The present invention relates to the technical field of devices for water treatment. More particularly, the present invention relates to a flotation cell for water treatment by gas injection on a laboratory scale.
Field water treatment equipment such as Wemco flotation cells are well known in the state of the art. To optimize the performance of these flotation cells it is important to carry out laboratory scale studies in order to know the effect of different parameters on the water treatment.
A well-known device in the state of the art is the IFPEN flotation cell, which is used to study the impact of different parameters in water treatment requested by different customers in the industry but, since it is an open cell, it does not allow studies to be carried out when foam is generated. This is because, depending on whether the system components have natural or added surfactants, when air enters, the formation of foams and their ascent through the column can be very fast having to suspend, or directly discard in its totality, the tests. This is due to the fact that part of the fluids, which are being studied, are lost through the overflow that occurs at the top of this flotation cell, since it does not have a lid and does not allow controlling the level of foam that is generated.
It should be noted that the formation of foam is difficult to control if there is sufficient surfactant and a certain pressure difference to favor gas migration out of the liquid.
Consequently, there is a need to provide a device that allows to study the different parameters that affect water treatment independently of the generation or not of foam during a test.
Based on the above considerations, the present invention provides a flotation cell that allows studying the effect of different parameters in water treatment and that tolerates the generation of foam in the cell without affecting the performance of different tests.
Accordingly, it is an object of the present invention a flotation cell for water treatment comprising:
In an embodiment of the present invention, the plurality of conduits of the body is located above a middle part of the body.
In an embodiment of the present invention, the plurality of conduits of the body comprises four conduits located at a same height of the cylindrical body and spaced 90° apart from each other in relation to a central longitudinal axis of the cylindrical body.
In a preferred embodiment of the present invention, the plurality of conduits of the body comprises eight conduits, wherein four conduits of the eight conduits are located at a first height of the cylindrical body, spaced 90° apart from each other in relation to the central longitudinal axis of the cylindrical body; and wherein the remaining four conduits of the eight conduits are located at a second height of the cylindrical body, above the first height, spaced 90° apart from each other in relation to the central longitudinal axis of the cylindrical body.
In an embodiment of the present invention, the body comprises an additional conduit for placing measuring instruments, preferably, the additional conduit comprises an elongated body for placing a temperature sensor.
In an embodiment of the present invention, a temperature sensor adapter is placed in at least one of the conduits of the cylindrical body.
In an embodiment of the present invention, the cylindrical body comprises, in a lower part thereof, interchangeable porous plates that are supported by the lower lid.
In an embodiment of the present invention, the band heater is located below the middle part of the cylindrical body.
In an embodiment of the present invention, the control unit is a control panel.
The flotation cell of the present invention will be described in detail below with reference to
In each of the figures the same reference numbers are used to refer to similar or the same elements of the device of the present invention.
Referring to
The cylindrical body 2 is hollow and comprises upper and lower openings at its vertically opposite ends which are covered, respectively, by the upper lid 3 and the lower lid 4. Additionally, the cylindrical body 2 comprises a plurality of conduits 8 projecting from, and arranged on, the outer surface of the cylindrical body 2. These conduits 8 are located above a middle part of said body 2.
In particular, for the embodiment shown in
In this embodiment, since the conduits 8 are located at two different heights, the flotation cell 1 of the present invention allows working with two working test volumes, for example, with 4 liters and 5 liters, wherein one or the other volume is operated depending on the total amount of sample to be tested available. The function of said conduits 8 is to evacuate the supernatant obtained from the cleaning by gas bubble-carrying. In addition, the conduits 8 can be connected to hoses to collect the fluid for analysis. Thus, depending on the test, the conduits 8 can be used to dose products (e.g. flocculants, coagulants, clarifying agents, demulsifiers, etc.) or to take samples from another level.
It should be noted that, although eight conduits 8 are shown, the cylindrical body 2 may comprise a different number of conduits 8 as required. For example, the cylindrical body 2 may comprise only four conduits 8 located at the same height of the cylindrical body 2 and spaced 90° apart in relation to the central longitudinal axis of the cylindrical body 2. In the latter case, only one of the two working volumes would be used.
The cylindrical body 2 comprises, preferably, a total inner volume of 7 liters of which 4 or 5 liters are used with liquid fluid and the remaining volume is used as a containment chamber for gas and possible formation of foams (depending on the fluids to be tested).
When the flotation cell 1 is operating at the minimum test volume, for example, the volume of 4 liters, the upper conduits 8 are closed so as to allow more height of the column which allows a foam thickness controlled by pressure regulation through the upper lid 3.
On the other hand, if operating at the maximum volume of, for example, 5 liters, one of the four lower conduits 8 can be used to take samples, for example, from the conduit closest to the supernatant. In addition, in at least one of said conduits 8 a temperature sensor adapter can be placed so as to sample at points close to the gas injection.
As is evident said inner volume is easily modifiable by scaling the dimensions of the flotation cell of the present invention. Thus, in case it is required to work with large or small volumes, the dimensions of the flotation cell and, consequently, of the cylindrical body, will be larger or smaller, respectively. Moreover, the position of the conduits 8 on the outer surface of the cylindrical body 2 could be modified. Thus, taking into consideration either of these two characteristics, the working volumes would be different from, for example, 4 liters and 5 liters.
As described above, the body 2 comprises upper and lower openings which are covered, respectively, by the upper lid 3 and lower lid 4, wherein the upper lid 3 comprises a conduit 10 and the lower lid 4 comprises a conduit 9.
The conduit 9 is used to inject gas (during the test) and, depending on the suspended solids content of the sample to be tested, fluids can be evacuated through this conduit.
The conduit 10 is used to load the sample to be tested (before the test) and to regulate the pressure (during the test), if necessary, in order to control a possible generation of foams inside the body 2. More precisely, the conduit 10 allows the entry of the water to be studied into the body 2, wherein said water to be studied will comprise hydrocarbons and suspended solids as is evident to an expert in the corresponding technical field.
The cylindrical body 2 is made of transparent material, preferably borosilicate glass 3.3. The cylindrical body 2 allows operation up to 200° C. and withstands slight overpressures up to 10 psi.
The control unit 6 is a control or command panel by means of which temperature regulation is enabled within the cylindrical body 2. More precisely, the panel serves to regulate temperature by means of the band heater 5.
The support structure 7 supports above the ground the cylindrical body 2 in a vertical position together with the upper lid 3 and the lower lid 4. For this purpose, the support structure 7 comprises a plurality of vertical and horizontal bars, wherein the control unit 6 is attached to one of the vertical bars, as seen in
The flotation cell 1 of the present invention allows studying the effect of most of the parameters influencing water treatment by gas injection. These influencing parameters are bubble size distribution, gas flow rate, gas composition, temperature, salinity, pH and concentration of suspended solids of different nature.
The flotation cell 1 of the present invention allows gas to be injected or bubbled into the body 2 to facilitate the flotation of hydrocarbons and suspended solids. As described above, the gas is injected through conduit 9 of the lower lid 4, which supports interchangeable porous plates (not shown) of different pore size distribution and/or material according to the desired bubble size to be dispersed in the fluid under study.
The flotation cell of the present invention has the versatility of being able to carry out tests under different conditions. Some of these conditions are that it can generate three types of gas bubble distribution when passing through the porous plates that disperse the injected gas. Depending on the test, the bubbles can be generated with different flow rates of injected gas or air.
The porous plates are preferably made of sintered glass or polytetrafluoroethylene (Teflon), and allow three bubble size distributions to be obtained, these being small, medium and large, ranging from the order of microns to the order of millimeters as required.
In case of having to work with the formation of foams when carrying out a test, such formation of foams can be attenuated by closing the conduits 8 while injecting gas, keeping the upper lid 3 slightly open.
Since in the field gas mixtures (natural gas) are injected which favor the cleaning process due to the interaction between the type of gas (bubbles) with the fluid (water and hydrocarbons with suspended solids of different nature and composition), in the flotation cell of the present invention different gas compositions can be injected through the conduit 9 or just compressed air so as to obtain conditions similar to those in the field. Finally, the flotation cell of the present invention allows working at different pressures and different temperatures. In this way, it is possible to adapt the phenomena studied to conditions as similar as possible to real field conditions and to be able to evaluate the effect of the different parameters in water treatment.
It should be noted that the aim during the tests is to obtain a constant gas flow in order to generate a turbulent regime, but with adequate distribution of bubbles. In other words, the aim is to obtain a turbulent regime where the bubbles carry the oil droplets and suspended solids to the surface.
The cylindrical body 2 of the flotation cell 1 of the present invention further comprises an additional conduit 11 for the placement of measuring instruments, preferably, for the placement of a temperature sensor. Said measuring instruments may be wired to the control unit 6, so that the latter, as described above, can control the temperature and represent it graphically for its display by an operator.
By means of the control unit 6, the band heater 5 can be controlled to heat more or to heat less as required. Said band heater 5 is located below the middle part of the cylindrical body 2 and surrounding the entire outer surface of said cylindrical body 2 so as to achieve a homogeneous heating of the fluid under study. In an embodiment, the band heater 5 allows heating the fluid under study up to 40° C. and can be connected to the control unit 6. In this way, the temperature generated by the band heater through its heating elements can be regulated.
In an embodiment, the flotation cell comprises at least one chamber for monitoring the interior of the cylindrical body and controlling the test dynamically.
Referring to
Referring to
Replacing the nut 13 and spigot 14 with a blind cap cancels out any conduits deemed necessary. Referring to
In this way, the flotation cell of the present invention allows the possibility of partially closing it since the conduits 8 may comprise blind caps and/or interchangeable spigots according to the design of the test to be carried out whereby the pressure difference and the formation of foam can be controlled.
Referring to
Finally, referring to
The upper lid 3 is attached to the body 2 by means of two flanges 16, which are joined together by studs and nuts (not shown) and which sit on inserts 17 which are preferably made of a thermosetting plastic material. Finally, the tight seal between the upper lid 3 and the cylindrical body 2 is achieved by means of the gasket 18 which is preferably a double o-ring gasket.
As is evident, the lower lid 4 and the body 2 are joined in the same way as the upper lid 3 with said body 2.
Number | Date | Country | |
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63297023 | Jan 2022 | US |