KR20120008124A - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- KR20120008124A KR20120008124A KR1020100068783A KR20100068783A KR20120008124A KR 20120008124 A KR20120008124 A KR 20120008124A KR 1020100068783 A KR1020100068783 A KR 1020100068783A KR 20100068783 A KR20100068783 A KR 20100068783A KR 20120008124 A KR20120008124 A KR 20120008124A
- Authority
- KR
- South Korea
- Prior art keywords
- gas
- container
- liquid separator
- liquid
- outlet
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 61
- 230000000903 blocking effect Effects 0.000 claims description 10
- 230000005484 gravity Effects 0.000 claims description 8
- 230000009471 action Effects 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000009434 installation Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000007547 defect Effects 0.000 abstract description 2
- 230000001747 exhibiting effect Effects 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 239000013013 elastic material Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000009474 immediate action Effects 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012780 transparent material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2247/00—Details relating to the separation of dispersed particles from gases, air or vapours by liquid as separating agent
- B01D2247/10—Means for removing the washing fluid dispersed in the gas or vapours
- B01D2247/108—Means for removing the washing fluid dispersed in the gas or vapours using vortex inducers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/06—Construction of inlets or outlets to the vortex chamber
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
A gas-liquid separator for removing a liquid component such as moisture from a gas such as air is disclosed. The disclosed gas-liquid separator covers the upper cap 20 on the upper side of the main body 10 and forms two piping connectors 22 and 23 on the upper cap, and an inlet 24 and an outlet 25 of the gas following each connector. The two connection ports are connected to an external gas pipe line to be installed, and a separate vortex forming pipe 40 is connected to the inlet port, and a separate outflow guide tube 50 is connected to the outlet port so as to form a liquid component from the gas. To form an airflow that can be centrifuged. According to this configuration, it can be connected as it is without having to bend the pipe in the middle of the outside gas pipe line, and its installation is very easy, and it is easy to manufacture and assemble through the standardization of parts such as vortex forming pipes. Reliability can be improved by minimizing defects caused by assembly and installation errors and exhibiting certain characteristics.
Description
The present invention relates to a gas-liquid separator for removing a liquid component such as water from a gas such as air, and particularly for improving the structure of a gas-liquid separator for centrifuging a liquid such as water from a gas such as air.
The gas-liquid separator as the subject of the present invention is essential in an environment for using sanitary equipment such as an air conditioner or a medical equipment that provides clean air as well as various mechanical devices that work through gas such as air. The reason is that the liquid components such as moisture contained in the gas such as air deteriorate the performance of various mechanical devices that work through the gas such as the air and corrode each part of the machine to shorten its lifespan, and in particular, adsorb foreign substances such as dust. This is because it provides a good habitat for microorganisms such as mold and contaminates the gas such as air.
Among the methods for removing liquid components such as moisture from gas such as air, centrifugal separation using a specific gravity difference between gas and liquid is well known. The centrifugal separation type is simpler in structure than the condensation cooling type using the refrigeration cycle, the absorption type using the solid adsorbent, the absorption type using the drying agent, the filter type, and the maintenance is easy.
The patent cited below relates to an oil separator which removes oil components from a refrigerant in a gas phase compressed in an air conditioner, and proposes the simplest structure of the centrifugal type. The oil separator consists of a cylindrical vessel and an inlet and outlet tube of refrigerant through which the refrigerant passes. The inlet pipe passes through a point close to the side wall portion away from its center at the top of the container and is curved to face the inner wall inside the container. The outlet pipe is in the form of a straight pipe passing through the center of the upper surface of the container. The compressed gaseous refrigerant introduced into the vessel through the inlet tube is ejected from the end of the inlet tube toward the inner wall of the vessel and flows in a vortex along the inner wall surface and moves through the centrally located outlet tube. As such, when the refrigerant flows in the vessel in a vortex form, an oil component having a larger specific gravity than the refrigerant in the gas phase is attached to the inner wall of the vessel by centrifugal force, and then flows down along the inner wall of the vessel by gravity to form the lower portion of the vessel. It is discharged to the outside through the discharge pipe.
Such centrifugal oil separators are useful for removing oil components from the refrigerant compressed into the gas phase, as well as for removing moisture from the compressed air.
The centrifugal formula proposed in the above-mentioned patent document is extremely simple in structure and efficient without compromising the compression efficiency of the gas, but has the following problems to be solved.
First, in order to maintain the compression efficiency of the gas passing through the container, the outlet of the lower part of the container must be closed at all times, so that the centrifuged liquid is temporarily stored in the lower part of the container, and the temporarily stored liquid is a gas circulating inside the container. Since it is exposed to, part of it is remixed with the gas, and the removal efficiency thereof is lowered.
Second, while the refrigerant pipe line and the compressed air line are piped in a straight line, the inlet pipe and the outflow pipe proposed in the above-mentioned patent document are vertically side by side, so it is not easy to vertically connect them in the middle of the straight pipe. not.
Third, in order to keep the liquid component removal efficiency good and constant, the position of the inlet and outlet tubes with respect to the container and the degree of curvature of the inlet tubes should be constant. However, the proposed prior patent did not suggest a means for standardization. In the end, it was difficult to secure reliability because the characteristics were not constant for each product due to manufacturing and assembly errors.
SUMMARY OF THE INVENTION An object of the present invention in view of these problems is to provide a gas-liquid separator that is improved in a structure that can be standardized to minimize remixing of the centrifuged liquid and to facilitate assembly and installation and to exhibit a certain characteristic.
A first feature of the present invention for achieving the above object is, having a tubular body forming a cylindrical space, and having an upper cap coupled to the upper end of the body to block the upper end of the space, the upper cap has an external gas pipe Two piping connectors capable of connecting the middle of the line, the inlet of the gas passing in the longitudinal direction at a distance from the center thereof so as to communicate the connector with one side thereof, and with the other connector thereof The outlet port of the gas penetrating in the longitudinal direction is formed at the center portion, and the inlet port is connected to a curved vortex forming tube to blow out the gas toward the inner wall of the body, and the outlet port is a straight pipe for allowing gas to flow out from the center portion of the space. It is to connect the type of spill guide.
A second feature of the present invention is to form the two pipe connectors of the first feature so as to lie in a straight line in the transverse direction so that the external gas pipe lines can be connected on the same line.
A third feature of the present invention is to interconnect the inlet and the vortex forming tube of the first feature with separate elbows.
A fourth feature of the present invention is to provide a removable cap under the intermediate cap having an intermediate cap coupled to the lower end of the body in the first feature, and a separate container for collecting the liquid components centrifuged inside the body. It is.
A fifth feature of the present invention is to form a hole in the intermediate cap of the fourth feature with a hole for passing the centrifuged liquid component through the container while blocking the gas forming the vortex inside the body.
A sixth aspect of the present invention is to provide a holder for enclosing the container in the fourth aspect, so that the holder can be detachably fitted to the intermediate cap while the container is stored.
The seventh feature of the present invention forms an outlet for discharging liquid to the outside at the bottom of the container in the fourth to sixth features, by using a float to drop the outlet by gravity action at all times and the collection As the liquid level rises, the outlet is automatically opened.
Eighth feature of the present invention is a vertically long shape that the water container in the seventh feature as a transparent or translucent material that can be seen through the inside, the level in the container of the transparent or translucent material can be confirmed in the holder To form a perspective sphere.
The gas-liquid separator according to the first aspect of the present invention described above standardizes parts such as a container main body, an upper cap, a curved vortex forming tube, and a straight pipe type outlet pipe, and is easy to assemble. The connection position of the gas pipe is constant, so that defects caused by manufacturing, assembly and installation errors can be minimized. In addition, the reliability thereof can be improved by certain characteristics such as vortex formation conditions and centrifugal action in the installed state.
According to the second aspect of the present invention, the middle of the horizontal gas pipe is cut in a predetermined width, and then the one pipe and the other pipe, which are broken and divided into two sides, are connected to each opening of the inlet and the outlet pipe formed in the side portion of the upper cap. In this case, since the openings of the inlet and the outlet of the side portion of the upper cap are formed in a straight line, the work is simply completed without the need to bend the one side pipe and the other side pipe and sealing the gas to prevent leakage. can do. Therefore, the installation is very easy, as well as the verticality of the container body can be stably maintained, thereby providing the effect of ensuring maximum performance.
According to the third aspect of the present invention described above, the shape of the vortex forming tube can be simplified by replacing a part of the vortex forming tube with an elbow conventionally standardized. That is, the effect is provided that can be manufactured easily and uniformly, for example, to cut a part of the threaded pipe.
According to the fourth aspect of the present invention described above, it is possible to clean the inside of the main body by separating the separate container, thereby providing an easy maintenance effect.
According to the fifth aspect of the present invention, the liquid collected in the container can be prevented from being remixed with the outflowing gas in the process of flowing out the gas after circulating the inside of the main body in the form of vortex, thereby improving liquid removal efficiency. The effect is provided.
According to the sixth aspect of the present invention, the holder is made of a high-elastic material such as plastic, for example, and the container can be easily detached by fitting, for example, and the effect of preventing damage to the container from external impact. Is provided.
According to the seventh aspect of the present invention described above, the effect of automatically discharging the centrifuged liquid is provided for the continuous operation without interrupting the operation of the target machine.
According to the eighth aspect of the present invention described above, it is possible to check the water level or the float operation state in the container from time to time, so that the effect of enabling the action in advance in the event of the operation of the float is provided.
1 is an external perspective view of a gas-liquid separator according to a preferred embodiment of the present invention.
Figure 2 is an exploded perspective view illustrating the assembly structure of the gas-liquid separator according to a preferred embodiment of the present invention.
Figure 3 is a longitudinal cross-sectional view illustrating the operation of the gas-liquid separator according to a preferred embodiment of the present invention.
Figure 4 is a cross-sectional view illustrating the principle of vortex formation of the gas-liquid separator according to a preferred embodiment of the present invention.
One type of gas-liquid separator according to a preferred embodiment of the present invention is shown in FIGS. These drawings are merely examples for understanding the present invention, and some elements may be different from the actual items such as omitting or exaggerating.
Referring to FIG. 1, the gas-liquid separator of the present invention may be divided into a
Referring to FIG. 2, the components constituting the
The
The
The
The
The
The
The
The
In FIGS. 2 and 3,
The gas-liquid separator carried out as shown in FIG. 3 is connected to the
Centrifugal force acts on the gas moving in the vortex (W) form in the space in the
The centrifuged liquid component passes through the hole (63) formed in the blocking portion (62) of the intermediate cap (60), falls to the container (70), and accumulates in the container (70). The
On the other hand, since the liquid level in the
The present invention will be more variously possible in various forms in addition to the forms described above and illustrated in the drawings.
10: main body, 11: inner wall, 20: upper cap, 22, 23: piping connection, 24: inlet, 25: outlet, 30: elbow, 40: vortex forming tube, 50: outlet guide tube, 60: intermediate cap, 62: cutout, 63: hole, 70: container, 71: outlet, 80: holder, 81: sight glass, 90: float valve
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100068783A KR20120008124A (en) | 2010-07-16 | 2010-07-16 | Gas-liquid separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100068783A KR20120008124A (en) | 2010-07-16 | 2010-07-16 | Gas-liquid separator |
Publications (1)
Publication Number | Publication Date |
---|---|
KR20120008124A true KR20120008124A (en) | 2012-01-30 |
Family
ID=45613185
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020100068783A KR20120008124A (en) | 2010-07-16 | 2010-07-16 | Gas-liquid separator |
Country Status (1)
Country | Link |
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KR (1) | KR20120008124A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019098617A1 (en) * | 2017-11-15 | 2019-05-23 | 이준범 | Gas-liquid separator for compressed air |
KR20190060819A (en) * | 2016-10-11 | 2019-06-03 | 아틀라스 캅코 에어파워, 남로체 벤누트삽 | Liquid separator |
KR20220049505A (en) * | 2019-06-14 | 2022-04-21 | 엑스-에너지 엘엘씨 | A system for recovering entrained particles from an exhaust gas stream |
-
2010
- 2010-07-16 KR KR1020100068783A patent/KR20120008124A/en not_active Application Discontinuation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20190060819A (en) * | 2016-10-11 | 2019-06-03 | 아틀라스 캅코 에어파워, 남로체 벤누트삽 | Liquid separator |
US11130085B2 (en) | 2016-10-11 | 2021-09-28 | Atlas Copco Airpower, Naamloze Vennootschap | Liquid separator |
WO2019098617A1 (en) * | 2017-11-15 | 2019-05-23 | 이준범 | Gas-liquid separator for compressed air |
KR20220049505A (en) * | 2019-06-14 | 2022-04-21 | 엑스-에너지 엘엘씨 | A system for recovering entrained particles from an exhaust gas stream |
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Legal Events
Date | Code | Title | Description |
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A201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
E601 | Decision to refuse application |