Generation apparatus for dissolving gas in liquid and fluid nozzle

Abstract

A generation apparatus for dissolving gas in liquid includes a sealed dissolving tank, a gas supply tube, a liquid supply set, and a fluid nozzle, wherein the sealed dissolving tank having a liquid inlet tube and a liquid outlet tube; a gas chamber formed inside the tank above liquid level; the gas supply tube supplying gas into gas chamber; the fluid nozzle disposed inside the tank; the liquid supply set supplying liquid to the fluid nozzle; the fluid nozzle disposed with at least a gas inlet and at least a liquid bubble inlet at different locations on shell wall; the gas inlet connected to a gas tube to the gas chamber, and the liquid bubble inlet located below the liquid level inside the tank. As such, the fluid nozzle performs at least two dissolving operations to miniaturize the bubbles to increase contact surface and improve dissolving efficiency.

Claims

1. A generation apparatus for dissolving gas in liquid, comprising: a sealed dissolving tank, having a liquid inlet tube and a liquid outlet tube, a gas chamber being formed inside the sealed dissolving tank above the liquid level; a gas supply tube, linked to the sealed dissolving tank and connected to the gas chamber for supplying gas into the gas chamber; a liquid supply set, further comprising a liquid transport tube, a pump, a gas sucking tube, and a liquid supply tube, the pump being connected to both the liquid transport tube and the liquid supply tube, the liquid transport tube being connected to the sealed dissolving tank and located below the liquid level, the gas sucking tube having one end connected to the liquid transport tube and the other end connected to the sealed dissolving tank for linking with the gas chamber, the liquid transport tube supplying the liquid to the pump, the pump pressurizing the liquid for outputting by the liquid supply tube; the liquid supply tube extending into the sealed dissolving tank; and a fluid nozzle, disposed inside the sealed dissolving tank, the fluid nozzle having a solution channel and being disposed with at least a gas inlet and at least a liquid bubble inlet at different locations on a shell wall of the fluid nozzle; both the gas inlet and the liquid bubble inlet being connected to the solution channel; the solution channel having an entrance connected to the liquid supply tube, and an exit located below the liquid level inside the sealed dissolving tank; the gas inlet further connected to a gas tube to the gas chamber, and the liquid bubble inlet located below the liquid level inside the sealed dissolving tank, wherein the solution channel passing through the fluid nozzle and comprising a plurality of channel segments of different diameters linked in series, the plurality of channel segments comprising: a first segment, a second segment, a third segment, and a fourth segment; the solution channel entrance located at an entrance of the first segment; the gas inlet being linked to the second segment; the liquid bubble inlet being linked to the third segment; the solution channel having an exit located at the exit of the fourth segment; a path of the solution channel entrance and the first segment having a cross-sectional area larger than a cross-sectional area of a path of the second segment; a path of the third segment having a cross-sectional area larger than a cross-sectional area of the second segment; a diameter of the third segment shrinking gradually along a flow direction; a diameter of the fourth segment increasing gradually along the flow direction; a joint of the third segment and the fourth segment forming a tube throat with a smaller diameter.

2. The generation apparatus for dissolving gas in liquid as claimed in claim 1, wherein the gas inlet is closer to the channel solution entrance than the liquid bubble inlet to the channel solution entrance.

3. The generation apparatus for dissolving gas in liquid as claimed in claim 1, wherein a joint between the gas inlet and the solution channel has a cross-section area smaller than the cross-section area of the solution channel entrance.

4. The generation apparatus for dissolving gas in liquid as claimed in claim 1, wherein a joint between the liquid bubble inlet and the solution channel has a cross-section area larger than the cross-section area of the solution channel entrance.

5. A fluid nozzle, applicable to a generation apparatus for dissolving gas in liquid, comprising a solution channel, the fluid nozzle being disposed with at least a gas inlet and at least a liquid bubble inlet at different locations on a shell wall of the fluid nozzle; both the gas inlet and the liquid bubble inlet being connected to the solution channel; the solution channel having an entrance connected to the liquid supply tube, and an exit located below the liquid level inside the sealed dissolving tank; the gas inlet further connected to a gas tube to the gas chamber, and the liquid bubble inlet located below the liquid level inside the sealed dissolving tank, wherein the solution channel passing through the fluid nozzle and comprising a plurality of channel segments of different diameters linked in series, the plurality of channel segments comprising: a first segment, a second segment, a third segment, and a fourth segment; the solution channel entrance located at an entrance of the first segment; the gas inlet being linked to the second segment; the liquid bubble inlet being linked to the third segment; the solution channel having an exit located at the exit of the fourth segment; a path of the solution channel entrance and the first segment having a cross-sectional area larger than a cross-sectional area of a path of the second segment; a path of the third segment having a cross-sectional area larger than a cross-sectional area of the second segment; a diameter of the third segment shrinking gradually along a flow direction; a diameter of the fourth segment increasing gradually along the flow direction; a joint of the third segment and the fourth segment forming a tube throat with a smaller diameter.

6. The fluid nozzle as claimed in claim 5, wherein the gas inlet is closer to the channel solution entrance than the liquid bubble inlet to the channel solution entrance.

7. The fluid nozzle as claimed in claim 5, wherein a joint between the gas inlet and the solution channel has a cross-section area smaller than the cross-section area of the solution channel entrance.

8. The fluid nozzle as claimed in claim 5, wherein a joint between the liquid bubble inlet and the solution channel has a cross-section area larger than the cross-section area of the solution channel entrance.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) 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:

(2) FIG. 1 shows a schematic view of the structure of a known apparatus using diffuser;

(3) FIG. 2 shows a schematic view of the structure of a known apparatus using Venturi tube;

(4) FIG. 3 shows a schematic view of an embodiment of the present disclosure;

(5) FIG. 4 shows a schematic view of an embodiment of the fluid nozzle of the present disclosure;

(6) FIG. 5 shows a cross-sectional view of an embodiment of the fluid nozzle of the present disclosure; and

(7) FIG. 6 shows a schematic view of the operation of the present disclosure.

DETAILED DESCRIPTION OF THE DISCLOSED EMBODIMENTS

(8) 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.

(9) FIG. 3 shows a schematic view of an embodiment of the present disclosure. The generation apparatus for dissolving gas in liquid of the present disclosure includes: a sealed dissolving tank 3, a gas supply tube 4, a fluid nozzle 5, and a liquid supply set 6.

(10) The sealed dissolving tank 3 is a sealed container with a liquid inlet tube 31 and a liquid outlet tube 32. The liquid enters the tank through the liquid inlet tube 31, after internal operation, and a high density gas solution flows out from the liquid outlet tube 32. A gas chamber 33 is formed inside the sealed dissolving tank 3 above the liquid level. The gas chamber 33 is for housing the gas to be dissolved. The gas supply tube 4 is linked to the sealed dissolving tank 3 and is connected to the gas chamber 33 for supplying gas into the gas chamber 33. The gas is to be dissolved in the liquid. The sealed dissolving tank further includes a gas vent tube 35 connected to the gas chamber 33. The gas vent tube 35 is disposed with a automatic valve 36, which will be automatically opened to vent out a part of gas to maintain normal operation when the pressure inside the sealed dissolving tank 3 reaching a default threshold.

(11) The fluid nozzle 5 is disposed inside the sealed dissolving tank 3. A support frame 34 is disposed inside the tank to fix the position of the fluid nozzle 5. The fluid nozzle 5 can suck in gas and the liquid bubble of mixed gas and liquid. After twice stirring, the bubbles are miniaturized to increase contact surface between the gas and the liquid to accelerate dissolving. As shown in FIG. 4 and FIG. 5, the fluid nozzle 5 includes a solution channel 51, and also includes at least a gas inlet 52 and at least a liquid bubble inlet 53 at different locations on the shell wall. Both the gas inlet 52 and the liquid bubble inlet 53 are connected to the solution channel 51. The gas inlet 52 is also connected to a gas tube 56, leading to the gas chamber 33. The solution channel 51 passes through the fluid nozzle 5 and includes a plurality of channel segments of different diameters linked in series. As in the present embodiment, the solution channel 51 includes a first segment 511, a second segment 512, a third segment 513 and a fourth segment 514. The solution channel 51 has an entrance 54 located at the entrance of the first segment 511. The gas inlet 52 is linked to the second segment 512. The liquid bubble inlet 53 is linked to the third segment 513. The solution channel 51 has an exit 55 located at the exit of the fourth segment 514. The path of solution channel entrance 54 and the first segment 511 has a cross-section area larger than the cross-section area of the path of the second segment 512. Because the cross-section area shrinks, the fluid velocity increases. The negative pressure caused by the high speed jet current results in the sucking in of the gas through the gas inlet 52. Although the path cross-section of the third segment 513 is larger than the second segment 512, the velocity here is higher than the velocity at the outer wall of the fluid nozzle 5. With the high speed negative pressure and the abrupt enlarged part of the third segment 513, a swirl will be generated inside the third segment 513. The liquid bubble inlet 53 sucks in un-dissolved gas (bubble) and liquid. The swirl generates a shear force to further break down the bubbles into smaller bubbles to increase contact surface between the gas and the liquid and improve the dissolving efficiency. In addition, the diameter of the third segment 513 gradually shrinks along the flow direction, while the diameter of the fourth segment 514 gradually increases along the flow direction. The joint of the third segment 513 and the fourth segment 514 forms a tube throat with smaller diameter. As such, the velocity is accelerated and when the liquid flows out from the solution channel exit 55, a jet current is generated to further accelerate the stirring inside the tank to improve the dissolving.

(12) The liquid supply set 6 is for supplying pressurized liquid to the fluid nozzle 5. The liquid supply set 6 includes a liquid transport tub 61e, a pump 62 and a liquid supply tube 63. The pump 62 is connected to the liquid transport tube 61 and the liquid supply tube 63. The liquid transport tube 61 supplies the liquid to the pump 62, and the pump 62 pressurizes the liquid for outputting by the liquid supply tube 63. In the present embodiment, the liquid transport tube 61 is connected to the seal dissolving tank 3 and located below the surface of the liquid to supply the liquid directly inside the tank. However, in other embodiments, the liquid can also be from external liquid supply device through the liquid transport tube 61 or connecting the liquid transport tube 61 to the liquid inlet tube 31 for supplying the liquid. The liquid supply tube 63 extends into the sealed dissolving tank 3, and is connected to the solution channel entrance 54 of the fluid nozzle 5. In the present embodiment, the support frame 34 for fluid nozzle 5 can also be omitted. Instead, a liquid supply tube 63 of sufficient diameter and strength can be directly connected to the fluid nozzle 5.

(13) the fluid nozzle being disposed inside the sealed dissolving tank, the fluid nozzle having a solution channel and being disposed with at least a gas inlet and at least a liquid bubble inlet at different locations on shell wall of fluid nozzle; both the gas inlet and the liquid bubble inlet being connected to the solution channel; the solution channel having an entrance connected to the liquid supply tube, and an exit located below the liquid level inside the tank; the gas inlet further connected to a gas tube to the gas chamber, and the liquid bubble inlet located below the liquid level inside the tank.

(14) The liquid supply set 6 of the present disclosure further includes a gas sucking tube 64, with one end connected to the liquid transport tube 61 and the other connected to the gas chamber 33 of the sealed dissolving tank 3. When the pump 62 operates and the liquid transport tube 61 transports liquid, the gas is also sucked in through the gas sucking tube 64 so that a large amount of bubbles is inside the liquid. Because the pump 62 operates by vane centrifugal pressurization, the vane can further break down the bubble into smaller bubbles during the centrifugal pressurization, and transports the smaller bubbles through the liquid supply tube 63 to the fluid nozzle 5. This process also increases the surface area of the bubble to improve gas dissolving.

(15) The following describes the operation of the generation apparatus. FIG. 6 shows a schematic view of the operation of the present disclosure. As shown in FIG. 6, the liquid enters the sealed dissolving tank 3 through the liquid inlet tube 31 so that the liquid level maintains at a suitable level. The gas to be dissolved enters the gas chamber 33 through the gas supply tube 4. The liquid supply set 6 starts to operate to transport the liquid to the fluid nozzle 5. As described earlier, when the pump 62 operates, the gas is also sucked in during sucking in the liquid. During the pump 62 pressurization, the bubbles are broken down into smaller bubbles so that a part of gas is dissolved in the liquid. The un-dissolved smaller bubbles and the liquid are outputted to the solution channel 51 through the liquid supply tube 63.

(16) When the liquid enters the solution channel 51 of the fluid nozzle, with the pressure difference caused by different diameters of different segments of the solution channel 51 and the resulted negative pressure, a large amount of gas is sucked through the gas tube 56 to the gas inlet 52. After gas-liquid dissolving, the solution is outputted through the solution channel exit 55. The un-dissolved gas surfaces and passes the liquid bubble inlet 53. Because the speed inside the solution channel 51 is higher than the speed outside, a negative pressure causes the nearby liquid and bubbles are sucked in through the liquid bubble inlet 53, which causes further swirl inside the solution channel 51. The shear force from the swirl breaks down the bubbles into smaller bubbles to further improve dissolving. The double cyclic operation increases the contact area between the gas and the liquid. The vertical cyclic operation inside the tank can prolong the time the bubbles remain in the liquid. With increased contact surface and prolonged contact time, the dissolving efficiency improves.

(17) In summary, the present disclosure uses a set of fluid nozzle inside the sealed dissolving tank to perform the first dissolving operation, and then sucks in the un-dissolved gas and liquid again to break down the bubbles for efficient dissolving. In addition, the pump and the gas sucking tube of the liquid supply set perform another bubble miniaturization for efficient dissolving. As such, three times of dissolving operation, combined with the vertical cyclic operation inside the sealed dissolving tank to prolong contact time. Hence, the present disclosure can generate a large amount of high density gas solution and use gas efficiently in a unit time.

(18) 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.