The present application is based on, and claims priority form, Taiwan Patent Application No. 103205686, filed Apr. 2, 2014, the disclosure of which is hereby incorporated by reference herein in its entirety.
The technical field generally relates to a debubbler apparatus, and in particular, more related to a technique using fluid to concentrate the gas in a liquid pipe to the central part of the debubbler apparatus and using buoyancy to surface for collection and venting.
In chemical engineering process, the bubbles often exist in pipes to affect the yield rate of the process. The known technique often employs a temporary storage tank to reduce the flow speed so that the bubbles surfacing due to buoyancy are then collected and vented.
1. If the flow speed inside the tank 10 is faster than the speed at which the bubbles surface, the bubbles will flow along with the liquid from the liquid outlet tube 12 and the de-bubble effect is failed to achieved.
2. If the bubbles are very small, the surfacing speed is too slow to be effectively surfacing to the top portion inside the tank 10.
3. The flow speed inside the tank 10 must be slow, which may easily cause residual deposited at the bottom of the tank 10.
4. The size of the tank 10 must be larger than the size of the tubes to achieve slow flow speed, which takes up more space.
An exemplary embodiment describes a debubbler apparatus to allow a liquid to enter a tank at a specific angle. Combined with the specific shape of the tank, the kinetic of the liquid inside the tank causes a swirl current, resulting in a centrifugal force to make the liquid and the gas to flow at different speeds so that the gas is easily concentrated around the center and surfaces due to the buoyancy. The surfaced gas is collected and vented to accomplish the object of de-bubbling.
To achieve the above object, the present disclosure provides a debubbler apparatus, including a debubbler tank, and a liquid inlet tube, a liquid outlet tube and a gas venting tube, all connected to the debubbler tank; wherein the debubbler tank including a first tank and a second tank, vertically connected to each other; the second tank starting to shrink in diameter gradually from the top connected to the first tank downward; when the liquid entering the debubbler tank, a gas chamber being formed inside the first tank above the liquid level; the liquid inlet tube being disposed at the first tank and linked to the inside of the first tank; the liquid outlet tube being disposed at the second tank and connected to the bottom of the second tank; the gas venting tube being disposed at the first tank and connected to the gas chamber inside the first tank.
With the present apparatus, after the liquid enters the tank, the liquid kinetic causes a swirl. The flow speed inside the pipes of the system will not slow down to cause the residual deposition problem. No additional driving device is necessary to drive the liquid. As such, the size can be kept small.
The foregoing will become better understood from a careful reading of a detailed description provided herein below with appropriate reference to the accompanying drawings.
The embodiments can be understood in more detail by reading the subsequent detailed description in conjunction with the examples and references made to the accompanying drawings, wherein:
In the following detailed description, for purpose of explanation, numerous specific details are set forth in order to provide a thorough understanding of the disclosed embodiments. It will be apparent, however, that one or more embodiments may be practiced without these specific details. In other instances, well-known structures and devices are schematically shown in order to simplify the drawing.
The debubbler tank 2 is a sealed hollow container, including a first tank 21 and a second tank 22, vertically connected to each other. The first tank 21 has a cylinder shape, with the same diameter for most of the part. A liquid inlet hole 211 is disposed on the wall of the first tank 21. The angle at which the liquid enters the first tank 21 has a direct impact on the debubbler effect. As shown in
The liquid inlet tube 3 is disposed at the first tank 21 and linked to the liquid inlet hole 211. The liquid outlet tube 4 is disposed at the second tank 22 at the location on a vertical side wall at the bottom of the second tank 22. The liquid outlet tube 4 is connected to the liquid outlet hole 221. To eliminate the bubbles from the pipes in the system, the liquid inlet tube 3 and the liquid outlet tube 4 are disposed in a liquid supply system serially. The gas venting tube 5 is disposed at the first tank 21 and connected to the gas venting hole 212 of the first tank 21.
It will be apparent to those skilled in the art that various modifications and variations can be made to the disclosed embodiments. It is intended that the specification and examples be considered as exemplary only, with a true scope of the disclosure being indicated by the following claims and their equivalents.
Number | Date | Country | Kind |
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103205686 | Apr 2014 | TW | national |