阅读说明：本技术 模块化浮选法水处理设备 (Modularized flotation method water treatment equipment ) 是由 C·德尔·皮科洛 G·吉罗拉米 R·维切尔 N·维涅龙-拉罗萨 于 2020-02-13 设计创作，主要内容包括：浮选法水处理设备,其具有大致呈平行六面体形的组合体(1),组合体由模块(2、2a)联合而形成,所述组合体具有接触罐(3)、浮选罐(6)和已浮选泥浆排出装置,所述接触罐具有待处理水输送装置(4)和白水输送装置(5),所述浮选罐具有已处理水排出装置(7、7a),所述浮选罐由竖直壁(8)与所述接触罐隔开,其特征在于,所述接触罐(3)沿所述浮选罐(6)布置,并限定所述待处理水与所述白水接触的单独接触区域；并且,所述待处理水输送装置(4)设计成根据纵向水输送流使待处理水分配到所述接触罐中,浮选罐中的水分配流垂直于所述接触罐中的所述纵向水输送流。(Flotation process water treatment plant having a substantially parallelepiped-shaped assembly (1) formed by the union of modules (2, 2a), said assembly having a contact tank (3) with a treated water discharge (7, 7a), a flotation tank (6) separated from the contact tank by a vertical wall (8), and a floated sludge discharge, said contact tank having a treated water conveying device (4) and a white water conveying device (5), characterized in that the contact tank (3) is arranged along the flotation tank (6) and defines a separate contact zone where the water to be treated comes into contact with the white water; and the water conveying device (4) to be treated is designed to distribute water to be treated into the contact tank according to a longitudinal water conveying flow, the water distribution flow in the flotation tank being perpendicular to the longitudinal water conveying flow in the contact tank.)

1. Flotation process water treatment plant having a substantially parallelepiped-shaped combination (1) formed by the union of modules (2, 2a), said combination having a contact tank (3) with a treated water discharge (7, 7a), a flotation tank (6) and a floated sludge discharge, said flotation tank (6) being separated from said contact tank by a vertical wall (8), characterised in that said contact tank (3) is arranged along said flotation tank (6) and defines a separate contact zone where said water to be treated comes into contact with said white water; and the water delivery device (4) to be treated is designed to distribute the water to be treated into the contact tank according to a longitudinal water delivery flow, the water distribution flow (A) in the flotation tank being perpendicular to the longitudinal water delivery flow (B) in the contact tank.

2. The flotation water treatment plant according to claim 1, wherein the height (H) of the flotation tank is between 1 and 4 meters, preferably between 1 and 2.5 meters; and the width (L) of the tank is between 0.5 and 4 meters.

3. The flotation process water treatment plant according to claim 1 or 2, characterized in that the white water conveying means conveying white water into the contact tank has a multiphase pump connected to nozzles adapted to generate bubbles of very small diameter.

4. The flotation water treatment apparatus according to claim 3, wherein the white water conveying means that conveys white water into the contact tank has a multiphase pump and a static mixer connected to nozzles adapted to generate bubbles of very small diameter.

5. The flotation water treatment plant according to claim 3 or 4, wherein the nozzles are arranged at a height (h) of between 0.2 and 2 meters from the bottom of the contact tank.

6. The flotation process water treatment plant according to claim 5, wherein the nozzles are arranged with a nozzle density of between 3 and 30 nozzles per square meter of tank bottom of the contact, preferably between 5 and 12 nozzles.

7. The flotation process water treatment plant according to any one of the preceding claims, characterized in that the combination consists of a combination of 2 to 24, preferably 2 to 12 modules.

8. The flotation water treatment plant according to any one of the preceding claims, characterized in that the total Length (LT) of the flotation water treatment plant is between 0.5 and 20 meters, preferably between 1 and 12 meters.

9. The flotation water treatment apparatus according to any one of the preceding claims, wherein the water to be treated conveying device that conveys the water to be treated into the contact tank has an open-pored pipe, the open-pored pipe of the water to be treated conveying device being arranged longitudinally in a lower portion of the contact tank.

10. The flotation water treatment apparatus according to any one of the preceding claims, wherein the treated water discharge device has at least one open-pored conduit, the open-pored conduit of the treated water discharge device being arranged longitudinally in the lower part of the flotation tank.

11. The flotation water treatment plant according to any one of the preceding claims, wherein the floated sludge discharge device has a scraper equipped with a moving device for moving the scraper along a longitudinal axis transverse to the water distribution flow (a) in the flotation tank.

12. The flotation process water treatment plant according to any one of the preceding claims, characterized in that the ratio of the height (H) of the flotation tank to its width (L) is greater than 1.1.

Technical Field

The field of the invention is that of water treatment, making it water-purifying or potable.

In particular, the invention relates to a flotation process water treatment plant.

Background

The contaminated liquid or water may contain suspended matter (particulates, algae, bacteria, etc.) and dissolved matter (organics, micro-contaminants, etc.). There are various techniques in the prior art for treating suspended matter with the aim of reducing its content.

Among these techniques, a precipitation method and a flotation method are cited.

Flotation water treatment has many advantages over precipitation.

The first advantage is that the flotation process water treatment rate is higher than the usual precipitation process treatment rate.

Another advantage is that flotation processes remove algae and grease better than sedimentation processes for high flow rates of process water.

In addition, another advantage of the flotation process is that the amount of slurry produced can be reduced.

In the flotation process, a distinction should be made between:

natural flotation, in which the difference in weight per volume between the suspended matter and the water containing it is generally sufficient to cause it to separate (the matter floats on the surface of the water);

the auxiliary flotation, which is characterized in that bubbles are blown into the whole liquid to accelerate the separation of particles, so that the particles can be floated;

flotation is produced in which the weight per volume of the suspended matter is initially greater than the weight per volume of the water containing said suspended matter and is then artificially reduced by means of air bubbles. Indeed, some solid or liquid particles may be incorporated into the bubbles, forming "particle-bubble" links lighter than the water containing them;

dissolved air Flotation (FAD) is a resulting flotation process that uses bubbles of very small diameter, in practice, 40 to 70 microns in diameter. It generally comprises a sequence of different steps: coagulation to neutralize the debris material carried on the surface of the colloid and adsorb the dissolved material; flocculation by means of a flocculating polymeric material in contact with small bubbles and flocculated water; separating, separating the flocs from the clarified liquor; collecting the clear liquid; the floated sludge is collected.

The dissolved air flotation technology is generally applied to high-quality water, cold water with a small amount of suspended matter, and particularly water rich in algae, in a range where water is drinkable. Therefore, the dissolved air flotation is applied to the treatment of urban or industrial wastewater to purify the wastewater.

WO2008142026 therefore proposes a flotation plant having a contact tank which brings the water to be treated into contact with small bubbles, a lower contact tank area separated from the contact tank by an apertured plate which receives small bubble injection nozzles, and a flotation tank separated from the contact tank by a wall which is crossed in its upper part by a mixture of water and small bubbles.

According to the apparatus, the contact tank is arranged at one end of the flotation tank, which has the drawback that inside the contact tank, the small bubbles are not uniformly distributed, but instead have a gradient. In practice, the area of the tank near the contact tank has more bubbles than the area of the tank far from the contact tank. This gradient causes the water arriving in the device to be treated unevenly. One part of the water receives more bubbles than the other part and is thus better treated.

Another drawback is that the design and dimensions of the apparatus make it difficult to transport, especially in containers. However, there is an increasing demand in the market for water treatment plants, in particular flotation plants, which are easy to transport, in particular container transport, which can be loaded on container ships to use sites remote from the manufacturing site. This occurs, for example, when these devices are used at natural disaster sites where water treatment facilities are damaged or destroyed, or when rented for occasional demand.

Another drawback is therefore that such a device is not of a standard type. However, there is an increasing demand on the market for water treatment plants, in particular flotation plants, which have standardized characteristics, can offer different treatment capacities, eliminating the use of bulky plants which increase the treatment costs.

To this end, it should be noted that the applicant has already proposed flotation plants of the standard type, which are described in italian patent applications ITTO20080399a1, ITTO20080401a1 and ITTO20080402a 1. The apparatus is formed by a combination of modules each having a U-shaped cross-section with sidewalls having a recessed portion defining a contact area with the water to be treated, the flocculent and the white water. Each module therefore has a recess in one of its walls, in which the water to be treated and the white water come into contact. These devices are modular in that they can be provided in larger or smaller capacities depending on the number of components used.

However, depending on their size (volume), these devices also do not allow standardized container transport by sea.

In addition, each module is provided with a dedicated contact area, in fact a recessed portion, which complicates the manufacture of the module and affects the overall cost of such a flotation plant.

Finally, with such plants, the production of white water must be regulated before start-up, which in practice results in limiting the passage rate of the water to be treated, limiting its production capacity.

Object of the Invention

The invention aims to propose a standardized flotation plant which is simple to implement.

The invention also aims to propose a device that is compact and that allows standardized container shipping.

Disclosure of Invention

All or part of these objects are achieved by means of the apparatus of the invention, which relates to a flotation process water treatment apparatus having a generally parallelepiped-shaped combination formed by the union of modules, said combination having a contact tank with a treated water conveying means and a white water conveying means, a flotation tank with a treated water discharging means, and a floated slurry discharging means, said flotation tank being separated from said contact tank by a vertical wall, characterized in that said contact tank is arranged along said flotation tank and defines a separate contact area where said water to be treated contacts said white water; and the water to be treated delivery device is designed to distribute the water to be treated into the contact tank according to a longitudinal water delivery flow, the water distribution flow in the flotation tank being perpendicular to the longitudinal water delivery flow in the contact tank.

The invention therefore proposes that the contact tank is no longer arranged at the end of the flotation tank, as in the prior art of WO2008056057, but along the flotation tank. At the same time, the invention also establishes that the contact tank defines a contact area common to all modules, thus solving the problem of complex technical implementation of the ITTO20080399a1, ITTO20080401a1 and ITTO20080402a 1.

Depending on the number of modules used, the standardization may allow the plant to have a greater or lesser capacity.

According to the invention, the flow of water to be treated fed into the contact tank is perpendicular to the flow of water in the flotation tank. In general, for a good distribution of the hydraulic mass flow in the flotation plant, it is established, under the operation of the skilled person, that the water to be treated is injected in parallel with the distribution of the water in the flotation tank.

The dimensions of the modules are selected to make the apparatus of the invention of a volume suitable for standardized container shipping.

Preferably, the modules are designed so that the resulting plant has a flotation tank with a height H of 1 to 4 meters and a width L of 0.5 to 4 meters. It should be noted that by height H is meant the distance between the point at which water is collected at the bottom of the flotation tank and the point at which the floated water is collected. The width L of the flotation tank is the distance between the vertical separating wall of the contact tank and the flotation tank and the opposite wall.

Advantageously, said white water conveying means, which convey the white water into the contact tank, have a multiphase pump connected to nozzles adapted to generate bubbles of very small diameter, in practice having a diameter of 40 to 70 microns.

Using such nozzles, the apparatus of the invention can be operated at a higher mirror speed of water in the flotation apparatus, in practice about 25 m/h, which is generally limited to 10 m/h for similar water qualities using prior art flotation apparatus.

Advantageously, the white water conveying device, which conveys the white water into the contact tank, has a multiphase pump and a static mixer, which are connected to nozzles adapted to generate bubbles of very small diameter.

According to a preferred embodiment, the nozzles are arranged at a height h of between 0.2 and 2 meters from the bottom of the contact tank.

Preferably, the nozzles are arranged such that the nozzle density is between 3 and 30 nozzles, preferably between 5 and 12 nozzles, per square metre of bottom of the contacting tank.

According to one embodiment, the assembly consists of a combination of 2 to 24, preferably 2 to 12 modules.

As mentioned above, the volume of the apparatus of the present invention allows standardized container shipping.

Therefore, the total length LT of the flotation process water treatment plant according to the invention is preferably between 0.5 and 20 meters, preferably between 1 and 12 meters.

Preferably, the water-to-be-treated delivery device that delivers the water to be treated into the contact tank has an apertured pipe, the apertured pipe of the water-to-be-treated delivery device being arranged longitudinally in a lower portion of the contact tank.

Advantageously, the treated water discharge has at least one open-pored duct, the open-pored duct of the treated water discharge being arranged longitudinally in the lower part of the flotation tank.

Preferably, the floated sludge discharge device has a scraper equipped with a moving device for moving the scraper transversely to the distributed flow of water in the flotation tank along the longitudinal axis.

Preferably, the ratio of the height H of the tank to its width L is greater than 1.1.

Drawings

An embodiment of the flotation plant according to the invention will now be described in detail, given by way of example only, with reference to the accompanying drawings, in which:

FIG. 1 is a perspective view of one embodiment of the present invention;

FIG. 2 is a partial perspective view of this embodiment;

FIG. 3 is a cross-sectional view of the apparatus illustrating a horizontal cross-section P-P' of the water flow in the tank thereof;

FIG. 4 is a perspective view of one of the modules comprising the contact tank and flotation tank combination of the apparatus;

FIG. 5 is a schematic top view of the contact tank and flotation tank arrangement of the apparatus;

FIG. 6 is a side sectional view of the contact tank and flotation tank arrangement of the apparatus;

figure 7 is a diagram showing the reduction of suspended matter of the effluent by means of a flotation plant of the prior art of WO 2008142026;

figure 8 is a graph showing the content of suspended matter of the same effluent at the inlet and outlet of the flotation plant of the invention;

fig. 9 is a top view photograph of the contact tank of the apparatus of the present invention shown in fig. 1 to 6 in an inspection process to complete the chart shown in fig. 8.

Detailed Description

As shown in fig. 1 to 6, the apparatus has a tank assembly 1, which has a parallelepiped shape, and is arranged on a base frame 1 a. In addition to the combination 1, the bottom frame 1a also receives a white water producing device 10.

The tank assembly is formed by the union of two modules 2 as shown in figure 4. It should be noted that in other embodiments, it is apparent that the combination may be implemented using more than two modules.

These modules 2 are connected to each other and to the end walls 2a and 2b, forming a combined body 1 of a technique known to the person skilled in the art, thus forming a contact tank 3 and a flotation tank 6.

The contact tank 3 has a water-to-be-treated conveying device 4 and a white water conveying device 5.

The water-to-be-treated delivery means 4 has an open-pored pipe arranged in the lower part of the contact tank 3, longitudinally thereto.

The white water conveyance device 5 has a conveyance pipe provided with a nozzle 5a (see fig. 6) that can generate bubbles having a very small diameter, and is connected to a multiphase pump (not shown).

The pipe is arranged parallel to the water delivery device 4 to be treated, above it. Thus, as shown in fig. 6, these nozzles are arranged in the contact tank at a height h of between 0.2 and 2 meters from its bottom 3 a. The density of nozzles on the pipe is arranged to optimise the flotation process in the flotation tank, and in practice it is preferred to have between 3 and 30 nozzles per square metre at the bottom of the contact tank.

In addition, the flotation tank 6 has a treated water discharge device with two pipes 7, 7a arranged in its lower part. The flotation tank 6 is separated from the contact tank by a vertical wall 8.

In addition, the tank is equipped with a drained floated sludge discharge device with weirs 9 and scrapers 11 (as shown in figure 5).

According to the invention, the contact tank 3 is arranged along the flotation tank 6, defining a separate contact area for contacting the water to be treated with the white water.

According to the invention, the water transport device 4 to be treated is designed, as shown in fig. 3, such that the water to be treated is transported into the contact tank 3 in a longitudinal water transport flow, the water distribution flow a in the flotation tank 3 being perpendicular to the longitudinal water transport flow B in the contact tank 6.

In operation, water to be treated is conveyed through conduit 4 into the individual flotation zones defined by flotation tank 3, where it is contacted with white water supplied through conduit 5 having nozzles.

The very small bubbles distributed by these nozzles are immediately mixed with the water to be treated, which mixture passes from the overflow conduit through the wall 8 into the flotation tank 6. In this tank 8, the substances separated from the water are floated by the action of the bubbles, which mix with these substances, reducing their density and thus causing them to float.

Periodically, the material floating on the water in the flotation tank and in the contact tank is pushed towards the discharge opening 9 using the scraper 11 and discharged from the apparatus for final treatment. For this purpose, the scraper has a displacement axis l1a, which is perpendicular to the flow a of water in the flotation tank 6.

It should therefore be noted that the scraper 11 is designed to scrape the flotation tank 6 and to contact the water surface in the tank B. Of course, the discharge opening 9 extends transversely to the two tanks for receiving flotation substance.

The treated water is recovered in the lower part of the tank by pipes 7 and 7 a.

Comparative test

The flotation plant of the invention described above and the flotation plant of the prior art of WO2008142026 are used for treating effluents constituted by water of the dairy industry.

In comparison, the apparatus of the present invention is more compact than prior art test apparatus. In fact, the apparatus of the present invention is 30% smaller than the prior art apparatus.

In addition, the apparatus of the present invention is standardized and transportable in containers, as opposed to prior art apparatus which is neither standardized nor transportable.

Different batches of said effluent have been treated by the plant of WO2008142026, for each batch the MES content of the suspensions is determined at the raw water inlet and the purified water outlet of the plant, and for each batch the reduction (%) of these suspensions is obtained.

During these tests, coagulant and flocculant were injected into the equipment.

In the test, the effluent was fed to the apparatus at a mirror image speed of 26 m/h.

As shown in fig. 7, the reduction rate of suspended matter was 85% to 98% as a function of the lot.

Different batches of the same effluent are then treated by means of an embodiment of the invention, as shown in figures 1 to 6.

As shown in fig. 8, the suspended matter content TSS of the inlet and outlet of the apparatus was determined for each batch. After these measurements, the reduction of suspended matter was calculated and compared completely with the reduction obtained with the device of WO 2008142026.

In the tests, the effluent was fed to the plant at a mirrored speed of 20 to 25 m/h as a function of batch, similar to the plants of the prior art.

These comparative tests show that the apparatus of the present invention can achieve a process performance equivalent to that of the prior art apparatus while having a size 30% smaller than that of the prior art apparatus.

This is because white water is well distributed in the contact tank by means of the invention. The photograph of fig. 9 shows the uniform white hue of the mixture of effluent and white water in the contact tank of the apparatus of fig. 1-6, and indeed, the present invention allows for even distribution of white water in the contact tank, thereby ensuring that the treated effluent is all in contact with the same amount of white water.