CN114751494B - Sediment separation device and method - Google Patents

Sediment separation device and method Download PDF

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Publication number
CN114751494B
CN114751494B CN202210408251.8A CN202210408251A CN114751494B CN 114751494 B CN114751494 B CN 114751494B CN 202210408251 A CN202210408251 A CN 202210408251A CN 114751494 B CN114751494 B CN 114751494B
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sediment
reaction chamber
water
separation device
treated
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CN114751494A (en
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赵敏
郭兴建
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China University of Petroleum Beijing
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China University of Petroleum Beijing
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    • 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
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The invention discloses a sediment separation device and a sediment separation method. The invention provides a sediment separation device, which comprises a main shell, a deposition piece and a stripping assembly; the inside of the main shell encloses a reaction chamber, the side wall of the main shell is provided with a plurality of water injection ports for injecting liquid to be treated, and the bottom of the main shell is provided with a water outlet which can be opened and closed; the deposition part is movably suspended in the reaction chamber to deposit sediment in the liquid to be treated; the stripping assembly includes an impeller rotatably disposed below the depositing member, and the impeller is configured to rotate under the impact of water flow from the water inlet and to impinge on the depositing member to strip sediment deposited on the depositing member from the surface of the depositing member. The invention provides a sediment separation device and a sediment separation method, which can save cost.

Description

Sediment separation device and method
Technical Field
The invention relates to the field of oilfield exploitation, in particular to a sediment separation device and method.
Background
In the middle and later stages of oil field exploitation, as the energy of an oil layer is continuously consumed, the pressure of the oil layer is continuously reduced, so that underground crude oil is largely degassed, the viscosity is increased, the oil well yield is greatly reduced, even the spraying and the production stopping are carried out, and a large amount of dead oil remains in the underground and cannot be exploited. In order to compensate for the underground deficiency caused by the crude oil extraction, the pressure of an oil layer is maintained or increased, the high and stable yield of an oil field is realized, the higher recovery ratio is obtained, and the oil field is generally injected with water. However, the stratum is rich in a large amount of minerals, and in order to save water resources, water injected into the stratum is pumped to the ground by mixing with crude oil and is generally injected into the stratum again after oil-water separation, so that the content of the minerals in the water injected into the stratum is increased, deposits such as scale and the like are easily formed on the inner wall of the oil pipe, and the passage of the oil pipe is reduced due to the existence of the scale or other deposits, so that the conveying efficiency of the crude oil is affected.
In the prior art, corresponding scale inhibitors are generally added into water injected into stratum according to the mineral substance type contained in the oil field so as to prevent the formation of sediment, thereby protecting the oil pipe.
However, not only are the scale inhibitors expensive, but because the amount of water injected into the subsurface tends to be large, the amount of scale inhibitor required is also large, further increasing the cost of scale removal.
Disclosure of Invention
In order to solve at least one of the problems mentioned in the background art, the present invention provides a sediment separation device and method, which can save cost.
In order to achieve the above object, the present invention provides the following technical solutions:
in a first aspect, the present invention provides a sediment separation assembly comprising a main housing, a sediment element, and a stripping assembly; the inside of the main shell encloses a reaction chamber, the side wall of the main shell is provided with a plurality of water injection ports for injecting liquid to be treated, and the bottom of the main shell is provided with a water outlet which can be opened and closed; the deposition part is movably suspended in the reaction chamber to deposit sediment in the liquid to be treated; the stripping assembly includes an impeller rotatably disposed below the depositing member, and the impeller is configured to rotate under the impact of water flow from the water inlet and to impinge on the depositing member to strip sediment deposited on the depositing member from the surface of the depositing member.
As an alternative embodiment, the main casing is a revolution body, and the plurality of water filling ports are uniformly arranged along the circumferential direction of the main casing.
As an alternative embodiment, the orientation of the water injection ports and the central axis of the reaction chamber are staggered, so that the liquid to be treated injected from the water injection ports forms vortex in the reaction chamber.
As an alternative implementation mode, the deposition piece is a hollow steel pipe hung in the reaction chamber, the bottom of the deposition piece is arranged in a suspending mode, and a plurality of through holes are formed in the side wall of the deposition piece.
As an alternative implementation mode, the upper end of the deposition piece is fixedly connected with a spherical part, the top wall of the reaction chamber is provided with a spherical accommodating groove matched with the rotating ball, and the spherical part is clamped in the spherical accommodating groove.
As an alternative embodiment, a plurality of depositing elements are arranged in the reaction chamber at intervals.
As an alternative embodiment, the stripping assembly further comprises a rotating shaft, one end of the rotating shaft is vertically arranged and connected to the upper end of the main shell, and the impeller is arranged at the lower end of the rotating shaft.
As an alternative embodiment, the device further comprises a driving motor, wherein the driving motor is arranged on the main shell, and an output shaft of the driving motor is connected with the rotating shaft.
As an alternative embodiment, a heat exchange member is further provided along the circumference of the outer wall of the main casing, and is used for exchanging heat with the main casing to raise or lower the temperature of the main casing.
In a second aspect, the present invention also provides a precipitate separation method applied to the precipitate separation device of any one of the first aspects, the precipitate separation method comprising:
the water outlet of the sediment separation device is kept in a closed state, and the liquid to be treated is injected into the reaction chamber of the sediment separation device through the water injection port of the sediment separation device;
continuing the reaction for a preset time to enable the sediment piece in the sediment separation device to sediment;
the drain is opened and water free of sediment is injected into the reaction chamber so that the impeller of the stripping assembly collides with the sediment by the water flow, thereby stripping the sediment from the sediment and draining the sediment through the drain.
The sediment separation device provided by the invention comprises a main shell, a deposition piece and a stripping assembly; the inside of the main shell encloses a reaction chamber, the side wall of the main shell is provided with a plurality of water injection ports for injecting liquid to be treated, and the bottom of the main shell is provided with a water outlet which can be opened and closed; the deposition part is movably suspended in the reaction chamber to deposit sediment in the liquid to be treated; the stripping assembly includes an impeller rotatably disposed below the depositing member, and the impeller is configured to rotate under the impact of water flow from the water inlet and to impinge on the depositing member to strip sediment deposited on the depositing member from the surface of the depositing member. When the device is used, the to-be-treated liquid after oil-water separation can flow into the reaction chamber from the water injection port, the to-be-treated liquid flowing into the reaction chamber can be adhered to the surface of the deposition piece after being subjected to reaction deposition for a period of time under the action of the scaling agent, wherein the to-be-treated liquid collides with the free end of the deposition piece through the impeller of the impact stripping assembly in the process of being injected into the reaction chamber, so that the precipitate on the deposition piece can fall off, and the fallen precipitate is discharged from the reaction chamber through the water outlet.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, and it is obvious that the drawings in the following description are some embodiments of the present invention, and other drawings may be obtained according to the drawings without inventive effort to a person skilled in the art.
FIG. 1 is a schematic diagram of the overall structure of a sediment separation device according to an embodiment of the present invention;
FIG. 2 is a cross-sectional view taken at C-C of FIG. 1;
FIG. 3 is an enlarged view of FIG. 1 at A;
FIG. 4 is a schematic diagram of the overall structure of a sediment separation device according to an embodiment of the present invention;
FIG. 5 is an enlarged view at B in FIG. 4;
FIG. 6 is a flow chart of a method for treating a precipitate according to an embodiment of the present invention;
fig. 7 is a schematic diagram of a method for treating a precipitate according to an embodiment of the present invention.
Reference numerals illustrate:
1-a precipitate separation device;
100-a main housing;
110-a water filling port;
120-a water outlet;
200-depositing a piece;
210-hanging rings;
220-spherical portion;
230-accommodating grooves;
240-stop sleeve;
300-stripping assembly;
310-impeller;
320-rotating shaft;
330-a bearing;
400-drive motor
2-a water tank;
3-a water pump;
4-water storage equipment.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
In the application, the terms "upper", "lower", "left", "right", "front", "rear", "top", "bottom", "inner", "outer", "vertical", "horizontal", "lateral", "longitudinal" and the like indicate an azimuth or a positional relationship based on that shown in the drawings. These terms are only used to better describe the present invention and its embodiments and are not intended to limit the scope of the indicated devices, elements or components to the particular orientations or to configure and operate in the particular orientations.
Also, some of the terms described above may be used to indicate other meanings in addition to orientation or positional relationships, for example, the term "upper" may also be used to indicate some sort of attachment or connection in some cases. The specific meaning of these terms in the present invention will be understood by those of ordinary skill in the art according to the specific circumstances.
Furthermore, the terms "mounted," "configured," "provided," "connected," and "connected" are to be construed broadly. For example, it may be a fixed connection, a removable connection, or a unitary construction; may be a mechanical connection, or an electrical connection; may be directly connected, or indirectly connected through intervening media, or may be in internal communication between two devices, elements, or components. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art according to the specific circumstances.
Furthermore, the terms "first," "second," and the like, are used primarily to distinguish between different devices, elements, or components (the particular species and configurations may be the same or different), and are not used to indicate or imply the relative importance and number of devices, elements, or components indicated. Unless otherwise indicated, the meaning of "a plurality" is two or more.
In the field of oilfield development, along with oilfield development, oil layer pressure can continuously decline for oil recovery efficiency declines, in order to keep or improve oil layer pressure, generally can carry out the water injection to the oil layer, the water of injection oil layer can take away a large amount of ground bottom mineral substance in cyclic process, and in order to save water resource, the water of injection stratum generally can reuse, so cyclic down, the content of mineral substance contained in the water of injection stratum will be more and more, very easily form the precipitate on oil pipe inner wall, the existence of precipitate can cause oil pipe's passageway to diminish, influence crude oil's conveying efficiency. In the prior art, corresponding scale inhibitors are generally added into water injected into a stratum according to the mineral substance type contained in an oil field so as to prevent the formation of sediments, thereby protecting the oil pipe. However, not only are the scale inhibitors expensive, but because the amount of water injected into the subsurface tends to be large, the amount of scale inhibitor required is also large, further increasing the cost of removing the sediment.
In view of this, the present invention provides a sediment separation assembly comprising a main housing, a sediment element, and a stripping assembly; the inside of the main shell encloses a reaction chamber, the side wall of the main shell is provided with a plurality of water injection ports for injecting liquid to be treated, and the bottom of the main shell is provided with a water outlet which can be opened and closed; the deposition piece is movably suspended in the reaction chamber, the stripping component comprises an impeller rotatably arranged below the deposition piece, when the device is used, the liquid to be treated after oil-water separation can flow into the reaction chamber from the water injection port, the liquid to be treated flowing into the reaction chamber can be adhered to the surface of the deposition piece after being subjected to reaction deposition for a period of time under the action of the scaling agent, wherein the liquid to be treated collides with the free end of the deposition piece by impacting the impeller of the stripping component in the process of being injected into the reaction chamber, so that the precipitate on the deposition piece can be stripped, and the stripped precipitate is discharged from the reaction chamber through the water outlet.
Example 1
FIG. 1 is a schematic diagram of the overall structure of a sediment separation device according to an embodiment of the present invention; fig. 2 is a cross-sectional view at C-C in fig. 1. Referring to fig. 1 and 2, an embodiment of the present invention provides a sediment separation device 1, wherein the sediment separation device 1 may include a main housing 100, a sediment member 200, and a peeling assembly 300; wherein, the inside of the main casing 100 encloses a reaction chamber, the side wall of the main casing 100 is provided with a plurality of water injection ports 110 for injecting the liquid to be treated, and the bottom of the main casing 100 is provided with a water outlet 120 which can be opened and closed; the deposition piece 200 is movably hung in the reaction chamber to deposit sediment in the liquid to be treated; the stripping assembly 300 includes an impeller 310 rotatably disposed under the deposition member 200, and the impeller 310 is configured to rotate under the impact of the water flow of the water injection port 110 and collide with the deposition member 200 so that the deposits deposited on the deposition member 200 are stripped from the surface of the deposition member 200.
It will be appreciated that the precipitate separating device 1 according to the present invention may be applied to the separation of various types of precipitate in a liquid to be treated. The sediment separation device 1 may for example clean and remove scale from the liquid to be treated, for example clean the liquid to be treated; or collecting the precipitate in the liquid to be treated as a matter to be collected, thereby facilitating the subsequent utilization of the precipitate and the like. Thus, the sediment separation assembly 1 may be used in a variety of different applications, thereby achieving different sediment separation applications. For convenience of explanation, the sediment in the liquid to be treated is taken as scale, and the sediment separation device 1 is mainly used for performing scale removal operation on the liquid to be treated.
Specifically, in the sediment separation device 1 of the present invention, when in implementation, the water injection port 110 may be communicated with the water outlet of the oil-water separation device, the to-be-treated liquid after oil-water separation may flow into the reaction chamber from the water injection port 110, and the to-be-treated liquid flowing into the reaction chamber may be deposited by a period of reaction and may adhere to the surface of the deposition member 200, where the to-be-treated liquid impacts the free end of the deposition member 200 by impacting the impeller 310 of the stripping assembly 300 during the injection into the reaction chamber, so that the sediment such as scale on the deposition member 200 may be removed, and the water after scale removal and the scale after removal may be discharged from the water outlet 120.
Therefore, the sediment separation device 1 provided by the invention can create favorable conditions for the formation of scale, actively consume mineral substances in the liquid to be treated, does not need to use a scale inhibitor, and has low cost.
Second, it should be appreciated that the use of scale inhibitors in the prior art to remove deposits such as scale, in fact, merely inhibit scale formation, does not substantially reduce or eliminate the minerals that result in scale formation, and even the scale inhibitors themselves contain minerals. Thus, when the content of the scale inhibitor injected into the oil layer is insufficient, the inhibiting effect of the scale inhibitor on the formed sediments such as scale and the like is reduced, the oil pipe still faces the scaling problem, and the sediment separating device 1 provided by the embodiment is used for removing the scale or other sediments, so that the mineral content injected into the water layer can be effectively reduced, thereby fundamentally avoiding the formation of the scale sediments and having better cleaning effect on the sediments. In addition, since the process of treating the precipitate using the precipitate separating device 1 provided in the present embodiment may be performed on the ground, it is also convenient to adjust the process of treating the precipitate such as scale by controlling the process conditions to further improve the effect of treating the precipitate.
In practice, the deposition member 200 and the stripping assembly 300 may be installed into the reaction chamber through the drain port 120 at the bottom of the main housing 100, or an installation opening may be formed above the main housing 100, and an installation cover may be disposed at the installation opening, where the deposition member 200 and the stripping assembly 300 may be installed.
In one embodiment, the main housing 100 may be designed as a revolution body, and the plurality of water injection ports 110 are uniformly arranged along the circumferential direction of the main housing 100. Specifically, the main housing 100 may be designed in an inverted kettle shape as shown in fig. 1, i.e., the upper half is cylindrical and the lower half is tapered, so that not only the construction difficulty is reduced, but also the tapered structure of the lower half is convenient for discharging water, scale and other sediments.
The plurality of water injection ports 110 provided on the main housing 100 may be offset from the central axis of the reaction chamber, so that when the plurality of water injection ports 110 simultaneously inject the liquid to be treated into the reaction chamber, a vortex is formed in the reaction chamber, and the vortex may push the impeller 310 of the stripping assembly 300 to rotate. In order to obtain greater power for the impeller 310, the water filling port 110 and the impeller 310 may be located at the same height as much as possible, so that the liquid to be treated flowing into the reaction chamber from the water filling port 110 may directly act on the blades of the impeller 310. Specifically, the plurality of water injection ports 110 may be oriented tangentially to the inner wall of the reaction chamber, and thus the impact force of water injected into the reaction chamber from the water injection ports 110 on the blades of the impeller 310 may be further increased.
FIG. 3 is an enlarged view of FIG. 1 at A; FIG. 4 is a schematic diagram of the overall structure of a sediment separation device according to an embodiment of the present invention; fig. 5 is an enlarged view at B in fig. 4. Referring to fig. 3 to 5, the deposition member 200 may be a hollow steel pipe suspended in the reaction chamber, the bottom of the deposition member 200 may be suspended, specifically, the hanging ring 210 may be movably inserted into the upper end of the deposition member 200, and then one end of the hanging ring 210 away from the deposition member 200 is fixed to the upper end of the main housing 100. It should be understood that the suspended lower end (suspended end) of the depositing member 200 should be partially located between two adjacent blades of the impeller 310, so that when the impeller 310 rotates, the blades of the impeller 310 may collide with the lower end of the depositing member 200 to shake off the deposits such as scale on the depositing member 200.
As shown in fig. 5, in another arrangement of the deposition member 200, the upper end of the deposition member 200 may be a ball-shaped portion 220 fixedly connected, and a ball-shaped receiving groove 230 matched with the ball-shaped portion 220 may be provided on the top wall of the reaction chamber such that the ball-shaped portion 220 is caught in the ball-shaped receiving groove 230, and when the lower end of the deposition member 200 is collided with the impeller 310, the ball-shaped portion 220 of the upper end of the deposition member 200 may freely rotate in the ball-shaped receiving groove 230. Further, a stopper 240 may be further provided at the junction of the spherical portion 220 and the spherical receiving groove 230, and the stopper 240 may be used to prevent the spherical portion 220 from being separated from the spherical receiving groove 230. The deposition member 200 may be provided in other arrangements, without limitation.
In one embodiment, a plurality of through holes may be further formed on the sidewall of the deposition member 200, so that the surface area of the deposition member 200 may be increased to increase the deposition rate of the deposition of the scale, etc. on the deposition member 200.
In addition, there may be a plurality of deposition members 200, and a plurality of deposition members 200 may be disposed at intervals. By increasing the number of deposition pieces 200, the overall surface area of the deposition pieces 200, i.e., the deposition area, can be increased, and the efficiency of the treatment of the deposits such as scale can be improved.
The stripping assembly 300 may further include a rotation shaft 320, and when the stripping assembly is implemented, one end of the rotation shaft 320 may be vertically disposed and connected to the upper end of the main housing 100, and the impeller 310 may be mounted to the lower end of the rotation shaft 320. Specifically, the impeller 310 may be directly welded to the lower end of the rotation shaft 320, and the upper end of the rotation shaft 320 may be connected to the upper end of the main housing 100 through a bearing 330. In order to improve the stability of rotation of the impeller 310, the length of the connection section of the upper end of the rotation shaft 320 to the upper end of the main casing 100 may be appropriately increased, for example, may be connected to the upper end of the main casing 100 through a plurality of bearings 330 axially provided along the rotation shaft 320.
In one embodiment, the sediment separation assembly 1 may further include a driving motor having an output shaft connected to the rotation shaft 320. Specifically, the driving motor may be disposed on an outer surface of an upper end of the main housing 100, and an upper end of the rotation shaft 320 is penetrated out of the upper end of the main housing 100, so that the rotation shaft 320 penetrated out of the main housing 100 is fixedly connected with an output shaft of the driving motor. In this way, the peeling assembly 300 can be driven to rotate by the driving motor, so that the deposits such as scale on the deposition member 200 can be peeled at any time. And the driving motor drives the stripping assembly 300 to rotate with more sufficient power, so that the stripping effect of the sediment on the deposition member 200 can be improved.
In one embodiment, a heat exchange member may be further provided along the circumference of the outer wall of the main housing 100, wherein the heat exchange member is used to exchange heat with the main housing 100 to increase or decrease the temperature of the main housing 100. The heat exchange piece can heat the liquid to be treated in the reaction chamber, so that the precipitate forming speed is improved, and the precipitate treatment efficiency is improved. Specifically, the heat exchange member may be an electric heating wire wound on the outer wall of the main housing 100, and heating is convenient and efficient by the electric heating wire. The electrothermal exchange element may also be a heat exchanger, such as a water heating pipe, a gas heating pipe, a water cooling pipe or a gas cooling pipe, disposed along the outer wall of the main casing 100, and the heat exchanger is used to change the temperature of the main casing 100, so that the electrothermal exchange element is safe and reliable.
It should be noted that, in the embodiment of the present application, a plurality of precipitate separation devices 1 may be provided, and the plurality of precipitate separation devices 1 may be communicated with the outlet of the oil and water homogenizing separation device through a multi-directional valve, so that when the liquid to be treated in one of the precipitate separation devices 1 is fully loaded, the multi-directional valve may be controlled to inject water into the other precipitate separation device 1, thereby further improving the efficiency of treating the precipitate such as scale.
In one embodiment, the precipitate separation device 1 is further provided with a feeding port, specifically, the feeding port may be disposed at the top of the main casing 100, and the feeding port may be conveniently used to add substances capable of accelerating the scaling process into the reaction chamber.
The sediment separation assembly 1 provided by the present invention includes a main housing 100, a deposition member 200, and a stripping assembly 300; the inside of the main casing 100 encloses a reaction chamber, the side wall of the main casing 100 is provided with a plurality of water injection ports 110 for injecting liquid to be treated, and the bottom of the main casing 100 is provided with a water outlet 120 which can be opened and closed; the deposition member 200 is movably suspended in the reaction chamber, the stripping assembly 300 comprises an impeller 310 rotatably arranged below the deposition member 200, when the device is used, the liquid to be treated after oil-water separation can flow into the reaction chamber from the water injection port 110, the liquid to be treated flowing into the reaction chamber can be adhered to the surface of the deposition member 200 after being reacted and deposited for a period of time under the action of a scaling agent, wherein the liquid to be treated impacts the free end of the deposition member 200 by impacting the impeller 310 of the stripping assembly 300 in the process of injecting into the reaction chamber, so that the precipitate on the deposition member 200 can be stripped, and the stripped precipitate is discharged from the reaction chamber through the water outlet 120.
Example two
Fig. 6 is a flowchart of a method for treating a precipitate according to an embodiment of the present invention. As shown in fig. 6, the present invention also provides a sediment separation method which can be applied to the sediment separation device of any one of the first embodiments, thereby removing sediment such as scale in the liquid to be treated. The precipitate separation method may include:
s100, enabling a water outlet of the sediment separation device to be kept in a closed state, and injecting liquid to be treated into a reaction chamber of the sediment separation device through a water injection port of the sediment separation device.
And S200, continuously reacting for a preset time to enable sediment to be deposited on a deposition piece in the sediment separation device.
The formation of the precipitate can be accelerated by adding the scaling agent into the liquid to be treated in the reaction chamber, the precipitate can be gradually deposited on the surface of the deposition piece, and the preset time can be controlled to be 1-5 h, so that the reaction is not thorough enough due to the too short reaction time, the efficiency is not reduced due to the too long reaction time, and the preset time can be 3h.
S300, opening the water outlet, and injecting water without sediment into the reaction chamber again, so that the impeller of the stripping assembly collides with the sediment piece under the action of water flow, and the sediment is stripped from the sediment piece and discharged from the water outlet.
The water without sediment can be clean water which does not flow into the stratum or water treated by the sediment separation device. Fig. 7 is a schematic diagram of a sediment treatment method according to an embodiment of the present invention, as shown in fig. 7, specifically, water and sediment discharged from a water outlet may be collected in a water tank for solid-liquid separation (for example, the sediment may be settled at the bottom of the water tank to separate the water and the sediment), the separated water in the water tank may be pumped out by a water pump and injected into a water storage device, the water entering the water storage device may be reused and injected into a reaction chamber through a water filling port, or the water in the water storage device storing clean water may be directly injected into the reaction chamber to drive an impeller to rotate.
It should be understood that when the water outlet is opened and water without sediment is injected into the reaction chamber, the water without sediment entering the reaction chamber from the water injection port forms vortex to drive the stripping assembly to rotate, the impeller of the stripping assembly collides with the lower end of the deposition member, so that the sediment is separated from the surface of the deposition member, and when the sediment is separated from the deposition member, water injection into the reaction chamber can be stopped.
In addition, because the reaction chamber is already stored with the liquid to be treated, when the reaction chamber is filled with water again, the water inlet can face a certain water pressure, at this time, the pressure during water injection can be properly increased to overcome the water pressure at the water inlet in the reaction chamber, and meanwhile, the force of the impeller when the impeller collides with the deposition piece can be increased, the time for stripping the sediment on the deposition piece is shortened, and the sediment treatment efficiency is improved.
It should be understood that in this step, even if the precipitate on the deposition member is not completely peeled off, the precipitate remaining on the deposition member can be peeled off by continuing the method of colliding with the deposition member when the liquid to be treated is injected into the reaction chamber next time.
In addition, after the water and the sediment in the reaction chamber are discharged from the water outlet, the reaction chamber can be optionally washed by using the water without the sediment, or the water can directly enter the next round of sediment treatment, the treatment method can be consistent with the sediment treatment method in the embodiment, and the sediment treatment method in the embodiment is repeated until all the water containing the sediment is treated at least once by the sediment separation device.
In this embodiment, the fouling process can also be accelerated by adjusting the reaction chamber temperature through heat exchange elements or by adding substances to the reaction chamber that assist in the fouling process, as desired.
The sediment treatment method provided by the embodiment has the advantages that the sediment separation device provided by the embodiment I is used, the cost is lower, and the sediment removal effect is better.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present invention, and not for limiting the same; although the invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the invention.

Claims (8)

1. A sediment separator comprising a main housing, a sediment element, and a stripping assembly;
the reaction chamber is enclosed inside the main shell, a plurality of water injection ports for injecting liquid to be treated are formed in the side wall of the main shell, the orientation of each water injection port and the central axis of the reaction chamber are staggered, so that water injected by the water injection ports forms vortex in the reaction chamber, and the orientation of the water injection port is tangential to the inner wall of the reaction chamber;
the bottom of the main shell is provided with a water outlet which can be opened and closed;
the deposition part is movably suspended in the reaction chamber to deposit sediment in the liquid to be treated;
the stripping assembly comprises an impeller rotatably arranged below the depositing piece, and the impeller is configured to rotate under the impact of vortex formed by water flow of the water filling port and collide with the depositing piece so that sediment deposited on the depositing piece is stripped from the surface of the depositing piece and discharged from the water outlet;
the stripping assembly further comprises a rotating shaft, one end of the rotating shaft is vertically arranged and connected to the upper end of the main shell, and the impeller is arranged at the lower end of the rotating shaft.
2. The sediment separation device of claim 1, wherein the main housing is a revolution body, and the plurality of water injection ports are uniformly provided along the circumferential direction of the main housing.
3. The precipitate separating device according to any one of claims 1-2, wherein the depositing element is a hollow steel tube suspended in the reaction chamber, the bottom of the depositing element is suspended, and a plurality of through holes are formed in the side wall of the depositing element.
4. The sediment separator according to any one of claims 1-2, wherein the upper end of the sediment element is fixedly connected with a spherical portion, the top wall of the reaction chamber is provided with a spherical accommodating groove matched with the spherical portion, and the spherical portion is clamped in the spherical accommodating groove.
5. The apparatus according to any one of claims 1 to 2, wherein a plurality of the deposition members are provided in the reaction chamber at intervals.
6. The sediment separation assembly of claim 1, further comprising a drive motor disposed on the main housing, and wherein an output shaft of the drive motor is coupled to the rotating shaft.
7. The precipitate separating device according to any one of claims 1-2, wherein a heat exchanging element is further arranged in the circumferential direction of the outer wall of the main housing, said heat exchanging element being adapted to exchange heat with the main housing for increasing or decreasing the temperature of the main housing.
8. A precipitate separation method, characterized in that it is applied to the precipitate separation device according to any one of claims 1 to 7, comprising:
maintaining a water outlet of the sediment separation device in a closed state, and injecting liquid to be treated into a reaction chamber of the sediment separation device through a water injection port of the sediment separation device;
continuing the reaction for a preset time to enable the sediment piece in the sediment separation device to sediment;
opening the drain port and injecting water free of the sediment into the reaction chamber to cause the impeller of the stripping assembly to impinge upon the sediment piece under the influence of the water flow, thereby stripping the sediment from the sediment piece and draining the sediment from the drain port.
CN202210408251.8A 2022-04-19 2022-04-19 Sediment separation device and method Active CN114751494B (en)

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CN210419776U (en) * 2019-07-03 2020-04-28 烟台鲁航炭材料科技有限公司 Carbon/carbon composite material plate deposition device
CN113041645A (en) * 2019-12-26 2021-06-29 陕西博林生物技术有限公司 Extract separation and purification device convenient to clearance
CN216125852U (en) * 2021-08-23 2022-03-25 山东蓝繁环保科技有限公司 Wet-type electric precipitation defogging device

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Publication number Priority date Publication date Assignee Title
CN2461638Y (en) * 2000-09-12 2001-11-28 江苏省宜兴非金属化工机械厂 Ceramic filtering tube and filter for separating micron from titan white wasted water
CN107333699A (en) * 2017-08-24 2017-11-10 国家***第二海洋研究所 Precipitum acquisition equipment and biological in-situ culture apparatus
CN210419776U (en) * 2019-07-03 2020-04-28 烟台鲁航炭材料科技有限公司 Carbon/carbon composite material plate deposition device
CN113041645A (en) * 2019-12-26 2021-06-29 陕西博林生物技术有限公司 Extract separation and purification device convenient to clearance
CN216125852U (en) * 2021-08-23 2022-03-25 山东蓝繁环保科技有限公司 Wet-type electric precipitation defogging device

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