CN118163258A - Fluid separation device and processing equipment - Google Patents

Fluid separation device and processing equipment Download PDF

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Publication number
CN118163258A
CN118163258A CN202410440882.7A CN202410440882A CN118163258A CN 118163258 A CN118163258 A CN 118163258A CN 202410440882 A CN202410440882 A CN 202410440882A CN 118163258 A CN118163258 A CN 118163258A
Authority
CN
China
Prior art keywords
fluid
separation device
exhaust pipe
flow guiding
separation
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.)
Pending
Application number
CN202410440882.7A
Other languages
Chinese (zh)
Inventor
丁宇峰
刘晋
杨骥
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Ward Xinfeng Environmental Technology Co ltd
Original Assignee
Shanghai Ward Xinfeng Environmental Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shanghai Ward Xinfeng Environmental Technology Co ltd filed Critical Shanghai Ward Xinfeng Environmental Technology Co ltd
Priority to CN202410440882.7A priority Critical patent/CN118163258A/en
Publication of CN118163258A publication Critical patent/CN118163258A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/05Separating dispersed particles from gases, air or vapours by liquid as separating agent by condensation of the separating agent
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/02Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/18Cleaning-out devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D50/00Combinations of methods or devices for separating particles from gases or vapours
    • B01D50/40Combinations of devices covered by groups B01D45/00 and B01D47/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B15/00Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area
    • B08B15/04Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area from a small area, e.g. a tool
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28DWORKING STONE OR STONE-LIKE MATERIALS
    • B28D5/00Fine working of gems, jewels, crystals, e.g. of semiconductor material; apparatus or devices therefor
    • B28D5/0058Accessories specially adapted for use with machines for fine working of gems, jewels, crystals, e.g. of semiconductor material
    • B28D5/0082Accessories specially adapted for use with machines for fine working of gems, jewels, crystals, e.g. of semiconductor material for supporting, holding, feeding, conveying or discharging work

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

The invention provides a fluid separation device and processing equipment, wherein the processing equipment comprises a dust removal pipeline and a fluid separation device, and the fluid separation device is communicated with the dust removal pipeline and is used for separating mixed fluid in the dust removal pipeline. The fluid separation device comprises a separation part, the separation part comprises a flow director, an exhaust pipe and a flow guiding channel, a flow guiding inlet and a flow guiding outlet are arranged on the flow guiding channel, the exhaust pipe is inserted into the flow guiding outlet, and a gap is arranged between the exhaust pipe and the flow guiding outlet; the fluid director is arranged in the diversion channel and is used for driving the mixed fluid entering from the diversion inlet to move so as to discharge the fluid with low density from the exhaust pipe and discharge the fluid with high density from the gap. The fluid separation device can separate mixed fluid, so that the service life of processing equipment is prolonged, and the dust removal effect of a dust removal pipeline is ensured.

Description

Fluid separation device and processing equipment
Technical Field
The present invention relates to a fluid separation device and a processing apparatus, and more particularly, to a fluid separation device and a processing apparatus for separating a mixed fluid.
Background
When cutting crystals, the cutting fluid in the cabin door of the processing equipment can evaporate under the action of the cutting heat, the steam of the cutting fluid is condensed into tiny droplets in the cabin, and the tiny droplets absorb tiny dust particles in the cabin to form a dust mixture. As the cutting operation proceeds, part of the dust mixture collides with each other, increases in volume and naturally falls, and the remaining part of the dust mixture having a diameter of 10um or less floats in the cabin for a long time.
The dust removing pipe for sucking the dust mixture is arranged in the processing equipment, and after the dust mixture is sucked into the dust removing pipe, the dust mixture may collapse the dust removing pipe along with the aggregation of the dust mixture. Meanwhile, hardening phenomenon can occur after moisture of the dust mixture in the dust removing pipeline is evaporated, so that the pipeline is blocked, the air quantity in the pipeline is reduced, and the dust removing effect of the dust removing pipeline is affected. In addition, the dust removal pipeline with hardening phenomenon is difficult to clean, the workload of operators can be increased, and the production progress is influenced.
Therefore, it is a technical problem to be solved at present, how to design a device capable of separating dust mixture for those skilled in the art.
Disclosure of Invention
The invention aims to provide a fluid separation device and processing equipment, wherein the fluid separation device can separate mixed fluid, so that the service life of the processing equipment is prolonged, and the dust removal effect of a dust removal pipeline is ensured.
In order to achieve the above object, the present invention provides a fluid separation device, including a separation portion, the separation portion including a flow director, an exhaust pipe, and a flow guiding channel, the flow guiding channel being provided with a flow guiding inlet and a flow guiding outlet, the exhaust pipe being inserted into the flow guiding outlet, a gap being provided between the exhaust pipe and the flow guiding outlet; the fluid director is arranged in the fluid director channel and is used for driving the mixed fluid entering from the fluid director inlet to move so as to enable the fluid with low density to be discharged from the exhaust pipe and the fluid with high density to be discharged from the gap.
Optionally, the flow director includes a flow guiding vane for separating the gas and the liquid in the mixed fluid, so that the gas in the mixed fluid is discharged from the exhaust pipe, and the liquid in the mixed fluid is discharged from the gap.
Optionally, an annular gap is formed between the exhaust pipe and the diversion outlet.
Optionally, the fluid separation device further comprises a storage portion comprising a collection chamber in communication with the separation portion and adapted to collect liquid discharged through the gap.
Optionally, the number of the separation parts is a plurality of, all the separation parts are arranged at intervals along a direction perpendicular to the central axis of the exhaust pipe, and all the separation parts are communicated with the collection chamber through a corresponding gap.
Optionally, the storage part further comprises a drain pipe, which is communicated with the collecting chamber and is used for discharging the liquid in the collecting chamber.
Optionally, the central axis of the exhaust pipe, the central axis of the guide channel and the rotation axis of the guide vane are all coincident.
Optionally, the separation part further comprises an air inlet pipe, and the air inlet pipe is communicated with the diversion inlet.
Optionally, the internal profile of at least a portion of the air inlet pipe tapers in the direction of the flow guiding outlet and/or the internal profile of at least a portion of the air outlet pipe tapers in the direction of the flow guiding inlet.
In order to achieve the above object, the present invention also provides a processing apparatus, including a dust removing pipe and any one of the fluid separating devices, the fluid separating device being in communication with the dust removing pipe and configured to separate a mixed fluid inside the dust removing pipe.
The invention provides a fluid separation device and processing equipment, wherein the processing equipment comprises a dust removal pipeline and a fluid separation device, and the fluid separation device is communicated with the dust removal pipeline and is used for separating mixed fluid in the dust removal pipeline. The fluid separation device comprises a separation part, wherein the separation part comprises a flow director, an exhaust pipe and a flow guiding channel, the flow guiding channel is provided with a flow guiding inlet and a flow guiding outlet, the exhaust pipe is inserted into the flow guiding outlet, and a gap is arranged between the exhaust pipe and the flow guiding outlet; the fluid director is arranged in the flow guiding channel and is used for driving the mixed fluid entering from the flow guiding inlet to move so as to enable the fluid with low density to be discharged from the exhaust pipe and the fluid with high density to be discharged from the gap. The fluid separation device can realize the separation of mixed fluid, so that the mixed fluid can be prevented from being condensed in the dust removal pipeline after being evaporated, the service life of processing equipment is prolonged, and the dust removal effect of the dust removal pipeline in the processing equipment is ensured.
Drawings
FIG. 1 is a schematic view showing a part of a construction of a processing apparatus according to a preferred embodiment of the present invention;
fig. 2 is an enlarged view of a portion of the fluid separation device of fig. 1.
Reference numerals are described as follows:
A separation section 1; a deflector 11; an exhaust pipe 12; a diversion channel 13; a diversion inlet 131; a diversion outlet 132; a gap 14; an intake pipe 15; a storage unit (2); a collection chamber 21; a drain pipe 22; and a housing 3.
Detailed Description
The invention is described in further detail below with reference to the drawings and the specific examples. The advantages and features of the present invention will become more apparent from the following description. It should be noted that the drawings are in a very simplified form and are all to a non-precise scale, merely for convenience and clarity in aiding in the description of embodiments of the invention.
The terms "center," "longitudinal," "transverse," "length," "width," "thickness," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," "clockwise," "counter-clockwise," "axial," "radial," "circumferential," etc. refer to an orientation or positional relationship based on that shown in the drawings, merely for convenience of description and to simplify the description, and do not indicate or imply that the devices or elements referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the invention.
In the present invention, unless explicitly specified and limited otherwise, the terms "mounted," "connected," "secured," and the like are to be construed broadly and include, for example, either fixedly attached, detachably attached, or integrally formed; may be mechanically connected, may be electrically connected or may be in communication with each other; either directly, or through an intermediary, may be internal to the two elements or in an interactive relationship with the two elements, unless explicitly defined otherwise. 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. In the description of the present invention, "plurality" means at least two, for example, two or three or more, etc.
The invention will now be described in detail with reference to the drawings and a preferred embodiment. The following embodiments and features of the embodiments may be complemented or combined with each other without conflict.
As shown in fig. 1 and 2, a preferred embodiment of the present invention provides a fluid separation device, which includes a separation part 1, the separation part 1 includes a flow director 11, an exhaust pipe 12 and a flow guiding channel 13, a flow guiding inlet 131 and a flow guiding outlet 132 are provided on the flow guiding channel 13, the exhaust pipe 12 is inserted into the flow guiding outlet 132, and a gap 14 is provided between the air pipe 12 and the flow guiding outlet 132. The fluid director 11 is positioned within the fluid directing channel 13 and is configured to move the mixed fluid entering from the fluid directing inlet 131 such that a less dense fluid is discharged from the exhaust pipe 12 and a more dense fluid is discharged from the gap 14.
As shown in fig. 1, a preferred embodiment of the present invention also provides a processing apparatus including a dust removing pipe (not numbered) for sucking a mixed fluid generated in a cabin of the processing apparatus, and a fluid separating device. The fluid separation device is communicated with the dust removing pipeline and is used for separating mixed fluid in the dust removing pipeline.
The fluid separation device provided by the invention can realize the separation of the mixed fluid, so that the mixed fluid is prevented from being condensed in the dust removal pipeline after being evaporated, the service life of processing equipment is prolonged, and the dust removal effect of the processing equipment is ensured.
It should be noted that the processing equipment in the present application can be applied to the fields of machinery, semiconductors, solar energy, etc. Meanwhile, the application working conditions of the processing equipment are not limited to cutting of metal materials or nonmetal materials, and the processing equipment can be also suitable for working conditions such as polishing, welding and polishing of the metal materials or nonmetal materials. In the working condition, the mixed fluid generated by the metal material or the nonmetallic material during processing can be separated by adopting the fluid separation device.
Further, the diversion inlet 131 is used for being connected with a dust removing pipeline, so that mixed fluid in the dust removing pipeline is led into the fluid separation device, and the mixed fluid is separated through the fluid separation device.
When in actual use, the number of the fluid separation devices and the dust removal pipelines can be multiple, and at the moment, the fluid separation devices can be connected to each dust removal pipeline of the processing equipment so as to fully separate the mixed fluid in each dust removal pipeline, and the separation effect of the processing equipment on the mixed fluid is improved.
It should be understood that the mixed fluid in the present application may be a mixed gas, and the mixed fluid may also be a gas-liquid mixture formed by mixing a gas and a liquid. The application is not limited to the kind of the mixed fluid. For example, in cutting metallic or nonmetallic materials, the mixing fluid may be a mixture of various kinds of dust, and the mixing fluid may also be a mixture of cutting fluid droplets and dust. For another example, when polishing or grinding metallic or non-metallic materials, the mixing fluid may be a mixture of various kinds of dust, and the mixing fluid may be a mixture of cooling liquid and dust.
In a preferred embodiment, the deflector 11 comprises a deflector vane. Specifically, the deflector 11 includes a plurality of deflector blades (not numbered) for uniformly dispersing the mixed fluid, all of which are connected to each other and uniformly distributed in the circumferential direction. Because the densities of the components of the mixed fluid are different, the centrifugal forces applied to the fluids with different densities are different when the fluids with different densities flow, so that the flow track of the fluids with different densities is different, and the fluids with different densities can be separated through the fluid separation device. The arrangement of the guide vane can improve the separation efficiency of the fluid separation device, ensure the purity of the gas discharged by the exhaust pipe 12 and has great application prospect.
When the mixed fluid is a gas-liquid mixture, the guide vane is used for changing the movement direction of the mixed fluid so as to separate the gas and the liquid in the mixed fluid, so that the gas in the mixed fluid is discharged from the exhaust pipe 12, and the liquid in the mixed fluid is discharged from the gap 14, thereby realizing the gas-liquid separation of the mixed fluid by the fluid separation device.
Referring to fig. 1 and 2, in a preferred embodiment, the guide vane is fixed in the guide passage 13 while the guide vane is not rotated. After the mixed fluid enters the guide channel 13 through the guide inlet 131, the mixed fluid flows along the arc of the guide vane. Due to the density difference between the gas and the liquid, the flow track of the gas and the liquid in the mixed fluid is different under the action of the inertia force of the guide vane so as to separate the gas and the liquid in the mixed fluid.
In another preferred embodiment, the guide vane is rotatably disposed in the guide passage 13, in which case the guide vane can rotate in its own circumferential direction to apply work to the mixed fluid. When the mixed fluid enters the diversion channel 13 through the diversion inlet 131, the mixed fluid rotates under the combined action of the centrifugal force and the inertial force of the diversion blades, so that the mixed fluid generates a uniform rotational flow effect. Because the density of each component of the mixed fluid is different, the centrifugal force applied to the gas and the liquid in the mixed fluid during the rotation movement is different, so that the flow track of the gas and the liquid in the mixed fluid is different, and the gas and the liquid in the mixed fluid can be separated.
Further, after the mixed fluid passes through the action of the guide vane, the gas with smaller density in the mixed fluid moves at the middle part of the guide channel 13 (i.e. the position close to the central axis of the guide channel 13) and is discharged from the exhaust pipe 12; while the denser liquid in the mixed fluid moves substantially against the inner wall of the diversion channel 13 and out of the gap 14 between the exhaust pipe 12 and the diversion outlet 132.
Preferably, an annular gap is formed between the exhaust pipe 12 and the diversion outlet 132, in other words, the outer wall of the exhaust pipe 12 has a gap with the inner wall of the diversion outlet 132 on the whole circumference, at this time, the liquid separated from the mixed fluid can flow out through any position in the annular gap, so as to improve the gas-liquid separation efficiency of the fluid separation device.
With continued reference to fig. 1 and 2, the fluid separation device further comprises a storage portion 2, the storage portion 2 comprising a collection chamber 21, the collection chamber 21 being in communication with the separation portion 1 and being adapted to collect liquid discharged through the gap 14, i.e. the fluid separation device is adapted to store liquid separated from the mixed fluid through the collection chamber 21.
Preferably, the storage part 2 further includes a drain pipe 22, the drain pipe 22 being in communication with the collection chamber 21 and being for discharging the liquid in the collection chamber 21. In one embodiment, the liquid separated from the mixed fluid may flow through drain 22 into a sump within the processing equipment compartment.
Referring to fig. 1, in a preferred embodiment, the number of the separation parts 1 is plural, all the separation parts 1 are arranged at intervals in a direction perpendicular to the central axis of the exhaust pipe 12, and all the separation parts 1 are preferably arranged at intervals in the vertical direction in sequence. All the separating portions 1 are in communication with the collecting chamber 21 through a corresponding one of the gaps 14, that is, the gap 14 of each separating portion 1 is in communication with the collecting chamber 21, so that the collecting chamber 21 can collect the liquid separated in all the separating portions 1 to facilitate the concentrated treatment of the liquid.
In this embodiment, the fluid separation device further comprises a housing 3, all separation parts 1 being placed in the accommodation space of the housing 3. The collection chamber 21 is provided below the housing 3 and communicates with the bottom of the housing 3. The liquid flowing out of the gap 14 of each separation part 1 can enter the accommodation space of the housing 3 and flow into the collection chamber 21 below the housing 3.
In a preferred embodiment, the central axis of the exhaust pipe 12, the rotation axis of the guide vane 11 and the central axis of the guide channel 13 (i.e. the extending direction of the guide channel 13) are parallel or coincident, preferably coincident, at this time, the arrangement direction of the rotation axis of the guide vane 11 and the outflow direction of the gas in the guide outlet 132 are the same, so that the gas separated in the guide vane 11 can always move along the axial direction of the guide channel 13 until being discharged from the exhaust pipe 12, and the smoothness of gas discharge is improved.
As shown in fig. 1 and 2, in an exemplary embodiment, the internal profile of at least a portion of the exhaust pipe 12 gradually decreases toward the diversion inlet 131, i.e., the exhaust pipe 12 has a bell mouth structure, and the cross section of the exhaust pipe 12 gradually decreases along the direction from the diversion outlet 132 to the diversion inlet 131. So constructed, the caliber of the exhaust pipe 12 is gradually increased along with the outflow of the gas in the diversion channel 13, so as to further improve the fluency of the gas flow and the working efficiency of the fluid separation device.
With continued reference to fig. 1 and 2, the separating portion 1 further comprises an air inlet duct 15, the air inlet duct 15 being in communication with the diversion inlet 131. Further, the air inlet pipe 15 is used for connecting with a dust removing pipe, so that mixed fluid in the dust removing pipe is led into the diversion channel 13 through the diversion inlet 131.
Optionally, the internal profile of at least a portion of the section of the air inlet pipe 15 gradually decreases in the direction of the pilot outlet 132, i.e. the cross section of the air inlet pipe 15 gradually decreases in the direction of the pilot inlet 131 to the pilot outlet 132. The gas flow rate in the diversion channel 13 can be improved, so that the separation efficiency of the fluid separation device is improved under the action of the diversion device 11.
As a preferred solution, the central axis of the air inlet pipe 15, the central axis of the air outlet pipe 12, the central axis of the guide channel 13 and the rotation axis of the guide vane 11 are all coincident, and at this time, the inflow direction of the mixed fluid in the air inlet pipe 15, the outflow direction of the air in the air outlet pipe 12, and the extending direction of the guide channel 13 are all the same as the arrangement direction of the rotation axis of the guide vane 11. After the mixed fluid flows in along the extending direction of the diversion channel 13, the separated gas can be discharged along the extending direction of the diversion channel 13 under the action of the deflector 11, so that the mixed fluid always flows along the same direction (namely, the flowing direction) in the fluid separation device, and the fluency of the gas flow is further improved.
In summary, in the fluid separation device and the processing equipment provided by the application, the fluid separation device can realize the separation of the mixed fluid, so that the mixed fluid is prevented from being condensed in the dust removal pipeline after being evaporated, the service life of the processing equipment is prolonged, and the dust removal effect of the processing equipment is ensured.
The above description is only illustrative of the preferred embodiments of the present invention and is not intended to limit the scope of the present invention, and any alterations and modifications made by those skilled in the art based on the above disclosure shall fall within the scope of the present invention.

Claims (10)

1. The fluid separation device is characterized by comprising a separation part, wherein the separation part comprises a flow director, an exhaust pipe and a flow guiding channel, a flow guiding inlet and a flow guiding outlet are arranged on the flow guiding channel, the exhaust pipe is inserted into the flow guiding outlet, and a gap is arranged between the exhaust pipe and the flow guiding outlet; the fluid director is arranged in the fluid director channel and is used for driving the mixed fluid entering from the fluid director inlet to move so as to enable the fluid with low density to be discharged from the exhaust pipe and the fluid with high density to be discharged from the gap.
2. The fluid separation device of claim 1, wherein the deflector comprises a deflector vane for separating gas and liquid in the mixed fluid to expel gas in the mixed fluid from the exhaust pipe and liquid in the mixed fluid from the gap.
3. The fluid separation device of claim 2, wherein an annular gap is formed between the exhaust pipe and the flow directing outlet.
4. The fluid separation device of claim 2, further comprising a reservoir comprising a collection chamber in communication with the separation section and configured to collect liquid discharged through the gap.
5. The fluid separation device of claim 4, wherein the number of separation portions is plural, all the separation portions are arranged at intervals in a direction perpendicular to a central axis of the exhaust pipe, and all the separation portions communicate with the collection chamber through a corresponding one of the gaps.
6. The fluid separation device of claim 4, wherein the reservoir further comprises a drain in communication with the collection chamber and configured to drain liquid from within the collection chamber.
7. The fluid separation device of claim 1, wherein a central axis of the exhaust pipe, a central axis of the guide channel, and a rotational axis of the guide vane all coincide.
8. The fluid separation device of any one of claims 1-7, wherein the separation section further comprises an air inlet conduit in communication with the diversion inlet.
9. The fluid separation device of claim 8, wherein an interior profile of at least a portion of the intake pipe tapers in a direction toward the diversion outlet and/or an interior profile of at least a portion of the exhaust pipe tapers in a direction toward the diversion inlet.
10. A processing apparatus comprising a dedusting conduit and a fluid separation apparatus according to any one of claims 1 to 9 in communication with the dedusting conduit and operable to separate a mixed fluid within the dedusting conduit.
CN202410440882.7A 2024-04-12 2024-04-12 Fluid separation device and processing equipment Pending CN118163258A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202410440882.7A CN118163258A (en) 2024-04-12 2024-04-12 Fluid separation device and processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202410440882.7A CN118163258A (en) 2024-04-12 2024-04-12 Fluid separation device and processing equipment

Publications (1)

Publication Number Publication Date
CN118163258A true CN118163258A (en) 2024-06-11

Family

ID=91358263

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202410440882.7A Pending CN118163258A (en) 2024-04-12 2024-04-12 Fluid separation device and processing equipment

Country Status (1)

Country Link
CN (1) CN118163258A (en)

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