The present invention relates to an industrial station for separating granular materials, and in particular for classifying powders or similar materials with dynamic air separators.
The separation of materials into particle fractions with different sizes may be done by means of dynamic air separators. The concerned materials are powders with particle sizes of up to 1000 μm, such as cement, limestone or lime, ore and coal among others.
Dynamic separators have undergone several major evolutions allowing them to be classified in 3 major families. The first, generally known under the names “turbo”, “heyd” or “whirlwind”, was improved by a second called “Wedag” type. These separators may optionally have a cage instead of the selection blades.
Document EP2266715A1 (Hosokawa) discloses a separator where the material is not supplied and dispersed above, but below the cage or selection blades. Furthermore, the fan is not at the outlet of the purified air duct, but on the contrary it receives the air charged with material.
The latest generation of separators that has been developed is the most compact and highest performing in terms of separation efficiency. The operating principle of this type of separator is in particular described in documents U.S. Pat. No. 4,551,241 and EP 0023320 A1.
Document DE 19743491 (Schmidt) discloses three types of separators, focusing on the cage thereof. It discloses a so-called first-generation separator (Kompaktsichter), a so-called second-generation separator (Zyklonumluftsichter) and a so-called third-generation separator (Querstromsichter). In these separators, the fan and the cyclone are outside the separator. No compactness of the installation is sought.
Document U.S. Pat. No. 4,551,241 discloses a particle separator provided with a lateral cyclone in which the fine particles are sent with the air toward cyclones to be recovered. The fine particles that have not been cycloned are sent back to the rotary cage of the separator. The whole installation turns out to be relatively bulky and to have a fairly complex design.
Document WO 2005/075115 describes a device for classifying granular materials with the particularity of having a chamber for cycloning the fine fraction in the extension of the axis of the rotary cage. This recovery chamber arranged coaxially to the rotary cage is part of the body of the separator. This type of air separator thereby does not require an outside cyclone or filter to separate the fine material from the separation air. The recovery chamber benefits from the air vortex created by the cage for the cycloning. The fan that sucks the air in at the outlet of the separator and discharges it toward the air intake volute of the separator is, however, positioned outside the installation, which creates a significant bulk. Furthermore, the air must be distributed through a volute still designed for a predetermined air flow rate. It therefore does not allow optimal operation when the air flow rate varies.
All of the types of separators of the state of the art operate according to the same principle as shown in
The present invention aims to disclose a dynamic air separator with a rotary cage making it possible to avoid the use of an outside fan. The fan is integrated into the body of the separator, which makes it possible to improve the air distribution on the perimeter and height of the cage, and thus to produce a homogenous air flow preventing the segregation of the particles in the dead areas.
The separator according to the present invention also aims to reduce the overall bulk of the installation and to make it possible to install a high-performance separator in tight spaces where it was not previously possible to do so.
The present invention discloses a dynamic air separator for separating materials made up of particles of different sizes into particle-size fractions, said separator comprising a rotary cage and a fine particle recovery chamber arranged coaxially in the extension of the rotary cage, characterized in that:
According to specific embodiments, the invention comprises at least one or a suitable combination of the following features:
The principle of separating the particles in the installation according to the invention is diagrammed in
The separator according to the invention comprises a fine particle recovery chamber 2 adjacent and arranged coaxially in the extension of the rotary cage 1, said recovery chamber 2 being provided at one of its ends with a coaxial outlet duct 4 for the purified air, said duct comprising at its end a fan wheel 3. Said fan wheel 3 is positioned coaxially to the rotary cage 1 and the fine particle recovery chamber 2.
The fan wheel 3 is driven by a motor, the speed of which will be adapted to the pressure loss in the separator.
Between the recirculation enclosure of the fan 6 and the air distribution chamber 5 at the inlet of the separator, multiple ducts 7 (see
Due to the uniform distribution of the air recirculation ducts 7 on the perimeter of the air distribution chamber 5, the recirculation air is uniformly distributed around the cage 1 of the separator. As a result, the cutoff size (separating point of the particle sizes) of the separator is constant over the entire circumference of the separator cage.
One particular embodiment of the invention consists of replacing the multiple ducts 7 with a single outer ferrule 19 made up of a surface of revolution—of a generally cylindrical or conical design—the diameter of which is comprised between the diameter of the enclosure of the fan 6 and the outside diameter of the air distribution chamber 5 around the cage. In that case, it is preferable to install, in the transition area between the enclosure of the fan 6 and the ferrule 19, deflectors 8 making it possible to convert the tangential speed of the air at the outlet of the fan wheel 3 into a vertical speed. Likewise, it may be useful to install deflectors 9 at the junction between the ferrule 19 and the air distribution chamber 5 so as to impart the desired direction to the air in the air distribution chamber 5. As a result, it is also possible to influence the distribution of the air over the height of the air distribution chamber and the height of the cage. This therefore makes it possible to obtain a constant cutoff size over the entire height of the cage, which is very difficult to obtain with a traditional volute.
In the embodiment of the invention where the fan wheel 3 is located above the cage 1, recirculation through the ferrule 19 will be preferred. Said ferrule will have the form of a surface of revolution centered on the axis of the separator and will connect the enclosure of the fan 6 to the air distribution chamber 5. In that same case, the size of the ferrule 19 could be much smaller if the enclosure of the fan 6 and the air distribution chamber 5 are positioned near one another.
Number | Date | Country | Kind |
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2011/0547 | Sep 2011 | BE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2012/067825 | 9/12/2012 | WO | 00 | 6/2/2014 |
Publishing Document | Publishing Date | Country | Kind |
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WO2013/037820 | 3/21/2013 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
4551241 | Saverse et al. | Nov 1985 | A |
20070163925 | Prignon | Jul 2007 | A1 |
Number | Date | Country |
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19743491 | Apr 1998 | DE |
0023320 | Feb 1981 | EP |
2266715 | Dec 2010 | EP |
1221754 | Feb 1971 | GB |
WO 2005075115 | Aug 2005 | WO |
Entry |
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Machine translation of Konetzka et al., DE 102009030396 A1, retrieved Mar. 22, 2015. |
Number | Date | Country | |
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20140251878 A1 | Sep 2014 | US |