CN116832576A - Double-layer absorption type supergravity device - Google Patents

Double-layer absorption type supergravity device Download PDF

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Publication number
CN116832576A
CN116832576A CN202210294098.0A CN202210294098A CN116832576A CN 116832576 A CN116832576 A CN 116832576A CN 202210294098 A CN202210294098 A CN 202210294098A CN 116832576 A CN116832576 A CN 116832576A
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CN
China
Prior art keywords
baffle
layer
double
bed unit
shell
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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
CN202210294098.0A
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Chinese (zh)
Inventor
卢祐增
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Super Gravity Co ltd
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Super Gravity Co ltd
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Filing date
Publication date
Application filed by Super Gravity Co ltd filed Critical Super Gravity Co ltd
Priority to CN202210294098.0A priority Critical patent/CN116832576A/en
Publication of CN116832576A publication Critical patent/CN116832576A/en
Pending legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/14—Separation 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 absorption
    • B01D53/18—Absorbing units; Liquid distributors therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/14—Separation 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 absorption
    • B01D53/1406—Multiple stage absorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/24—Separation 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 centrifugal force
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/75—Multi-step processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/77—Liquid phase processes
    • B01D53/78—Liquid phase processes with gas-liquid contact

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

A double-layer absorption type super-gravity device comprises a shell, a rotating bed unit, a rotating shaft, a leaching layer, a baffle unit and a guide pipe. The rotary bed unit is arranged in the shell. The rinsing layer is disposed within the housing and spaced above the rotating bed unit and cooperates with the rotating bed unit to define an air flow space therebetween. The baffle unit is arranged in the airflow space and comprises a bottom baffle plate and a top baffle plate, wherein the bottom baffle plate and the top baffle plate are provided with bottom through holes. The top baffle plate is arranged above the bottom baffle plate at intervals and is arranged with the shell at intervals, and the bottom through hole is completely shielded in the axial direction of the rotating shaft. The double-layer absorption type super-gravity device can absorb different pollutants in gas, can avoid the mixture of the eluent and the liquid supplied by the guide pipe, and can ensure that the gas flowing through the bottom through hole uniformly enters the eluting layer.

Description

Double-layer absorption type supergravity device
Technical Field
The invention relates to a supergravity device, in particular to a double-layer absorption supergravity device.
Background
In the exhaust gas treatment industry, a plurality of treatment devices (such as a supergravity device, a scrubbing and absorbing tower, an activated carbon adsorption tower, a dust collector, etc.) are connected in series to treat various pollutants (such as sulfur oxides, nitrogen oxides, carbon dioxide, suspended particles, etc.) in exhaust gas (such as flue tail gas), respectively, so that a large configuration space is required.
Combining multiple treatment units capable of absorbing different contaminants in a gas in a single apparatus helps to reduce the required layout space, but liquids (e.g., alkaline liquid, acidic liquid, water, etc.) used by each treatment unit are easily mixed in a single apparatus, thereby resulting in a change in the composition of the individual liquids and a loss of absorption.
Disclosure of Invention
The first object of the present invention is to provide a double-layer absorption type supergravity device, which can overcome the above-mentioned drawbacks of the prior art.
The double-layer absorption type hypergravity device comprises a shell, a rotating bed unit, a rotating shaft, a leaching layer, a baffle unit and a guide pipe. The rotary bed unit is arranged in the shell and is arranged at intervals with the shell, and a circulation space positioned inside is defined. The rotating shaft is connected with the rotating bed unit and extends from the rotating bed unit to the outside of the shell. The rinsing layer is disposed within the housing and spaced above the rotating bed unit and cooperates with the rotating bed unit to define an air flow space therebetween. The baffle unit is arranged in the airflow space and comprises a bottom baffle and a top baffle. The bottom baffle plate is closely connected with the shell, the bottom baffle plate comprises a bottom upper surface and a bottom surface opposite to the bottom upper surface, and the bottom baffle plate forms a bottom through hole penetrating through the bottom upper surface and the bottom surface so as to enable the circulation space to be communicated with the leaching layer; the top baffle plate is arranged above the bottom baffle plate at intervals and is arranged with the shell at intervals, and the bottom through hole is completely shielded in the axial direction of the rotating shaft. The conduit extends from outside the housing into the flow space and is adapted to introduce a liquid into the flow space.
Preferably, the bottom baffle further comprises a bottom liquid-blocking annular wall extending upwardly from the bottom upper surface and surrounding the bottom through-hole.
Preferably, the top baffle extends in a radial direction of the rotation shaft.
Preferably, the housing includes an air inlet, an air outlet, an upper liquid outlet, and a lower liquid outlet. The gas inlet is adapted to introduce a gas into the housing. The gas outlet is adapted to direct gas through the rinse layer. The upper liquid outlet is adjacent to the bottom upper surface of the bottom baffle. The lower liquid outlet is arranged at the bottom of the shell.
Preferably, the rotating bed unit comprises a base plate and a filling layer extending upwards from the base plate, the filling layer and the base plate jointly surround and define the circulation space, and the rotating shaft is connected with the base plate of the rotating bed unit and extends from the base plate to the outside of the shell.
Preferably, the double layer absorption hypergravity device further comprises a leacheate dispersing unit adapted to disperse the leacheate in the leaching layer.
Preferably, the lower surface of the bottom baffle is connected to the top of the rotating bed unit by a dynamic seal.
Preferably, the conduit extends from outside the housing through the bottom liquid-resistant annular wall and the bottom through hole into the flow space.
A second object of the present invention is to provide a double-layer absorption type supergravity device, which can overcome the above-mentioned drawbacks of the background art.
The double-layer absorption type hypergravity device comprises a shell, a rotating bed unit, a rotating shaft, a leaching layer, a baffle unit and a guide pipe. The rotary bed unit is arranged in the shell and is arranged at intervals with the shell, and a circulation space positioned inside is defined. The rotating shaft is connected with the rotating bed unit and extends from the rotating bed unit to the outside of the shell. The rinsing layer is disposed within the housing and spaced above the rotating bed unit and cooperates with the rotating bed unit to define an air flow space therebetween. The baffle unit is arranged in the airflow space and comprises a bottom baffle, at least one middle baffle and a top baffle. The bottom baffle plate is closely connected with the shell, the bottom baffle plate comprises a bottom upper surface and a bottom surface opposite to the bottom upper surface, and the bottom baffle plate forms a bottom through hole penetrating through the bottom upper surface and the bottom surface so as to enable the circulation space to be communicated with the leaching layer; the at least one middle baffle plate is arranged above the bottom baffle plate at intervals and is arranged with the shell at intervals, and completely shields the bottom through hole in the axial direction of the rotating shaft, each middle baffle plate comprises a middle upper surface and a middle lower surface opposite to the middle upper surface, and each middle baffle plate forms a middle through hole penetrating through the middle upper surface and the middle lower surface; the top baffle plates are arranged above the at least one middle baffle plate at intervals and are arranged with the shell at intervals, and the middle through holes are completely shielded in the axial direction of the rotating shaft. The conduit extends from outside the housing into the flow space and is adapted to introduce a liquid into the flow space.
Preferably, each of the middle baffles further comprises a middle liquid-blocking annular wall extending upwardly from the middle upper surface and surrounding the middle through-hole.
Preferably, each intermediate baffle extends in a radial direction of the rotation shaft.
The invention has the beneficial effects that: the double-layer absorption type super-gravity device can absorb different pollutants in gas, can prevent leaching solution from flowing into the circulation space to be mixed with liquid supplied by the guide pipe, and can enable the gas flowing through the bottom through hole to uniformly enter the leaching layer.
Drawings
Other features and advantages of the invention will be apparent from the following description of the embodiments with reference to the accompanying drawings, in which:
FIG. 1 is a schematic cross-sectional view of a first embodiment of a dual layer absorption hypergravity device of the present invention;
FIG. 2 is a schematic cross-sectional view of a second embodiment of a dual layer absorption hypergravity device of the present invention; a kind of electronic device with high-pressure air-conditioning system
FIG. 3 is a schematic cross-sectional view of a third embodiment of a dual layer absorption hypergravity apparatus of the present invention.
Detailed Description
Before the present invention is described in detail, it should be noted that in the following description, like elements are denoted by the same reference numerals.
The invention will be further illustrated with reference to the following examples, but it should be understood that the examples are illustrative only and should not be construed as limiting the practice of the invention.
Referring to fig. 1, a first embodiment of a double-layer absorption type hypergravity device 1 of the present invention comprises a housing 2, a rotating bed unit 3, a rotating shaft 4, a rinsing layer 5, a baffle unit 6, a conduit 7, a dynamic seal 8 and a rinse dispersion unit 9.
The housing 2 includes an air inlet 21, an air outlet 22, an upper outlet 23, and a lower outlet 24. The gas inlet 21 is adapted to introduce gas into the housing 2. The gas outlet 22 is arranged at the top of the housing 2 and is adapted to lead out the gas passing through the rinsing layer 5. The lower liquid outlet 24 is disposed at the bottom of the housing 2.
The rotating bed unit 3 is disposed within the housing 2 and spaced apart from the housing 2 and defines an interior flow space 30. In this embodiment, the rotating bed unit 3 is a rotating packed bed (rotating packed bed). The rotating packed bed includes a base plate 31 and a packing layer 32 extending upward from the base plate 31 and having a hollow column shape. The filling layer 32 and the substrate 31 together surround and define the circulation space 30. The filler layer 32 is filled with a material selected from the group consisting of wire mesh, glass spheres, plastic filler, activated carbon, zeolite, metal plate, or combinations thereof. In this embodiment, the gas inlet 21 is disposed at a side of the housing 2 and adapted to introduce the gas flowing through the filling layer 32 to the circulation space 30.
The rotation shaft 4 is connected to the base plate 31 of the rotating bed unit 3 and extends from the base plate 31 to the outside of the housing 2.
In this embodiment, the rinsing layer 5 is disposed in the housing 2 and above the rotating bed unit 3 at intervals, and cooperates with the rotating bed unit 3 to define an airflow space 50 therebetween, and the rinsing layer 5 is a wire mesh.
In other embodiments of the invention, the rinse layer 5 is spaced from the housing 2 and has a hollow cylindrical structure (not shown) similar to the packed layer 32 of the rotating packed bed described above.
The baffle unit 6 is disposed in the airflow space 50. The baffle unit 6 includes a bottom baffle 61 and a top baffle 62. The bottom baffle 61 is closely attached to the housing 2, the bottom baffle 61 includes a bottom upper surface 611, a bottom lower surface 612 opposite to the bottom upper surface 611, and a bottom liquid blocking annular wall 613, and the bottom baffle 61 forms a bottom through hole 610 penetrating the bottom upper surface 611 and the bottom lower surface 612 for the communication space 30 to communicate with the rinse layer 5. The upper liquid outlet 23 is adjacent to the bottom upper surface 611 of the bottom baffle 61. The lower surface 612 is connected to the top of the rotating bed unit 3 by the dynamic seal 8. The bottom liquid-blocking annular wall 613 extends upward from the bottom upper surface 611 and surrounds the bottom through hole 610. The top baffle 62 is disposed above the bottom baffle 61 at a distance from the housing 2, and completely shields the bottom through hole 610 in the axial direction of the rotation shaft 4. The top baffle 62 extends in the radial direction of the rotation shaft 4.
The conduit 7 extends from the outside of the housing 2 into the flow space 30 through the side of the housing 2, the bottom liquid-blocking annular wall 613 and the bottom through hole 610 in this order.
In this embodiment, the rinse solution dispersing unit 9 is disposed above the rinse layer 5, and adapted to disperse the rinse solution on the upper surface of the rinse layer 5 from the outside of the housing 2, and the rinse solution dispersing unit 9 is a spray tube.
In other embodiments of the invention, the rinse solution dispersing unit 9 extends from the outside of the housing 2 into the space surrounded by the hollow columnar rinse layer 5, and is adapted to disperse the rinse solution on the inner circumferential surface (not shown) of the hollow columnar rinse layer 5.
When the rotating shaft 4 is externally driven to rotate so as to rotate the rotating bed unit 3 relative to the housing 2, the conduit 7 is supplied with a liquid (e.g. alkaline absorbing liquid) which is available for absorbing contaminants in the gas, which liquid enters the flow space 30 via an opening (not shown) in the conduit 7. As driven by centrifugal force, the liquid moves from inside to outside in the radial direction of the rotation shaft 4 and is dispersed into minute droplets, liquid filaments, or liquid films by centrifugal force in the filling layer 32 to promote the gas-liquid mass transfer rate. At the same time, a gas containing contaminants such as acid gas and alkaline gas is introduced into the housing 2 through the gas inlet 21, contacts the liquid in the filling layer 32 in countercurrent manner in the radial direction of the rotation shaft 4, and passes through the filling layer 32 from outside to inside.
Subsequently, the liquid absorbing part of the pollutants (such as acid gas) flows out from the lower liquid outlet 24 at the bottom of the shell 2; the gas still containing a part of the contaminants (e.g., alkaline gas) flows up to the gas flow space 50 and flows through the bottom through hole 610 and the space between the top baffle plate 62 and the housing 2, uniformly enters the rinse layer 5, and is absorbed in the rinse layer 5 by being contacted with the rinse solution (e.g., acidic or neutral rinse solution) introduced from the rinse solution dispersing unit 9 in a countercurrent manner. Finally, the gas passing through the rinsing layer 5 is discharged from the gas outlet 22 at the top of the housing 2; the rinse liquid that absorbs part of the contaminants (e.g., alkaline gas) flows through the top baffle 62 and the bottom upper surface 611 of the bottom baffle 61, and flows out through the upper outlet 23 on the side of the housing 2.
Referring to fig. 2, a second embodiment of the double-layered absorption hypergravity apparatus 1 of the present invention is similar to the first embodiment, except that in the second embodiment, the baffle unit 6 further includes a middle baffle 63. The middle baffle 63 is disposed above the bottom baffle 61 at a distance from the housing 2 and completely covers the bottom through hole 610 in the axial direction of the rotation shaft 4, the middle baffle 63 includes a middle upper surface 631, a middle lower surface 632 opposite to the middle upper surface 631, and a middle liquid blocking annular wall 633, and the middle baffle 63 forms a middle through hole 630 penetrating the middle upper surface 631 and the middle lower surface 632. The middle baffle 63 extends in the radial direction of the rotation shaft 4. The middle liquid blocking annular wall 633 extends upward from the middle upper surface 631 and surrounds the middle through hole 630. The top baffle 62 is disposed above the middle baffle 63 at a distance from the housing 2 and completely shields the middle through hole 630 in the axial direction of the rotation shaft 4.
In the second embodiment, the gas containing a part of the contaminants (e.g., alkaline gas) flows upward to the gas flow space 50 and flows through the bottom through hole 610, the middle through hole 630, the space between the middle baffle 63 and the housing 2, and the space between the top baffle 62 and the housing 2, uniformly into the rinse layer 5. Finally, the rinse liquid absorbing part of the contaminants (e.g., alkaline gas) flows through the top baffle 62, the upper surface 631 of the middle baffle 63 and the bottom upper surface 611 of the bottom baffle 61, and flows out through the upper outlet 23 on the side of the housing 2.
Referring to fig. 3, a third embodiment of the double-layered absorption hypergravity apparatus 1 of the present invention is similar to the second embodiment, except that in the third embodiment, the baffle unit 6 includes two middle baffles 63. The middle baffles 63 are disposed above the bottom baffle 61 at a vertical interval from each other and spaced from the housing 2, and the lower middle baffle 63 completely shields the bottom through hole 610 in the axial direction of the rotary shaft 4. Each middle baffle 63 includes a middle upper surface 631, a middle lower surface 632 opposite the middle upper surface 631, and a middle liquid blocking annular wall 633, and each middle baffle 63 forms a middle through hole 630 extending through the middle upper surface 631 and the middle lower surface 632. The upper middle barrier 63 completely shields the middle through hole 630 of the lower middle barrier 63 in the axial direction of the rotation shaft 4. Each intermediate baffle 63 extends in the radial direction of the rotation shaft 4. The middle liquid blocking annular wall 633 extends upward from the middle upper surface 631 and surrounds the middle through hole 630. The top baffle 62 is disposed above the middle baffle 63 at a distance from the housing 2, and completely shields the middle through hole 630 of the upper middle baffle 63 in the axial direction of the rotation shaft 4.
In the third embodiment, the gas containing a part of the contaminants (e.g., alkaline gas) flows upward to the gas flow space 50 and flows through the bottom through hole 610, the middle through hole 630, the space between the middle baffle 63 and the housing 2, and the space between the top baffle 62 and the housing 2, uniformly into the rinse layer 5. Finally, the rinse liquid absorbing part of the contaminants (such as alkaline gas) flows through the top baffle plate 62, the upper surface 631 of the middle baffle plate 63 and the bottom upper surface 611 of the bottom baffle plate 61, and flows out from the upper liquid outlet 23 on the side of the housing 2.
In summary, by arranging the baffle unit 6, the dual-layer absorption type hypergravity device 1 of the present invention can prevent the rinse liquid from flowing into the circulation space 30 to be mixed with the liquid supplied from the conduit 7, and can uniformly enter the rinse layer 5 through the bottom through hole 610 to uniformly contact the rinse liquid in a single device capable of absorbing different pollutants in the gas, so that the purpose of the present invention can be achieved.
The foregoing is merely illustrative of the present invention and is not intended to limit the scope of the invention, which is defined by the appended claims and their equivalents.

Claims (11)

1. The utility model provides a double-deck absorption formula hypergravity device which characterized in that: the double-layer absorption type super-gravity device comprises:
a housing;
the rotating bed unit is arranged in the shell and is spaced from the shell, and a circulation space positioned inside is defined;
a rotating shaft connected to the rotating bed unit and extending from the rotating bed unit to the outside of the housing;
the leaching layer is arranged in the shell, is arranged above the rotary bed unit at intervals, and is matched with the rotary bed unit to define an air flow space between the leaching layer and the rotary bed unit;
a baffle unit disposed in the airflow space, the baffle unit comprising:
a bottom baffle plate closely connected to the housing, the bottom baffle plate including a bottom upper surface and a bottom surface opposite to the bottom upper surface, the bottom baffle plate forming a bottom through hole penetrating the bottom upper surface and the bottom surface for the communication of the circulation space and the rinsing layer, and
the top baffle is arranged above the bottom baffle at intervals and is arranged with the shell at intervals, and the bottom through hole is completely shielded in the axial direction of the rotating shaft; a kind of electronic device with high-pressure air-conditioning system
A conduit extending from outside the housing into the flow space adapted to introduce a liquid into the flow space.
2. The double-layer absorption hypergravity device according to claim 1, wherein: the bottom baffle further includes a bottom liquid-blocking annular wall extending upwardly from the bottom upper surface and surrounding the bottom through-hole.
3. The double-layer absorption hypergravity device according to claim 1, wherein: the top baffle extends in a radial direction of the rotation shaft.
4. The double-layer absorption hypergravity device according to claim 1, wherein: the housing includes:
a gas inlet adapted to introduce a gas into the housing;
a gas outlet adapted to direct gas through the rinse layer;
an upper liquid outlet adjacent to the bottom upper surface of the bottom baffle; a kind of electronic device with high-pressure air-conditioning system
The lower liquid outlet is arranged at the bottom of the shell.
5. The double-layer absorption hypergravity device according to claim 1, wherein: the rotary bed unit comprises a base plate and a filling layer extending upwards from the base plate, the filling layer and the base plate jointly surround and define the circulation space, and the rotary shaft is connected with the base plate of the rotary bed unit and extends from the base plate to the outside of the shell.
6. The double-layer absorption hypergravity device according to claim 1, wherein: and a rinse solution dispersing unit adapted to disperse rinse solution in the rinse layer.
7. The double-layer absorption hypergravity device according to claim 1, wherein: the bottom surface of the bottom baffle is connected to the top of the rotating bed unit by a dynamic seal.
8. The double-layer absorption hypergravity device according to claim 2, wherein: the conduit extends from the exterior of the housing through the bottom liquid-blocking annular wall and the bottom through hole into the flow space.
9. The utility model provides a double-deck absorption formula hypergravity device which characterized in that: the double-layer absorption type super-gravity device comprises:
a housing;
the rotating bed unit is arranged in the shell and is spaced from the shell, and a circulation space positioned inside is defined;
a rotating shaft connected to the rotating bed unit and extending from the rotating bed unit to the outside of the housing;
the leaching layer is arranged in the shell, is arranged above the rotary bed unit at intervals, and is matched with the rotary bed unit to define an air flow space between the leaching layer and the rotary bed unit;
a baffle unit disposed in the airflow space, the baffle unit comprising:
a bottom baffle plate closely connected to the shell, the bottom baffle plate comprises a bottom upper surface and a bottom surface opposite to the bottom upper surface, the bottom baffle plate forms a bottom through hole penetrating the bottom upper surface and the bottom surface for the communication of the circulating space and the rinsing layer,
at least one middle baffle plate arranged above the bottom baffle plate at intervals and spaced from the shell and completely shielding the bottom through hole in the axial direction of the rotating shaft, each middle baffle plate comprising a middle upper surface and a middle lower surface opposite to the middle upper surface, each middle baffle plate forming a middle through hole penetrating the middle upper surface and the middle lower surface, and
the top baffle is arranged above the at least one middle baffle at intervals and is arranged with the shell at intervals, and the middle through hole is completely shielded in the axial direction of the rotating shaft; a kind of electronic device with high-pressure air-conditioning system
A conduit extending from outside the housing into the flow space adapted to introduce a liquid into the flow space.
10. The double-layer absorption hypergravity device according to claim 9, wherein: each middle baffle further comprises a middle liquid-blocking annular wall extending upward from the middle upper surface and surrounding the middle through hole.
11. The double-layer absorption hypergravity device according to claim 9, wherein: each intermediate baffle extends in a radial direction of the rotation shaft.
CN202210294098.0A 2022-03-24 2022-03-24 Double-layer absorption type supergravity device Pending CN116832576A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210294098.0A CN116832576A (en) 2022-03-24 2022-03-24 Double-layer absorption type supergravity device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210294098.0A CN116832576A (en) 2022-03-24 2022-03-24 Double-layer absorption type supergravity device

Publications (1)

Publication Number Publication Date
CN116832576A true CN116832576A (en) 2023-10-03

Family

ID=88171156

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210294098.0A Pending CN116832576A (en) 2022-03-24 2022-03-24 Double-layer absorption type supergravity device

Country Status (1)

Country Link
CN (1) CN116832576A (en)

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