge treatment device |
| CN109020118A (en) * | 2018-08-30 | 2018-12-18 | 中国石油天然气集团有限公司 | High height containing sand glues oily sludge preprocess method and pretreatment system |
| CN208995443U (en) * | 2018-10-12 | 2019-06-18 | 珠海巨涛海洋石油服务有限公司 | A kind of greasy filth sand separating apparatus |
| CN209052558U (en) * | 2018-10-22 | 2019-07-02 | 盘锦宏博石油科技服务有限公司 | High pressure hot-water cleaning machine is used in a kind of processing of ground sludge |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112024357A (en) * | 2020-07-17 | 2020-12-04 | 深圳市鹏城基业混凝土有限公司 | Polluted recycled aggregate treatment system and method |
| CN112024357B (en) * | 2020-07-17 | 2022-11-15 | 深圳市鹏城基业混凝土有限公司 | Polluted recycled aggregate treatment system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110479686B (en) | 2021-06-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102601106B (en) | Ectopic leaching restoring device and restoring method for chromic slag polluted soil | |
| US4836611A (en) | Method and apparatus for drilling and separating | |
| WO2007100805A1 (en) | Hydrogen sulfide treatment system | |
| US20140014589A1 (en) | Method for cleaning drilling fluid in rock sampling drilling and a cleaning unit | |
| CN106583436A (en) | Leaching method for remediating hexavalent chromium contaminated soil | |
| KR101915030B1 (en) | Drum type heavy metal release reactor for remediation of complex contaminated soils | |
| CN214076889U (en) | Pollute soil prosthetic devices | |
| CN108059311A (en) | A kind of mixing disposal of oily sludge system and method | |
| CN110479686A (en) | A kind of solid-liquid separating method for oily sediment recovery processing | |
| CN112321052A (en) | Multistage reciprocating type environment-friendly sewage treatment device | |
| CN106583438A (en) | Remediation system and method for poisonous and harmful soil | |
| CN204310925U (en) | Oil-containing solid waste indirect heating thermal desorption treatment unit | |
| KR101915035B1 (en) | Remediation of complex contaminated soils comprising drum type heavy metal release reactor | |
| CN211245666U (en) | Leachate solid-liquid separation device | |
| CN110204157B (en) | Oil sludge treatment process | |
| CN115634920B (en) | Integrated extraction device for extracting various heavy metals in soil | |
| KR200406313Y1 (en) | Cleaning apparatus sand of sewage and waste water | |
| CN108862678A (en) | Rainwater filtration equipment | |
| CN210543506U (en) | Oil-water separator | |
| JP4061327B2 (en) | Sludge treatment equipment | |
| CN110026426B (en) | Organic contaminated site soil remediation method | |
| US4834783A (en) | Rotary separator | |
| CN209635958U (en) | A kind of integration blowdown apparatus | |
| CN203741273U (en) | Agent room-temperature deep desorption reactor for recycling base oil from discarded oil-based drilling waste | |
| CN113521850A (en) | Mixed effluent treatment plant of oil field well drilling abandonment drilling fluid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |