CN110479686B - Solid-liquid separation method for oil-containing silt recovery treatment - Google Patents

Solid-liquid separation method for oil-containing silt recovery treatment Download PDF

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Publication number
CN110479686B
CN110479686B CN201910802731.0A CN201910802731A CN110479686B CN 110479686 B CN110479686 B CN 110479686B CN 201910802731 A CN201910802731 A CN 201910802731A CN 110479686 B CN110479686 B CN 110479686B
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filter plate
feeding device
solid
oily
liquid separation
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CN110479686A (en
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周春松
余云丰
胡成坤
贾建洪
王荔
孙坚
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Yixing International Environmental Protection Technology Development Co ltd
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Yixing International Environmental Protection Technology Development Co ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/04Stationary flat screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/42Drive mechanisms, regulating or controlling devices, or balancing devices, specially adapted for screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B1/00Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
    • B07B1/46Constructional details of screens in general; Cleaning or heating of screens
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B13/00Accessories or details of general applicability for machines or apparatus for cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/02Cleaning by the force of jets or sprays
    • B08B3/022Cleaning travelling work
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/06Cleaning involving contact with liquid using perforated drums in which the article or material is placed
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/40Devices for separating or removing fatty or oily substances or similar floating material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING 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
    • B07B2201/00Details applicable to machines for screening using sieves or gratings
    • B07B2201/04Multiple deck screening devices comprising one or more superimposed screens

Abstract

The invention discloses a solid-liquid separation method for recovering and treating oily sediment, which belongs to the field of resource environmental protection recovery, and the solid-liquid separation method for recovering and treating the oily sediment comprises the steps that a worker can remotely control an extrusion plate, the oily sediment is decomposed into particles with a certain diameter through a feeding device, the subsequent washing work is convenient to carry out, after the oily sediment is washed, the worker can adjust the positions of a second filter plate and a third filter plate in the vertical direction by controlling an electric telescopic rod, so that the solid sediment within different diameter ranges can be separately collected and treated, meanwhile, a rotary picking cage can enable the washed sediment to be more fully leached through rotary stirring, impurities in the oily sediment can be classified according to the diameter during washing, the later-stage sorting personnel can be greatly reduced in the operation of waste recovery, the opportunity for close contact with hazardous waste improves the safety of the associated personnel.

Description

Solid-liquid separation method for oil-containing silt recovery treatment
Technical Field
The invention relates to the field of resource environment-friendly recovery, in particular to a solid-liquid separation method for recovery treatment of oil-containing silt.
Background
The oil-containing silt is one of main pollutants generated in petroleum exploitation, storage and transportation and refining processes of petroleum and petrochemical enterprises, (the oil content of dry weight is generally more than 10%, and most of dry weight can reach 20% -30%), and simultaneously, the oil-containing silt also contains higher toxic and harmful substances such as other organic matters, metal inorganic salts and the like. Many polycyclic hydrocarbons (PAH) in oily silt have teratogenicity, mutagenicity and carcinogenicity, and bring serious damage to human health through direct and indirect approaches. Polycyclic aromatic hydrocarbons can mainly cause skin cancer, lung cancer and stomach cancer, the main harm parts of the polycyclic aromatic hydrocarbons to human bodies are respiratory tracts and skins, and people can cause acute or chronic injury when being in the polycyclic aromatic hydrocarbon polluted environment for a long time. After entering farmland, some harmful substances are absorbed by crops and enter human bodies, animals and plants through food chains, so that various diseases occur and the health of human beings is threatened. Meanwhile, the polymer-containing waste in the oily sediment is stacked in the open air, so that not only is the resource waste caused, but also the soil and the atmosphere are polluted, and more seriously, the migration and the permeation of petroleum hydrocarbon in the soil pollute underground water, so that an aquatic ecosystem is damaged.
Therefore, the treatment and recovery operation of the oily sediment is very necessary, and the treatment steps of the oily sediment in the prior art are divided into five parts: solid-liquid separation, oil-water separation, high-pressure dehydration, crushing and washing of recoverable substances, thermal shrinkage granulation, recovery of tobacco pulp, dust removal and discharge. The solid-liquid separation operation steps are as follows:
firstly, a trowel loader cuts off large waste materials, the trowel loader manually loads the waste materials into a hopper, and the hopper feeds aging oil into a rotary picking cage;
washing off particles on the aging oil, washing by water nozzles in front and back, pushing from front to back, and hanging plastics by teeth;
step three, heating the water in the separation to 80-90 ℃ through a heating chamber, discharging gas pollutants such as smoke dust and the like evaporated in the waste material when meeting heat, and aerating in a rotary picking cage by an aerator to float oil in the waste material;
and step four, pouring the waste which is not recycled after cleaning into a sorting room, and sorting different types of waste by sorting personnel.
In the prior operation of the oily sediment, the operation is carried out manually in the first step and the fourth step, and more harmful substances exist in the oily sediment.
Disclosure of Invention
1. Technical problem to be solved
Aiming at the problems in the prior art, the invention aims to provide a solid-liquid separation method for recovering and treating oily sediment, a worker can remotely control an extrusion plate to decompose the oily sediment into particles with a certain diameter through a feeding device, so that the subsequent washing work is convenient to carry out, after the oily sediment is cleaned, the worker can control an electric telescopic rod to adjust the vertical positions of a second filter plate and a third filter plate so as to separately collect and treat the solid sediment within different diameter ranges, and meanwhile, a rotary picking cage can lead the washed sediment to be more fully leached through rotary stirring, compared with the mode of manually sorting again in the middle and later periods of the prior art, the method can classify impurities in the oily sediment according to the diameter in the cleaning process, thereby greatly reducing the operation of the later-period sorting personnel on waste recovery, the opportunity for close contact with hazardous waste improves the safety of the associated personnel.
2. Technical scheme
In order to solve the above problems, the present invention adopts the following technical solutions.
A solid-liquid separation method for recovering and treating oily sediment comprises the following operation steps:
firstly, an operator places untreated oily silt on a conveyor belt and moves the untreated oily silt into a feeding device through a feed inlet by the conveyor belt, the feed inlet is positioned at the upper end of the feeding device, the feed inlet is fixed with the feeding device, the feeding device is communicated with a water pump, an extrusion plate slides in the feeding device, a scattering plate is connected with an internal thread of the feeding device, the upper and lower inner end walls of the feeding device are fixedly connected with limit blocks, the scattering plate and the limit blocks are matched with each other, a rotary picking cage is rotationally connected in the feeding device, the outer end of the rotary picking cage is electrically connected with an aerator, one end of the rotary picking cage close to the feeding device is fixedly connected with a plastic block, one end of the inner end wall of the feeding device close to the plastic block is provided with a clamping groove, the clamping groove is matched with the plastic block, and the lower end of the rotary picking cage is provided with a slag hole, a first filter plate is fixedly connected in the slag hole, a second filter plate is connected in the slag hole in a sliding manner, a third filter plate is connected in the second filter plate in a sliding manner, and electric telescopic rods are fixedly connected to the upper ends of the second filter plate and the third filter plate;
secondly, starting the extrusion plate by a worker, extruding the oily sediment through the scattering plate, extruding the large oily sediment into small blocks and pushing the small blocks into the rotary picking cage;
thirdly, starting the rotary picking cage by a worker to start to rotate, and washing the oily sediment in the rotary picking cage through a water pump;
fourthly, controlling a switch of the electric telescopic rod by a worker according to the diameter of solid particles, and adjusting the positions of the second filter plate and the third filter plate;
collecting particles with different diameters which are drained from the rotary picking cage in a centralized manner, discharging the particles from a slag outlet and discharging the particles from the slag outlet;
step six, heating the water in the separation to 80-90 ℃ through a heating chamber, discharging smoke dust evaporated in the waste material when meeting heat, and aerating the rotary picking cage by an aerator to float oil in the waste material;
and step seven, pouring the waste which is not recycled after cleaning into a sorting room, and sorting different types of waste by sorting personnel.
Through the operation steps, the working personnel can decompose the oily sediment into particles with certain diameter through the feeding device by remotely controlling the extrusion plate, so that the subsequent washing work is convenient to carry out, after the oily sediment is cleaned, the working personnel control the electric telescopic rod, the positions of the second filter plate and the third filter plate in the vertical direction are adjusted, so that the solid silt in different diameter ranges is separately collected and treated, meanwhile, the rotary picking cage can drain the washed silt more fully through rotary stirring, compared with the mode of manually sorting again in the middle and later periods of the prior art, in the cleaning process of the invention, can classify the impurity in the oily silt according to the diameter, the later stage letter sorting personnel that have significantly reduced in the operation to waste recovery, closely contacted opportunity with harmful waste material, improved relevant staff's security.
Furthermore, the outer end of the extrusion plate in the second step is electrically connected with a controller.
Furthermore, the outer end of the controller is electrically connected with a wireless transmission module, and the transmission mode of the wireless transmission module is WIFI signal transmission.
Further, supreme reducing in proper order is followed down to the aperture of first filter, second filter and third filter, and the staff spills through third filter, second filter and first filter at first controlling the silt of less diameter, shifts out the third filter from the second filter again, makes the diameter silt slightly bigger spill through second filter and first filter, at last with the second filter from the downthehole removal of slagging tap, make the diameter silt bigger spill after first filter filters.
Further, electric telescopic handle and controller electric connection can make the staff carry out remote operation to breaking up the board, reduce the staff and contain oily silt and the closely contacted possibility of processing apparatus with it, have reduced the possibility that the staff receives harmful substance influence in the oily silt.
3. Advantageous effects
Compared with the prior art, the invention has the advantages that:
(1) in the operation process of the scheme, a worker can control the extrusion plate remotely, the oily sediment is decomposed into particles with a certain diameter by the feeding device, so that the subsequent flushing work is convenient to carry out, and after the oily sediment is cleaned, a worker controls the electric telescopic rod, the positions of the second filter plate and the third filter plate in the vertical direction are adjusted, so that the solid silt in different diameter ranges is separately collected and treated, meanwhile, the rotary picking cage can drain the washed silt more fully through rotary stirring, compared with the mode of manually sorting again in the middle and later periods of the prior art, in the cleaning process of the invention, can classify the impurity in the oily silt according to the diameter, the later stage letter sorting personnel that have significantly reduced in the operation to waste recovery, closely contacted opportunity with harmful waste material, improved relevant staff's security.
(2) And electrically connecting the outer end of the extrusion plate in the second step with a controller, electrically connecting the outer end of the controller with a wireless transmission module, and transmitting the wireless transmission module in a WIFI signal transmission mode.
(3) The feed inlet is located loading attachment's upper end, and the feed inlet is fixed mutually with loading attachment, and loading attachment communicates each other with the water pump, and the stripper plate slides in loading attachment, under the effect of stripper plate, can be with the extrusion of the oily silt in the loading attachment through break up the board, change it into the tiny bulk thing of being convenient for water washing.
(4) The internal thread of the feeding device is connected with the scattering plate, the limiting blocks are fixedly connected to the upper inner end wall and the lower inner end wall of the feeding device, the scattering plate and the limiting blocks are matched with each other, the scattering plate is fixedly connected with the feeding device through threads, workers can conveniently select the aperture size of the scattering plate according to the actual situation of oily sediment, and meanwhile the limiting blocks play a role in assisting reinforcement of the scattering plate.
(5) The cage is picked up in the loading attachment internal rotation is connected with the rotation, the cage outer end electric connection is picked up in the rotation has the aeration machine, the cage is picked up in the rotation is close to loading attachment's one end fixedly connected with plastic piece, the one end that the end wall is close to the plastic piece in the loading attachment is dug there is the draw-in groove, draw-in groove and plastic piece match each other, under the mating reaction of draw-in groove and plastic piece, can fill up the gap between the cage is picked up in loading attachment and rotation, prevent that the cage is picked up in the rotation when the loading attachment internal rotation, the water that is used for wasing oily silt in the loading attachment flows out in.
(6) The rotatory cage lower extreme of picking up is dug there is the hole of slagging tap, the first filter of the downthehole fixedly connected with of slagging tap, it has the second filter to slag tap downthehole sliding connection, sliding connection has the third filter in the second filter, after oil-bearing silt is washd through water pump spun water in loading attachment, the rotatory cage of picking up is further broken up large granule oil-bearing silt through the rotation, can make it smoothly through the hole of slagging tap to can concentrate the recovery to it according to its original diameter size.
(7) The equal fixedly connected with electric telescopic handle in second filter and third filter upper end, under electric telescopic handle's flexible regulation effect, can control the position of second filter and the vertical side of third filter respectively to can reach the purpose of collecting respectively the silt of difference in diameter.
(8) The aperture of first filter, second filter and third filter is followed supreme the reducing in proper order down, and the staff at first controls the silt of less diameter through the third filter, second filter and first filter spill, shifts out the third filter from the second filter in again, makes the diameter slightly bigger silt spill through second filter and first filter, at last with the second filter from slagging tap downthehole shifting out, make the diameter bigger silt spill after first filter filters.
(9) Electric telescopic handle and controller electric connection can make the staff carry out remote operation to breaking up the board, reduce the staff and contain oil silt and the closely contacted possibility of processing apparatus with it, have reduced the possibility that the staff receives harmful substance influence in the oil silt.
Drawings
FIG. 1 is a block flow diagram of the present invention;
FIG. 2 is a block diagram of a process for recovering oily silt in the prior art;
FIG. 3 is a schematic structural diagram of a solid-liquid separation apparatus in the prior art;
FIG. 4 is an elevational view of a loading assembly portion of the present invention;
FIG. 5 is an elevational, cross-sectional view of a portion of the loading apparatus of the present invention;
FIG. 6 is a schematic structural view of a breaker portion of the present invention;
FIG. 7 is a schematic view of the rotary pick cage portion of the present invention;
FIG. 8 is a schematic view of the structure at A of FIG. 7;
FIG. 9 is a side cross-sectional view of the rotating pick cage portion of the present invention in use;
FIG. 10 is an elevational, cross-sectional view of the rotating pick cage portion of the present invention in use.
The reference numbers in the figures illustrate:
1 feeding device, 101 feed inlets, 102 break board, 103 stopper, 104 draw-in groove, 105 stripper plate, 2 drive belts, 3 water pumps, 4 aeration machines, 5 heating chambers, 6 rotatory cages, 601 plastic piece, 602 electric telescopic handle, 603 first filter, 604 second filter, 605 third filter, 7 letter sorting rooms, 8 slag notch.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention; it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and all other embodiments obtained by those skilled in the art without any inventive work are within the scope of the present invention.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "top/bottom", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should be noted that, unless otherwise specifically stated or limited, the terms "mounted," "disposed," "sleeved/connected," "connected," and the like are used in a broad sense, and for example, "connected" may be a fixed connection, a detachable connection, an integral connection, a mechanical connection, an electrical connection, a direct connection, an indirect connection through an intermediate medium, and a communication between two elements.
Example 1:
a solid-liquid separation method for recovering and treating oily sediment comprises the following operation steps:
firstly, placing untreated oily silt on a conveyor belt by a worker, and moving the untreated oily silt into a feeding device 1 through a feeding hole 101 by the conveyor belt;
step two, referring to fig. 4, the worker starts the extrusion plate 105 to extrude the oily sediment through the scattering plate 102, and extrudes the large oily sediment into small blocks to push the small blocks into the rotary picking cage 6;
thirdly, starting the rotary picking cage 6 by a worker to start rotary work, and washing the oily sediment in the rotary picking cage 6 through the water pump 3;
fourthly, the worker controls the switch of the electric telescopic rod 602 according to the diameter of the solid particles, and adjusts the positions of the second filter plate 604 and the third filter plate 605;
collecting particles with different diameters drained from the rotary picking cage 6 in a centralized manner and discharging the particles from a slag outlet 8;
step six, heating the water in the separation to 80-90 ℃ through a heating chamber 5, discharging smoke dust evaporated in the waste material when meeting heat, and aerating the rotary picking cage by an aerator to float oil in the waste material;
and step seven, pouring the waste which is not recycled after cleaning into a sorting chamber 7, and sorting different types of waste by sorting personnel.
Through the operation steps, the worker can remotely control the extrusion plate 105 to decompose the oily sediment into particles with a certain diameter through the feeding device 1, the subsequent washing work is convenient to carry out, after the oily sediment is washed, the worker can control the electric telescopic rod 602 to adjust the positions of the second filter plate 604 and the third filter plate 605 in the vertical direction, so that the solid sediment in different diameter ranges can be separately collected and treated, meanwhile, the rotary picking cage 6 can lead the washed sediment to be more fully leached through rotary stirring, compared with the mode of manual re-sorting in the later period in the prior art, the invention can classify the impurities in the oily sediment according to the diameter in the washing process, thereby greatly reducing the possibility that the sorting personnel in the later period can be in close contact with harmful waste in the operation of waste recovery, the safety of related workers is improved.
And in the second step, the outer end of the extrusion plate 105 is electrically connected with a controller, the outer end of the controller is electrically connected with a wireless transmission module, and the transmission mode of the wireless transmission module is WIFI signal transmission.
Referring to fig. 4-5, the feeding hole 101 is located at the upper end of the feeding device 1, the feeding hole 101 is fixed to the feeding device 1, the feeding device 1 is communicated with the water pump 3, and the extrusion plate 105 slides in the feeding device 1. The oily sediment in the loading device 1 can be pressed through the dispersing plate 102 by the pressing plate 105, and is converted into fine blocks which are convenient for water cleaning. Referring to fig. 5-6, the feeding device 1 is connected with a scattering plate 102 through an internal thread, the upper and lower inner end walls of the feeding device 1 are fixedly connected with a limiting block 103, and the scattering plate 102 and the limiting block 103 are matched with each other. The mutual threaded connection of board 102 and loading attachment 1 of breaing up is fixed, and the staff of being convenient for selects the aperture size of board 102 of breaing up according to the actual conditions of oiliness silt, and stopper 103 plays the supplementary reinforcing effect to board 102 of breaing up simultaneously.
Cage 6 is picked up in the rotation of loading attachment 1, and cage 6 outer end electric connection is picked up in the rotation has aerator 4, and cage 6 is picked up in the rotation is close to loading attachment 1's one end fixedly connected with plastic piece 601, and the chisel has draw-in groove 104, draw-in groove 104 and plastic piece 601 and match each other in the one end that loading attachment 1 inner endwall is close to plastic piece 601. Under the cooperation of draw-in groove 104 and plastic piece 601, can fill up the gap between loading attachment 1 and the rotatory cage 6 of picking up, prevent that rotatory cage 6 of picking up when loading attachment 1 internal rotation, the water that is used for wasing oiliness silt in the loading attachment 1 flows out from the middle of the gap. Referring to fig. 7-8, the lower end of the rotary pick-up cage 6 is drilled with a slag hole, a first filter plate 603 is fixedly connected in the slag hole, a second filter plate 604 is slidably connected in the slag hole, and a third filter plate 605 is slidably connected in the second filter plate 604. After the oily silt is cleaned through 3 spun water of water pump in loading attachment 1, cage 6 is picked up in the rotation further breaks up the oily silt of large granule through the rotation, can make it smoothly through the slag hole to can concentrate its recovery according to its original diameter size.
The upper ends of the second filter plate 604 and the third filter plate 605 are fixedly connected with an electric telescopic rod 602. Under the flexible adjustment effect of electric telescopic handle 602, can control the position of second filter 604 and third filter 605 vertical side respectively to can reach the purpose of collecting respectively the silt of difference in diameter. The pore diameters of the first filter plate 603, the second filter plate 604, and the third filter plate 605 decrease in order from bottom to top. The staff firstly controls the silt of less diameter to spill through third filter 605, second filter 604 and first filter 603, shifts out third filter 605 from second filter 604 again, makes the diameter silt slightly bigger spill through second filter 604 and first filter 603, and it is downthehole to follow the downthehole removal of slagging tap with second filter 604 at last, makes the diameter silt bigger spill after first filter 603 filters. The electric telescopic rod 602 is electrically connected to the controller. The scattering plate 102 can be remotely operated by workers, the possibility that the workers are in close contact with oily sediment and the treatment device of the oily sediment is reduced, and the possibility that the workers are influenced by harmful substances in the oily sediment is reduced.
The foregoing is only a preferred embodiment of the present invention; the scope of the invention is not limited thereto. Any person skilled in the art should be able to cover the technical scope of the present invention by equivalent or modified solutions and modifications within the technical scope of the present invention.

Claims (5)

1. A solid-liquid separation method for recovery treatment of oil-containing silt is characterized by comprising the following steps: the solid-liquid separation method comprises the following operation steps:
firstly, an operator places untreated oily silt on a conveyor belt and moves the untreated oily silt into a feeding device (1) through a feeding hole (101) by the conveyor belt, the feeding hole (101) is positioned at the upper end of the feeding device (1), the feeding hole (101) is fixed with the feeding device (1), the feeding device (1) is communicated with a water pump (3), an extrusion plate (105) slides in the feeding device (1), a scattering plate (102) is connected with an inner thread of the feeding device (1), the upper and lower inner end walls of the feeding device (1) are fixedly connected with a limiting block (103), the scattering plate (102) and the limiting block (103) are matched with each other, a rotary picking cage (6) is rotationally connected in the feeding device (1), the outer end of the rotary picking cage (6) is electrically connected with an aerator (4), one end of the rotary picking cage (6) close to the feeding device (1) is fixedly connected with a plastic block (601), a clamping groove (104) is formed in one end, close to the plastic block (601), of the inner end wall of the feeding device (1), the clamping groove (104) is matched with the plastic block (601), a slag hole is formed in the lower end of the rotary picking cage (6), a first filter plate (603) is fixedly connected in the slag hole, a second filter plate (604) is connected in the slag hole in a sliding mode, a third filter plate (605) is connected in the second filter plate (604) in a sliding mode, and electric telescopic rods (602) are fixedly connected to the upper ends of the second filter plate (604) and the third filter plate (605);
secondly, the staff starts the extrusion plate (105), extrudes the oily sediment through the scattering plate (102), extrudes the massive oily sediment into small blocks and pushes the small blocks into the rotary picking cage (6);
thirdly, starting the rotary picking cage (6) by a worker to start to rotate, and washing the oily sediment in the rotary picking cage (6) through the water pump (3);
fourthly, controlling the switch of the electric telescopic rod (602) by workers according to the diameter of solid particles, and adjusting the positions of the second filter plate (604) and the third filter plate (605);
fifthly, collecting the particles with different diameters which are drained from the rotary picking cage (6) in a centralized manner and discharging the particles from a slag outlet (8);
step six, heating the water in the separation to 80-90 ℃ through a heating chamber (5), discharging smoke dust evaporated in the waste after being heated, and aerating the rotary picking cage by an aerator to float oil in the waste;
and step seven, the waste which is not recycled after cleaning is poured into a sorting chamber (7), and sorting personnel sorts the waste of different types.
2. The solid-liquid separation method for recovering and treating oily sediment according to claim 1, characterized in that: and the outer end of the extrusion plate (105) in the second step is electrically connected with a controller.
3. The solid-liquid separation method for recovering and treating oily sediment according to claim 2, characterized in that: the outer end of the controller is electrically connected with a wireless transmission module, and the transmission mode of the wireless transmission module is WIFI signal transmission.
4. The solid-liquid separation method for recovering and treating oily sediment according to claim 1, characterized in that: the aperture of the first filter plate (603), the aperture of the second filter plate (604) and the aperture of the third filter plate (605) are sequentially reduced from bottom to top.
5. The solid-liquid separation method for recovering and treating oily sediment according to claim 1, characterized in that: the electric telescopic rod (602) is electrically connected with the controller.
CN201910802731.0A 2019-08-28 2019-08-28 Solid-liquid separation method for oil-containing silt recovery treatment Active CN110479686B (en)

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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

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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
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