DAL BEN, Antonio (Via S. Menna 2, San Biagio Di Callalta, I-31048, IT)
CLAIMS
1. Centrifugal machine for separating impurities from masses of incoherent materials, comprising a container (13) defining a separation chamber (14) inside which a mixture of impurities and masses of incoherent materials is able to be introduced, and first ventilation means (18), able to generate a flow of air so as to make said mixture rotate inside said separation chamber (14), characterized in that it comprises rotor means (21) associated with said separation chamber (14), able to promote the rotation of said mixture inside the separation chamber (14), and at least second ventilation means (23) able to generate a flow of air directed in a direction substantially opposite the fall direction of said masses of incoherent material, so as to keep said masses of incoherent materials in suspension inside the separation chamber (14) in order to subject them to subsequent passes and discharge steps from said separation chamber (14) and/or separation steps inside said separation chamber (14). 2. Centrifugal machine as in claim 1, characterized in that said container comprises a snail-shaped casing (13).
3. Centrifugal machine as in claim 1 or 2, characterized in that it comprises an outlet pipe (22), associated with said container (13), to discharge the masses of incoherent material, whose position along said container (13) is adjustable. 4. Centrifugal machine as in any claim hereinbefore, characterized in that it also comprises first separation means (20) disposed in correspondence with the inlet to said separation chamber (14).
5. Centrifugal machine as in claim 4, characterized in that it comprises second separation means (25) disposed in correspondence with the bottom of the separation chamber (14), able to separate impurities from incoherent materials that fall onto the bottom of said separation chamber (14).
6. Centrifugal machine as in any claim hereinbefore, characterized in that the flow rate and pressure of said second ventilation means (23) are able to be varied according to the flow rate and pressure of said first ventilation means (18), and vice versa.
7. Method for separating impurities from masses of incoherent materials by means of a centrifugal machine (10) comprising a container (13) defining a separation chamber (14) inside which a mixture of impurities and masses of incoherent materials is able to be introduced, and first ventilation means (18), able to generate a flow of air so as to make said mixture rotate inside said separation chamber (14), characterized in that it comprises at least a step in which a rotor means (21) associated with said separation chamber (14) promotes the rotation of said mixture inside the separation chamber (14), and at least a second ventilation means (23) generates a flow of air directed in a direction substantially opposite the fall direction of said masses of incoherent material, so as to keep said masses of incoherent materials in suspension inside the separation chamber (14) in order to subject them to subsequent separation passes and steps. |
"CENTRIFUGAL MACHINE FOR SEPARATING IMPURITES FROM MASSES OF INCOHERENT MATERIALS AND RELATIVE METHOD"
FIELD OF THE INVENTION The present invention concerns a centrifugal machine for separating impurities from masses of incoherent materials and the relative method.
In particular, the centrifugal machine according to the present invention is preferably but not only used to separate pollutant particles, for example sand or silica derivates, from powdered wood material to be sent to subsequent working steps.
BACKGROUND OF THE INVENTION
In the state of the art it is known to use centrifugal machines to separate pollutant particles, for example sand or silica derivates, from powdered wood material arriving from previous working steps. Such machines comprise a separation chamber, substantially circular, inside which the mixture of powdered wood material and pollutant particles is introduced through an inlet pipe. The machines also comprise that a ventilation unit generates a flow of air that hits said mixture, making it rotate inside the separation chamber. In said chamber, due to the effect of the centrifugal force, the heavier particles of the mixture, such as sand or silica derivates, hit against the internal walls of the chamber and fall onto the bottom of it; the powdered wood material, which is lighter, is held in suspension by the flow of air and continues its travel along the walls of the circular chamber until it reaches an outlet pipe through which the powder, thus filtered, is expelled from the machine. This is then sent to subsequent working steps, for example toward a drier to eliminate the residual humidity of the powder.
One disadvantage of centrifugal machines like these is that they have a limited filtering power, caused by the fact that the filtering operation is performed on the mixture introduced substantially during a single pass in front of the outlet pipe. Therefore, a considerable quantity of pollutant particles comes out of the outlet pipe with the powdered wood material, and furthermore, powdered wood material remains inside the separation chamber. This causes a low productive efficiency of the machine and the risk of damage to the apparatuses used in the
subsequent working steps of the powdered wood. For example, the unfiltered pollutant particles that are introduced inside driers can vitrify, thus compromising the efficiency of the driers themselves.
It is also known to use a vibration device, such as a hydrometric table, to separate pollutant particles from powdered wood material. In this machine, a vibratory movement imparted to a separation plane on which said mixture is disposed and a depression created by a suction system associated with the machine determine a separation of the pollutant particles according to their specific weight. For this machine too, one disadvantage is the limited filtering power and the consequent limited productive efficiency.
Purpose of the present invention is therefore to achieve a centrifugal machine which increases the capacity of separating pollutant particles, consequently increasing its productive efficiency and drastically reducing the risk of damage to the apparatuses used in the subsequent working steps.
The Applicant has devised, tested and embodied the present invention to overcome the shortcomings of the state of the art and to obtain these and other purposes and advantages.
SUMMARY OF THE INVENTION The present invention is set forth and characterized in the independent claims, while the dependent claims describe other characteristics of the invention or variants to the main inventive idea.
In accordance with said purpose, a centrifugal machine according to the present invention is used to separate impurities from masses of incoherent materials, such as for example powdered wood material. The centrifugal machine comprises a container defining a separation chamber, inside which a mixture of impurities and masses of incoherent materials is able to be introduced, and first ventilation means, able to generate a flow of air to make said mixture rotate inside the separation chamber. According to a characteristic feature of the present invention, the centrifugal machine comprises rotor means associated with the separation chamber, able to promote the rotation of the mixture inside the separation chamber, and at least second ventilation means able to generate a flow of air directed in the opposite
direction to the fall direction of said masses of incoherent material, in order to keep said masses of incoherent material in suspension inside the separation chamber in order to subject them to subsequent and numerous discharge passes from said separation chamber and/or to subsequent separation passes inside the separation chamber.
In this way, together with the centrifugal separation that is determined due to the effect of the flow of air generated by the first fan, the use of the rotor means further increases the centrifugal separation capacity of the machine. Furthermore, the rotor means promotes the recirculation of the masses of incoherent material which are not expelled from the separation chamber, thus allowing to subject them to further separation steps and passes inside the separation chamber.
The flow generated by the second ventilation means also allows to keep in suspension the masses of incoherent materials remaining inside the separation chamber, which tend to fall toward the bottom of the separation chamber so that they can be hit by the flow of air generated by the first ventilation means and be expelled from the machine or subjected to further separation steps inside the separation chamber.
According to an advantageous feature of the present invention, the machine comprises an outlet pipe associated with said container, the position of which along the external wall of the container is adjustable.
This allows to determine the position of the outlet pipe which gives the best compromise between separation capacity of the impurities and discharge of clean incoherent material.
According to a variant of the present invention the centrifugal machine comprises first separation means able to achieve a first separation of the impurities from the masses of incoherent material.
Advantageously, said first separation means is disposed in correspondence with the inlet to the separation chamber.
According to another variant of the present invention the centrifugal machine comprises second separation means, disposed in correspondence with the bottom of the separation chamber, able to separate the impurities from the masses of incoherent materials which fall onto the bottom of the separation chamber.
These features listed above therefore allow to increase the overall separation
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capacity of the centrifugal machine, improving its productive efficiency and drastically reducing the risk of damage to the apparatuses used in the subsequent working steps, due to the almost total lack of impurities in the masses of incoherent materials that exit from the machine. BRIEF DESCRIPTION OF THE DRAWINGS
These and other characteristics of the present invention will become apparent from the following description of a preferential form of embodiment, given as a non-restrictive example with reference to the attached drawings wherein:
- fig. 1 is a three-dimensional view of a centrifugal machine according to the present invention;
- fig. 2 is a schematic lateral view in section of fig. 1.
DETAILED DESCRIPTION OF A PREFERENTIAL FORM OF
EMBODIMENT With reference to the attached drawings, a centrifugal machine 10 according to the present invention is used preferably but not only to separate pollutant particles, for example sand or silica derivates, from powdered wood material, consisting of particles with a diameter comprised between about 0.3 mm and 0.6 mm and arriving, for example, from a sifting machine, and to be sent to subsequent working steps. The centrifugal machine 10 according to the present invention comprises a supporting frame 11, made by means of metal profiles 12, able to support a snail- shaped casing 13, defining a substantially circular separation chamber 14, and a hopper 15 able to feed the separation chamber 14 with powdered wood material to be filtered. The mixture of powdered wood material and pollutant particles is introduced inside the separation chamber 14 through a feed pipe 16 associated, at a first end 16a, to the bottom of the hopper and, at a second end 16b, opposite said first end 16a, to the snail-shaped casing 13, substantially in correspondence with a rectilinear pipe 17 with which said snail-shaped casing 13 is provided. The centrifugal machine 10 also comprises a first fan 18 associated with said rectilinear pipe 17 and disposed axially with respect to the latter. The first fan 18 is able to generate a flow of air inside the separation chamber 14 to hit the mixture of powdered wood material and pollutant particles introduced into the
separation chamber 14 and make it rotate inside the latter.
The centrifugal machine 10 also comprises a first sieve 19 disposed inside the rectilinear pipe 17, able to distribute uniformly the air generated by the first fan 18 over the whole section of the rectilinear pipe 17, before it reaches the separation chamber 14.
The centrifugal machine 10 also comprises a second sieve 20, disposed at inlet to the separation chamber 14, substantially in correspondence with the feed pipe 16 and having very fine mesh so as to generate a precise air front and to effect a first separation of the pollutant particles from the powdered wood material. A rotor 21 is disposed inside the separation chamber 14, in this case in correspondence with the upper part of the separation chamber 14, able to promote the circulation of the mixture inside the separation chamber 14 and thus increase the separation capacity due to the centrifugal effect.
The centrifugal machine 10 also comprises an outlet pipe 22 for the filtered powders, associated with the snail-shaped casing 13, whose position along the external wall of the snail-shaped casing 13 is adjustable.
The centrifugal machine 10 also comprises a second fan 23, disposed in correspondence with the base of the supporting frame 11, associated by means of a pipe 24 to the snail-shaped casing 13, in correspondence with the bottom of the separation chamber 14, where a net 25 with fine mesh is located, able to achieve a further separation of the pollutant particles and possible powdered wood material which does not emerge from the outlet pipe 22.
The second fan 23 is able to generate a flow of air inside the separation chamber 14 directed substantially upward, so as to keep in suspension inside the separation chamber 14 the powdered wood material which does not emerge from the outlet pipe 22 and which reaches the bottom of the separation chamber 14, but without interfering with the deposit of the pollutant particles on the bottom of the separation chamber 14 and their expulsion through a discharge pipe 26.
Both fans 18, 23 are also provided with adjustment valves, of a known type and not shown in the drawings, to adjust the pressure and flow rate of the respective air flows.
The centrifugal machine according to the present invention functions as follows.
The mixture of powdered wood material and pollutant particles is introduced inside the separation chamber 14 through the hopper 15 and the feed pipe 16.
The mixture introduced into the separation chamber 14 is hit by the flow of air arriving from the first fan 18 in correspondence with the second sieve 20, where a first separation is achieved of the powdered wood material from the pollutant particles, which are deposited on the bottom of the separation chamber 14 in correspondence with the discharge pipe 26. The speed of the air flow in correspondence with the second sieve 20 is such as to allow the displacement of the mixture in a horizontal direction toward the internal wall of the separation chamber 14, and is such that there is the time needed for the separation of part of the pollutant particles from the mixture. The flow of air generated by the first fan 18 then makes the mixture rotate inside the separation chamber 14. The mixture is therefore subjected to a filtering action due to the centrifugal effect, in which the pollutant particles, having a greater density than that of the powdered wood material, fall toward the bottom of the separation chamber 14, whereas the powdered wood material continues its circular motion along the internal walls of the separation chamber 14 thrust by the flow of air generated by the first fan 18. The rotation of the mixture inside the separation chamber is also promoted by the rotor 21 and this increases the filtering capacity, due to the centrifugal effect, of the machine 10. The filtered powdered wood material exits from the outlet pipe 22, whose position along the external wall of the snail-shaped casing 13 allows to achieve the best compromise between capacity to separate the impurities and discharge of clean incoherent material. Any powdered wood material that is not expelled through the outlet pipe 22 tends to fall toward the bottom of the separation chamber 14 together with the pollutant particles, in correspondence with the net 25. Here another separation is achieved of the pollutant particles and the residual powdered wood material. The latter, due to the effect of the flow of air generated by the second fan 23, is thrust upward, and held in suspension inside the separation chamber 14 where, due to the effect of the flow generated by the first fan 18, it is conveyed toward the outlet pipe 22 and/or subjected to another separation step inside the separation chamber 14.
The two fans 18, 23 are regulated in a dependent manner one with respect to the other by means of the adjustment valves of a known type and not shown in
the drawings. The pressures and flow rates of the two fans 18, 23 are therefore varied dependently, so as to guarantee the desired speed of separation according to the quantity of mixture introduced inside the separation chamber 14, preventing unwanted overpressures or depressions from being created inside it. It is clear that modifications and/or additions of parts may be made to the centrifugal machine as described heretofore, without departing from the field and scope of the present invention.
It is also clear that, although the present invention has been described with reference to some specific examples, a person of skill in the art shall certainly be able to achieve many other equivalent forms of centrifugal machine, having the characteristics as set forth in the claims and hence all coming within the field of protection defined thereby.
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