A device for treating at least one liquid, comprising at least one vacuum column and a foam collector equipped with a gravity-fed drainage system operating by vacuum.

The drainage system with a permanent liquid column in the conduit addresses the need for automatic foam collector emptying in liquid treatment devices, enhancing operational efficiency and reducing costs and maintenance.

FR3162431A1Pending Publication Date: 2025-11-28COLDEP DEVEMENT
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Patent Information

Application Number
FR2024005188
Authority / Receiving Office
FR · FR
Patent Type
Applications
Current Assignee / Owner
Filing Date
2024-05-22
Publication Date
2025-11-28

AI Technical Summary

Technical Problem

Existing liquid treatment devices require interruption of the vacuum pump operation and incur increased costs and failure risks due to the presence of level sensors, drain valves, and pumps during foam collector emptying.

Method used

A drainage system with a permanent liquid column maintained in the drainage conduit, controlled automatically without moving components like valves or pumps, ensuring the foam collector is emptied efficiently.

Benefits of technology

Enables automatic control of the liquid level in the foam collector, reducing costs and maintenance requirements while maintaining continuous operation.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention relates to a device for treating at least one liquid comprising at least one vacuum column and a foam collector equipped with a gravity-fed drainage system operating by vacuum. The invention relates to a device for treating at least one liquid comprising: at least one vacuum column (54), at least one vacuum generator (52) configured to generate in operation a first height of liquid (H54) in the vacuum column (54), at least one foam collector (64), at least one drainage system (72) for the foam collector (64) comprising: at least one drainage conduit (76) connected to a drainage orifice (64.2) of the foam collector (64), at least one system for maintaining (80) a permanent liquid column of a second liquid height (H76) in the drainage conduit (76), the second liquid height (H76) being between the first liquid height (H54) and the first liquid height (H54) + 30% of the first liquid height.Figure 2.
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Description

Title of the invention: Device for treating at least one liquid comprising at least one vacuum column and a foam collector equipped with a gravity-fed drainage system operating by vacuum

[0001] The present application relates to a liquid treatment device comprising a vacuum column and a foam collector equipped with a gravity drainage system operating by vacuum.

[0002] According to an embodiment visible in [Fig.1] and described in document FR2914296, a water treatment device 10 for a basin 12 comprises a set of riser and downramps 14, a supply conduit for the water to be treated 16 connecting the basin 12 and the set of riser and downramps 14, and a treated water return conduit 18 connecting the set of riser and downramps 14 and the basin 12. The basin 12 has a liquid height H12.

[0003] The riser and downr assembly 14, also called a vacuum column, comprises an enclosure 14.1, vertical partitions 14.2 positioned in the enclosure 14.1 and delimiting at least one riser 14.3 and at least one downr 14.4 as well as at least one pressurized gas injection system 14.5 which opens into the riser 14.3.

[0004] The enclosure 14.1 contains a first liquid phase PLI which has a first liquid surface SL1 and a first gaseous space 20 located above the first liquid surface SL1. The latter has a liquid height H14.

[0005] The treatment device 10 also includes a vacuum pump 22, connected to the first gaseous sky 20, allowing a depression to be obtained at the level of the first gaseous sky 20 and to form a depression in the rising column 14.3.

[0006] During operation, foam forms at the level of the first gaseous sky 20.

[0007] The treatment device 10 includes a foam collector 24 which includes a sealed enclosure 24.1 containing a second liquid phase PL2 and a second gaseous space 26 located above the second liquid phase PL2.

[0008] The foam collector 24 includes a drain orifice 24.2 opening into the lower part of the enclosure 24.1.

[0009] In addition, the treatment device 10 includes at least a first conduit 28 connecting the first gaseous space 20 of the rising and falling column assembly 14 and the second gaseous space 26 of the foam collector 24 as well as to the minus a second conduit 30 connecting the second gaseous sky 26 of the foam collector 24 and the vacuum pump 22.

[0010] After a certain period of operation, the foam collector 24 must be emptied.

[0011] According to one embodiment, the treatment device 20 includes a drainage system 32 which comprises a drainage conduit 32.1 connected to the drainage port 24.2 of the foam collector 24, a drainage valve 32.2, at least one level sensor 32.3 positioned in the enclosure 24.1 of the foam collector 24, a drainage pump 32.4 for emptying the enclosure 24.1 of the foam collector 24 and an automation system for managing the operation of the drainage valve 32.2 and the drainage pump 32.4.

[0012] This embodiment is not satisfactory because the treatment must be interrupted when emptying the foam collector 24, by stopping the operation of the vacuum pump 22.

[0013] According to another issue, the presence of a level sensor 32.3, a drain valve 32.2 and a drain pump 32.4 leads to an increase in the cost of the treatment device 10 and the risks of failure.

[0014] The present invention aims to remedy all or part of the drawbacks of the prior art.

[0015] To this end, the invention relates to a device for treating at least one liquid comprising: a. at least one set of rising and falling columns comprising a first sealed enclosure containing a first liquid phase with a first liquid surface and a first gaseous space situated above the first liquid surface, b. at least one foam collector comprising a second sealed enclosure containing a second liquid phase with a second liquid surface and a second gaseous space situated above the second liquid surface, the second enclosure comprising at least one drain port, c. at least one vacuum generator configured to generate, in operation, a first liquid height in the riser and downriller assembly, d. at least one first conduit connecting the first and second gaseous heavens, e. at least one second conduit connecting the second gaseous heaven and the vacuum generator, f. as well as at least one drainage system comprising at least one drainage conduit connected to the drainage port of the second chamber of the foam collector.

[0016] According to the invention, the drainage system includes at least one system for maintaining a permanent liquid column of a second liquid height in the drainage conduit, the second liquid height being between the first liquid height and the first liquid height + 30% of the first liquid height.

[0017] This solution allows for the automatic control of the level of the second liquid surface in the foam collector without moving components such as a valve or pump. It also reduces the costs of the treatment device and its maintenance.

[0018] Other features and advantages will become apparent from the following description of the invention, given by way of example only, with reference to the accompanying drawings, among which:

[0019] [Fig. 1] is a schematic representation of a processing device illustrating an embodiment of the prior art, and

[0020] [Fig.2] is a schematic representation of a processing device illustrating a first embodiment of the invention, and

[0021] [Fig.3] is a schematic representation of a processing device illustrating a second embodiment of the invention.

[0022] According to embodiments visible in figures 2 and 3, a treatment device 50 for a liquid contained in at least one reservoir 52 comprises at least one set of rising and falling columns 54 also called a vacuum column, at least one supply conduit 56 for the liquid to be treated connecting the reservoir 52 and the set of rising and falling columns 54, and at least one return conduit 58 for the treated liquid connecting the set of rising and falling columns 54 and the reservoir 52.

[0023] According to one application, the treated liquid is an effluent. Of course, the invention is not limited to this application.

[0024] According to one embodiment, the reservoir 52 contains a liquid which has a reservoir liquid surface SL52. The reservoir 52 has a liquid height H52 (or a first hydrostatic pressure) corresponding to the distance separating the bottom of the reservoir 52 and the reservoir liquid surface SL52.

[0025] The assembly of rising and falling columns 54 includes a first sealed enclosure 54.1 and at least one vertical partition 54.2, positioned in the first enclosure 54.1, delimiting at least one rising column 54.3 and at least one falling column 54.4.

[0026] According to one configuration, the riser and downr assembly 54 includes at least one gas injection system 54.5 configured to inject at least one gas into the riser 54.3.

[0027] According to one arrangement, the riser 54.3 is cylindrical and the downpipe 54.4 is positioned around the riser 54.3 and is in the form of an annular conduit. In addition, the gas injection system 54.5 is configured to inject pressurized gas at the base of the riser 54.3.

[0028] Of course, the invention is not limited to this arrangement for the gas injection system 54.5 and the rising and falling columns 54.3, 54.4. To give an order of magnitude, the set of rising and falling columns 54 has a height greater than 1 m, generally several meters.

[0029] The first chamber 54.1 of the riser and downr column assembly 54 contains a first liquid phase PLI which has a first liquid surface SL1 and a first gaseous space 60 located above the first liquid surface SL1. The latter has a first liquid height H54 (or a vacuum pressure) corresponding to a distance measured in the vertical direction between the reservoir liquid surface SL52 of the reservoir 52 and the first liquid surface SL1 in the first chamber 54.1 of the riser and downr column assembly 54.

[0030] The treatment device 50 also includes at least one vacuum pump 62, connected to the first gaseous space 60, enabling a vacuum to be created at the level of the first gaseous space 60 and to form a vacuum in the riser 54.3. This vacuum pump 62 is configured to generate, during operation, a desired first liquid height H54 in the riser and descender assembly 54. In one configuration, the first liquid height H54 is approximately 5 m. The liquid height H52 of the reservoir 52 is approximately 1 m.

[0031] Of course, the invention is not limited to this embodiment. The vacuum pump 62 can be replaced by any vacuum generator configured to generate, during operation, a first liquid height H54 in the rising and falling column assembly 54.

[0032] The treatment device 50 comprises at least one foam collector 64 having a second sealed enclosure 64.1 in which a second liquid phase PL2 is formed, which has a second liquid surface SL2. The second enclosure 64.1 also contains a second gaseous space 66 located above the second liquid surface SL2.

[0033] The foam collector 64 includes at least one drain orifice 64.2 positioned at a low point of the second enclosure 64.1.

[0034] In addition, the treatment device 50 includes at least a first conduit 68 connecting the first gaseous space 60 of the rising and falling column assembly 54 and the second gaseous space 66 of the foam collector 64, thus that at least a second conduit 70 connects the second gaseous space 66 of the foam collector 64 and the vacuum pump 62. The first conduit 68 has a first end 68.1 which opens into the first chamber 54.1 of the riser and downramp assembly 54 above the first liquid surface SL1, in the first gaseous space 60, and a second end 68.2 which opens into the second chamber 64.1 of the foam collector 64 above the second liquid surface SL2, in the second gaseous space 66. The second conduit 70 has a first end 70.1 which opens into the second chamber 64.1 of the foam collector 64, above the second liquid surface SL2 in the second gaseous space 66, and a second end 70.2 connected to the vacuum pump 62.

[0035] The reservoir 52, the riser and downr assemblies 54, the foam collector 64 and the vacuum pump 62 are not described in further detail as they may be identical to those of the prior art.

[0036] The treatment device 50 includes at least one drainage system 72 configured to empty at least partially the foam collector 64 and evacuate the second liquid phase PL2 present in the second enclosure 64.1 as soon as the second liquid surface SL2 reaches a trigger height.

[0037] According to a first embodiment visible in [Fig.2], the drainage system 72 comprises at least one container 74 which has a bottom 74.1 and at least one outlet 74.2 offset upwards relative to the bottom 74.1.

[0038] This container 74 contains the second liquid phase PL2, discharged from the foam collector 64, which has a third liquid surface SL3 separated from the bottom 74.1 by a distance (measured along the vertical direction) equal to that separating the bottom 74.1 and the outlet orifice 74.2. Thus, the third liquid surface SL3 is located at the same height as the outlet orifice 74.2 and the second liquid phase PL2 contained in the container 74 automatically exits by overflow through the outlet orifice 74.2.

[0039] The drainage system 72 also includes at least one drainage conduit 76, positioned under the second enclosure 64.1 of the foam collector 64, which has a first end 76.1 connected to the drainage port 64.2 of the foam collector 64 and a second end 76.2 located in the container 74 under the third liquid surface SL3. Thus, the second end 76.2 is separated from the bottom 74.1 by a distance less than that separating the bottom 74.1 and the opening 74.2. During operation, the second end 76.2 of the drainage conduit 76 is always immersed in the second liquid phase PL2 present in the container 74.

[0040] According to a second embodiment visible in [Fig. 3], the drainage system 72 comprises at least one drainage conduit 76, positioned under the second enclosure 64.1 of the foam collector 64, which has a first end 76.1 connected to the drainage port 64.2 of the foam collector 64 and a second end 76.2 as well as at least one non-return valve 78 located at the second end 76.2 of the drain conduit 76. For the present application, a non-return valve 78 is an element which permits flow in only one direction of the liquid, namely from the first end 76.1 to the second end 76.2.

[0041] Regardless of the embodiment, the drainage system 72 includes at least one retention system 80 for a permanent liquid column of a second liquid height H76 in the drainage conduit 76, the second liquid height H76 corresponding to a distance measured in the vertical direction between the second and third liquid surfaces SL2, SL3 or between the second liquid surface SL2 and the second end 76.2 of the drainage conduit 76. According to the first embodiment, the retention system 80 includes a container 74 for retaining the second end 76.2 of the drainage conduit 76 in the second liquid phase PL2 present in the container 74. According to the second embodiment, the retention system 80 includes a non-return valve 78 located at the second end 76.2 of the drainage conduit 76.

[0042] The drainage system 72 includes at least one substantially vertical drainage conduit 76, positioned under the second enclosure 64.1 of the foam collector 64 to obtain gravity flow into the drainage conduit 76.

[0043] According to a particular feature, the second height of liquid H76 in the drain channel 76 is between the first height of liquid H54 and the first height of liquid H54 + 30% of the first height of liquid H54.

[0044] According to one embodiment, the second liquid height H76 in the drain channel 76 corresponds to the sum of the vacuum pressure (equivalent to the first liquid height H54) and a positive hydrostatic pressure H82, substantially equal to the first hydrostatic pressure H52 and of the order of 0.1 bar.

[0045] According to one configuration, the rising and falling column assembly 54 and the foam collector 64 are arranged so that the first and second liquid surfaces SL1, SL2 are substantially at the same height.

[0046] According to this configuration, the third liquid surface SL3 or the second end 76.2 of the drain conduit 76 is located below the reservoir liquid surface SL52. The third liquid surface SL3 and the reservoir liquid surface SL52 are separated by a height substantially equal to the hydrostatic pressure H82.

[0047] During operation, when the second liquid surface SL2 exceeds a height, measured from the third liquid surface SL3, greater than or equal to the first liquid height H54 plus the hydrostatic pressure H82, the vacuum generated by the vacuum pump 62 in the second chamber 64.1 is not sufficient to prevent the liquid from flowing into the drain channel 76. This The latter flows by gravity from the foam collector 64 to the second end 76.2 of the drain conduit 76.

[0048] This solution allows for the automatic control of the level of the second liquid surface SL2 in the foam collector 64 without any moving components such as a valve or pump. It also reduces the costs of the treatment device and its maintenance.

Claims

Demands

1. Device for treating at least one liquid comprising: a. at least one set of rising and falling columns (54) comprising a first sealed enclosure (54.1) containing a first liquid phase (PLI) with a first liquid surface (SL1) and a first gaseous space (60) situated above the first liquid surface (SL1), b. at least one foam collector (64) which includes a second sealed enclosure (64.1) containing a second liquid phase (PL2) with a second liquid surface (SL2) and a second gaseous sky (66) situated above the second liquid surface (SL2), the second enclosure (64.1) including at least one drain port (64.2), c. at least one vacuum generator (62) configured to generate in operation a first liquid height (H54) in the rising and falling column assembly (54), d. at least one first conduit (68) connecting the first and second gaseous stacks (60, 66), e. at least one second conduit (70) connecting the second gaseous sky (66) and the vacuum generator (62), f. as well as at least one drainage system (72) comprising at least one drainage conduit (76) connected to the drainage port (64.2) of the second enclosure (64.1) of the foam collector (64), g. characterized in that the drainage system (72) comprises at least one system for maintaining (80) a permanent liquid column of a second liquid height (H76) in the drainage conduit (76), the second liquid height (H76) being between the first liquid height (H54) and the first liquid height (H54) + 30% of the first liquid height.

2. Processing device according to the preceding claim, characterized in that the second liquid height (H76) in the drain conduit (76) is equal to the first liquid height (H54) increased by a positive hydrostatic pressure (H82) of the order of 0.1 bar.

3. Processing device according to any one of the preceding claims, characterized in that the rising and falling column assembly (54) and the foam collector (64) are arranged so that the first and second liquid surfaces (SL1, SL2) are substantially at the same height.

4. Processing device according to any one of the preceding claims, characterized in that the drain conduit (76) extends between a first end (76.1) connected to the drain port (64.2) of the second chamber (64.1) of the foam collector (64) and a second end (76.2) and in that the retaining system (80) includes at least one check valve (78) located at the second end (76.2) of the drain conduit (76), the second liquid height (H76) corresponding to a distance measured along the vertical direction between the second liquid surface (SL2) and the second end (76.2) of the drain conduit (76).

5. Processing device according to the preceding claim, characterized in that the processing device comprises at least one reservoir (52) which contains a liquid with a reservoir liquid surface (SL52) and in that the second end (76.2) of the drain conduit (76) is located below the reservoir liquid surface (SL52).

6. Processing device according to any one of claims 1 to 3, characterized in that the drain conduit (76) extends between a first end (76.1) connected to the drain port (64.2) of the second enclosure (64.1) of the foam collector (64) and a second end (76.2) and in that the holding system (80) comprises at least one container (74) which contains the second liquid phase (PL2) discharged from the foam collector (64) and has a third liquid surface (SL3), the second end (76.2) being positioned below the third liquid surface (SL3), the second liquid height (H76) corresponding to a distance measured along the vertical direction between the second and third liquid surfaces (SL2, SL3).

7. Processing device according to the preceding claim, characterized in that the processing device comprises at least one reservoir (52) which contains a liquid with a reservoir liquid surface (SL52) and in that the third liquid surface (SL3) is located below the reservoir liquid surface (SL52).

8. Processing device according to any one of claims 6 to 7, characterized in that the container (74) comprises at least one outlet orifice (74.2), the third liquid surface (SL3) being located at the same height as the outlet orifice (74.2)

9. Processing device according to any one of the preceding claims, characterized in that the drain conduit (76) is substantially vertical and positioned under the second enclosure (64.1) of the foam collector (64) to obtain gravity flow in the drain conduit (76).

Citation Information

Patent Citations

  • Treating aqueous effluent for extracting carbon dioxide and nitrogen gaseous compound useful in aquaculture in recirculated aqueous environment, comprises separating the compound from the effluent for obtaining the treated aqueous phase

    FR2914296A1

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    US11767235B2

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