US3240335A - Classifier with gas flow distributor - Google Patents

Classifier with gas flow distributor Download PDF

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US3240335A
US3240335A US158509A US15850961A US3240335A US 3240335 A US3240335 A US 3240335A US 158509 A US158509 A US 158509A US 15850961 A US15850961 A US 15850961A US 3240335 A US3240335 A US 3240335A
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gas
stream
particles
gas flow
vanes
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Vandenhoeck Jean Paul
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General Electric Environmental Services Inc
Buell Engineering Co Inc
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Buell Engineering Co Inc
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Assigned to GENERAL ELECTRIC COMPANY, A CORP. OF NY. reassignment GENERAL ELECTRIC COMPANY, A CORP. OF NY. ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ENVIROTECH CORPORATION
Assigned to GENERAL ELECTRIC ENVIRONMENTAL SERVICES, INCORPORATED reassignment GENERAL ELECTRIC ENVIRONMENTAL SERVICES, INCORPORATED ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: GENERAL ELECTRIC COMPANY A NY CORP.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B07SEPARATING SOLIDS FROM SOLIDS; SORTING
    • B07BSEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
    • B07B7/00Selective separation of solid materials carried by, or dispersed in, gas currents
    • B07B7/08Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force

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  • classification of granular material using gravitational classifying techniques has been effected by conveying a gas entrained granular material downwardly in a stream. As the material flows downwardly, gas is withdrawn from the stream, carrying with it particles of a certain size through an exhaust duct. The remainder of the gas and granular material pass downwardly through The degree of classification is varied by varying the amount of gas withdrawn from the falling stream of gas entrained granular material and thereby the size of the heaviest particles carried away with the withdrawn gas.
  • the total downward forces acting upon any particular particle of material in the stream decrease at successively lower positions in the stream due to the braking effect on the downward movement of the particle by the gas that is withdrawn. If, then, the same exhaust force is applied to the stream at all points in its downward course, as is the case with systems of the prior art, the net forces acting upon any particular downwardly fiowing particle do not remain constant throughout the downward travel, and, therefore, the classification effected is not uniform.
  • This invention is directed toward providing a classifying system utilizing gravitational and or inertial classifying techniques in which the net forces acting upon any downwardly flowing particle of granular material are equal throughout the entire course of the particles downward flow. This is accomplished by varying the exhaust forces acting upon the particles during their downward flows in accordance with the decreasing downward forces acting upon the particles.
  • the varying exhaust forces are provided by a substantially vertical series of cascaded vanes positoned adjacent the downwardly flowing stream of material.
  • Each of the vanes forms a different angle with a vertical plane, the angles decreasing from top to bottom through the series of vanes.
  • adjacent vanes effectively form single exhaust ducts, and, because of the varying angular positions of the vanes, each duct provides a gas flow characteristic different from any other duct.
  • the flow resistances progressively increase at successively lower positions in the stream, thereby providing decreasing exhaust forces on a particular particle as it proceeds downwardly past the vanes to compensate for the decreasing downward force acting upon the particle.
  • the net force acting upon the particle remains substantially constant, and a uniform clasisfication is effected.
  • FIG. 1 is a sectional view of a typical classifying unit embodying the principles of the invention.
  • FIG. 2 is a view of a series of cascaded vanes shown in FIG. 1, together with vector diagrams of the forces acting upon a single particle of material at two different positions in front of the vanes.
  • a typical classifying unit 11 having an input line 12 into which a stream of 3,24%,335 Patented Mar. 15, 1966 gas entrained granular material is introduced, as shown by the arrows in the figure.
  • the gas entrained granular material flows downwardly through the input line 12 and into a classifying chamber 13.
  • the stream flows downwardly past a series of cascaded vanes 14a through 14] toward a coarse material outlet duct 15 provided at the lower portion of the classifying chamber 13.
  • a subsidiary fiow of gas is also applied to the classifier through a gas inlet 16 to help establish an eddy current within the chamber 13 as indicated by the arrows 17 and 18. This eddy current returns some of the particles of granular material at the bottom portion of the chamber 13 to the top of the chamber adjacent the vane 14a so that these particles again may flow downwardly past the vanes 14a through 14f.
  • FIG. 2 The action of the cascaded vanes 14a through 14 in providing a uniform classification, i.e., in uniformly withdrawing particles smaller in size than a predetermined reference particle, is best understood with reference to FIG. 2.
  • a particle 20 of granular material at an upper position adjacent the top vane 14a and at a lower position adjacent the vane 14e. Examining first the particle 20 in its upper position, there are effectively four forces acting upon the particle. The first is a downward force F which is related to the mass of the particle and to its downward movement. An exhaust force P is exerted upwardly and generally parallel to the vane 14a by the gas that is withdrawn from the gas entrained stream of particles past the vane 14a.
  • a small centrifugal force P is imparted to the particle as a result of its spin.
  • the resultant of all these forces is indicated as F which is substantially horizontal since the particle 20 is deemed to be the cut point particle. That is, with a horizontal resultant force acting upon the particle, the particle has as much of a chance of being swept upwardly through the vanes 14a through 14 and into the exhaust duct 19 as it has a passing downwardly past the vanes and into the coarse material outlet duct 15.
  • particles of a size greater than the cut point particle 20 would have resultant forces which are directed downwardly from the horizontal, thus increasing their chances of reaching the exhaust outlet 15.
  • particles smaller than the cut point particle 20 would have resultant forces directed upwardly with respect to the horizontal, thereby increasing their chances of passing through the vanes 14a through 14).
  • the centrifugal force F remains substantially constant.
  • the total downward force acting on the particle decreases, however, due to the progressive withdrawal of gas from the stream through the vanes 14a through 14
  • the downward force F acting upon the particle 20 in its lower position adjacent the vane 14a is less than the force F acting upon the particle in its upper position adjacent the vane 14a. Accordingly, if the resultant force F acting upon the particle in this lower position is to remain unchanged, thereby rendering constant the cut point characteristics of the classifier throughout the entire series of the vanes 14a through 141, the exhaust force F must change correspondingly.
  • each of the vanes 14a through 14 is positioned at an angle with respect to a vertical reference plane 21.
  • the angle that each vane forms with the vertical plane 21 is larger than the angle formed by any lower vane.
  • the vanes 14a through 14 overlap to form what may be considered separate exhaust ducts between adjacent ones of the vanes. Because of the overlapping and varying angular arrangements of the vanes, these ducts exhibit varying gas flow characteristics. The flow characteristics are graded or varied so that the gas flow resistances provided by the ducts increase for progressively lower ducts, i.e., so that gas is withdrawn from the stream at progressively decreasing velocities at successively lower positions in the stream.
  • Apparatus for efiecting a uniform classification of gas entrained particles comprising a substantially upwardly extending main exhaust duct, gas flow control means including a plurality of smaller substantially upwardly extending exhaust ducts in said main exhaust duct, means for providing a pressure differential across said gas fiow control means to provide gas flow therethrough, means for conveying a stream of the .gas entrained particles downwardly in front of said gas flow control means thereby providing passage of gas through the stream of downwardly flowing particles and through the plurality of smaller exhaust ducts to remove predetermined ones of the particles from the stream, the passage of gas through the stream acting to decrease the downward forces acting on the particles, said gas flow control means providing resistances to the flow of gas therethrough increasing in a downward direction therealong thereby to pass gas at successively lower velocities through the stream to provide a net force on the particles that remains substantially constant.
  • the method of uniformly classifying a flowing stream of particles comprising the steps of passing gas through and at least partially counter to the direction of the stream to withdraw predetermined ones of the particles from the stream, the gas passing through the stream acting to slow the movement of the particles remaining in the stream and thus to decrease the force acting on the particles in the direction of stream movement, and progressively decreasing the velocity at which the gas passes through the stream at successive positions in the stream in the direction of stream movement to provide a net force on the particles that remains substantially constant.

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Description

March 15, 1966 Filed Dec. 11, 1961 GAS ENTRAINED GRANULAR MATERIAL GAS WITHDRAWAL MEANS INVENTOR JEAN- PAUL VANDENHOECK ATTORNEYS .a second exhaust duct.
United States Patent 3,240,335 CLASSIFIER WITH GAS FLOW DISTRIBUTOR Jean Paul Vandenhoeck, New York, N.Y., assignor to Buell Engineering Company, Inc., New York, N.Y., a corporation of New York Filed Dec. 11, 1961, Ser. No. 158,509 3 Claims. (Cl. 209-436) This invention relates to apparatus for classifying granular material and, more particularly to apparatus for classifying granular material employing gravitational classifying techniques.
Heretofore, classification of granular material using gravitational classifying techniques has been effected by conveying a gas entrained granular material downwardly in a stream. As the material flows downwardly, gas is withdrawn from the stream, carrying with it particles of a certain size through an exhaust duct. The remainder of the gas and granular material pass downwardly through The degree of classification is varied by varying the amount of gas withdrawn from the falling stream of gas entrained granular material and thereby the size of the heaviest particles carried away with the withdrawn gas.
In a system of the type just described, the total downward forces acting upon any particular particle of material in the stream decrease at successively lower positions in the stream due to the braking effect on the downward movement of the particle by the gas that is withdrawn. If, then, the same exhaust force is applied to the stream at all points in its downward course, as is the case with systems of the prior art, the net forces acting upon any particular downwardly fiowing particle do not remain constant throughout the downward travel, and, therefore, the classification effected is not uniform.
This invention is directed toward providing a classifying system utilizing gravitational and or inertial classifying techniques in which the net forces acting upon any downwardly flowing particle of granular material are equal throughout the entire course of the particles downward flow. This is accomplished by varying the exhaust forces acting upon the particles during their downward flows in accordance with the decreasing downward forces acting upon the particles.
In an illustrative embodiment of the invention, the varying exhaust forces are provided by a substantially vertical series of cascaded vanes positoned adjacent the downwardly flowing stream of material. Each of the vanes forms a different angle with a vertical plane, the angles decreasing from top to bottom through the series of vanes. By this arrangement, adjacent vanes effectively form single exhaust ducts, and, because of the varying angular positions of the vanes, each duct provides a gas flow characteristic different from any other duct. Specifically, the flow resistances progressively increase at successively lower positions in the stream, thereby providing decreasing exhaust forces on a particular particle as it proceeds downwardly past the vanes to compensate for the decreasing downward force acting upon the particle. Thus, the net force acting upon the particle remains substantially constant, and a uniform clasisfication is effected.
A detailed description of the invention follows, which is to be read in conjunction with the appended drawing in which:
FIG. 1 is a sectional view of a typical classifying unit embodying the principles of the invention; and
FIG. 2 is a view of a series of cascaded vanes shown in FIG. 1, together with vector diagrams of the forces acting upon a single particle of material at two different positions in front of the vanes.
Referring to FIG. 1, a typical classifying unit 11 is shown having an input line 12 into which a stream of 3,24%,335 Patented Mar. 15, 1966 gas entrained granular material is introduced, as shown by the arrows in the figure. The gas entrained granular material flows downwardly through the input line 12 and into a classifying chamber 13. Within the chamber, the stream flows downwardly past a series of cascaded vanes 14a through 14] toward a coarse material outlet duct 15 provided at the lower portion of the classifying chamber 13. A subsidiary fiow of gas is also applied to the classifier through a gas inlet 16 to help establish an eddy current within the chamber 13 as indicated by the arrows 17 and 18. This eddy current returns some of the particles of granular material at the bottom portion of the chamber 13 to the top of the chamber adjacent the vane 14a so that these particles again may flow downwardly past the vanes 14a through 14f.
As the particles of granular material flow downwardly past the vanes 14a through 14 gas is withdrawn from the stream through an exhaust duct 19 to provide a pressure differential across the vanes and, along with the withdrawn gas, relatively fine ones of the particles flowing past the vanes are also withdrawn. Relatively coarse particles of the material not passing through the vanes 14a through 14 are exhausted through the coarse material outlet duct 15.
The action of the cascaded vanes 14a through 14 in providing a uniform classification, i.e., in uniformly withdrawing particles smaller in size than a predetermined reference particle, is best understood with reference to FIG. 2. In that figure there is shown a particle 20 of granular material at an upper position adjacent the top vane 14a and at a lower position adjacent the vane 14e. Examining first the particle 20 in its upper position, there are effectively four forces acting upon the particle. The first is a downward force F which is related to the mass of the particle and to its downward movement. An exhaust force P is exerted upwardly and generally parallel to the vane 14a by the gas that is withdrawn from the gas entrained stream of particles past the vane 14a. A small centrifugal force P is imparted to the particle as a result of its spin. The resultant of all these forces is indicated as F which is substantially horizontal since the particle 20 is deemed to be the cut point particle. That is, with a horizontal resultant force acting upon the particle, the particle has as much of a chance of being swept upwardly through the vanes 14a through 14 and into the exhaust duct 19 as it has a passing downwardly past the vanes and into the coarse material outlet duct 15. Of course, particles of a size greater than the cut point particle 20 would have resultant forces which are directed downwardly from the horizontal, thus increasing their chances of reaching the exhaust outlet 15. On the other hand, particles smaller than the cut point particle 20 would have resultant forces directed upwardly with respect to the horizontal, thereby increasing their chances of passing through the vanes 14a through 14).
As the particle 20 passes downwardly past the vanes 14a through 14 the centrifugal force F remains substantially constant. The total downward force acting on the particle decreases, however, due to the progressive withdrawal of gas from the stream through the vanes 14a through 14 Thus, the downward force F acting upon the particle 20 in its lower position adjacent the vane 14a is less than the force F acting upon the particle in its upper position adjacent the vane 14a. Accordingly, if the resultant force F acting upon the particle in this lower position is to remain unchanged, thereby rendering constant the cut point characteristics of the classifier throughout the entire series of the vanes 14a through 141, the exhaust force F must change correspondingly. This is what is accomplished by the cascade vanes 14a through 14 As may be seen, each of the vanes 14a through 14 is positioned at an angle with respect to a vertical reference plane 21. The angle that each vane forms with the vertical plane 21 is larger than the angle formed by any lower vane. Thus, the vanes 14a through 14 overlap to form what may be considered separate exhaust ducts between adjacent ones of the vanes. Because of the overlapping and varying angular arrangements of the vanes, these ducts exhibit varying gas flow characteristics. The flow characteristics are graded or varied so that the gas flow resistances provided by the ducts increase for progressively lower ducts, i.e., so that gas is withdrawn from the stream at progressively decreasing velocities at successively lower positions in the stream. In this fashion, the exhaust forces applied to the particles decrease as the particles pass downwardly past th'e'vanes. As may be seen, the exhaust force F acting on the particle 20 in its upper position is greater than the exhaust force F acting on the particle in its lower position. In this fashion, the resultant force F remains constant, and the cut point characteristics of the classifier do not change.
it is apparent that a novel classifying unit has been provided utilizing a series of individual exhaust passages or ducts having varying gas flow characteristics. It may be appreciated that the embodiment shown is susceptible of being modified in a manner which would nonetheless retain it within the scope of the invention. Therefore, the invention should not be deemed to be limited except as it is defined by the following claims.
I claim:
1. Apparatus for efiecting a uniform classification of gas entrained particles, comprising a substantially upwardly extending main exhaust duct, gas flow control means including a plurality of smaller substantially upwardly extending exhaust ducts in said main exhaust duct, means for providing a pressure differential across said gas fiow control means to provide gas flow therethrough, means for conveying a stream of the .gas entrained particles downwardly in front of said gas flow control means thereby providing passage of gas through the stream of downwardly flowing particles and through the plurality of smaller exhaust ducts to remove predetermined ones of the particles from the stream, the passage of gas through the stream acting to decrease the downward forces acting on the particles, said gas flow control means providing resistances to the flow of gas therethrough increasing in a downward direction therealong thereby to pass gas at successively lower velocities through the stream to provide a net force on the particles that remains substantially constant.
2,, Apparatus as recited in claim 1 wherein said plurality of smaller exhaust ducts are formed from a plurality of inclined vanes spaced one over another adjacent the stream, each smaller duct being formed from a pair of adjacent vanes, and the vanes being more steeply inclined for successively lower vanes.
3. The method of uniformly classifying a flowing stream of particles, comprising the steps of passing gas through and at least partially counter to the direction of the stream to withdraw predetermined ones of the particles from the stream, the gas passing through the stream acting to slow the movement of the particles remaining in the stream and thus to decrease the force acting on the particles in the direction of stream movement, and progressively decreasing the velocity at which the gas passes through the stream at successive positions in the stream in the direction of stream movement to provide a net force on the particles that remains substantially constant.
References Cited by the Examiner UNITED STATES PATENTS 1,079,979 12/1913 Fletcher 209-136 2,777,576 1/1957 Stevenson 20913 6 3,006,470 10/ 1961 Franken 209-132 FOREIGN PATENTS 515,058 11/1939 Great Britain.
HARRY B. THORNTON, Primary Examiner.
FRANK W. LUTTER, RICHARD A. OLEARY,
Examiners.

Claims (1)

1. APPARATUS FOR EFFECTING A UNIFORM CLASSIFICATION OF GAS ENTRAINED PARTICLES, COMPRISING A SUBSTANTIALLY UPWARDLY EXTENDING MAIN EXHAUST DUCT, GAS FLOW CONTROL MEANS INCLUDING A PLURALITY OF SMALLER SUBSTANTIALLY UPWARDLY EXTGENDING EXHAUSE DUCTS IN SAID MAIN EXHAUSE DUCT, MEANS FOR PROVIDING A PRESSURE DIFFERENTIAL ACROSS SAID GAS FLOW CONTROL MEANS TO PROVIDE GAS FLOW THERETHROUGH, MEANS FOR CONVEYING A STREAM OF THE GAS ENTRAINED PARTICLES DOWNWARDLY IN FRONT OF SAID GAS FLOW CONTROL MEANS THEREBY PROVIDING PASSAGE OF GAS THROUGH THE STREAM OF DOWNWARDLY FLOWING PARTICLES AND THROUGH THE PLURALITY OF SMALLER EXHAUST DUCTS TO REMOVE PREDETERMINED ONES OF THE PARTICLES FROM THE STREAM, THE PASSAGE OF GAS THROUGH THE STREAM ACTING TO DECRESE THE DOWNWARD FORCES ACTING ON THE PARTICLES SAID GAS FLOW CONTROL MEANS PROVIDING RESISTANCES TO THE FLOW OF GAS THERETHROUGH INCRESING IN A DOWNWARD DIRECTION THEREALONG THEREBY TO PASS GS AT SUCCESSIVELY LOWER VELOCITIES THROUGH THE STREAM TO PROVIDE A NET FORCE ON THE PARTICLES THAT REMAINS SUBSTNTIALLY CONSTANT.
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3397780A (en) * 1965-04-27 1968-08-20 Buell Engineering Company Inc Classification apparatus
US3426893A (en) * 1967-04-18 1969-02-11 Kennedy Van Saun Co Method and apparatus for classifying finely-divided solids carried in a gas stream
US3538688A (en) * 1968-06-13 1970-11-10 Aeroglide Corp Lower filter assembly
US4915824A (en) * 1985-08-12 1990-04-10 Surtees Guy F Pneumatic classifier for tobacco and method
US5205415A (en) * 1991-07-10 1993-04-27 The Standard Commercial Tobacco Co., Inc. Modular classifier
US5325875A (en) * 1987-08-24 1994-07-05 Universal Leaf Tobacco Co., Inc. Apparatus for separating threshed leaf tobacco
US5344025A (en) * 1991-04-24 1994-09-06 Griffin & Company Commingled waste separation apparatus and methods
US6435191B1 (en) 1999-02-26 2002-08-20 Dimon Inc. Tobacco separator
US6543619B1 (en) * 2001-03-20 2003-04-08 Advanced Sorting Technologies, Llc Method and apparatus for sorting utilizing a product rake and a relief valve
US6910585B1 (en) 2000-08-31 2005-06-28 Fisher-Klosterman, Inc. Dynamic centrifugal gas classifier and method of classifying performed therewith
US20100064953A1 (en) * 2008-09-15 2010-03-18 Alstom Technology Ltd Exhauster bypass system
WO2013102451A1 (en) * 2012-01-07 2013-07-11 Dirk Barnstedt Cyclone-like separator, in particular for waste management
US10131507B1 (en) 2017-07-27 2018-11-20 Mss, Inc. Ejector hood

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1079979A (en) * 1912-03-27 1913-12-02 American Steel Foundries Device for reclaiming sand.
GB515058A (en) * 1938-05-20 1939-11-24 Harold Edward Blake Improvements in or relating to separators
US2777576A (en) * 1954-03-05 1957-01-15 Stevenson Calvin Separating apparatus
US3006470A (en) * 1958-06-20 1961-10-31 Tongeren N V Bureau Van Apparatus for classifying particulate material

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1079979A (en) * 1912-03-27 1913-12-02 American Steel Foundries Device for reclaiming sand.
GB515058A (en) * 1938-05-20 1939-11-24 Harold Edward Blake Improvements in or relating to separators
US2777576A (en) * 1954-03-05 1957-01-15 Stevenson Calvin Separating apparatus
US3006470A (en) * 1958-06-20 1961-10-31 Tongeren N V Bureau Van Apparatus for classifying particulate material

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3397780A (en) * 1965-04-27 1968-08-20 Buell Engineering Company Inc Classification apparatus
US3426893A (en) * 1967-04-18 1969-02-11 Kennedy Van Saun Co Method and apparatus for classifying finely-divided solids carried in a gas stream
US3538688A (en) * 1968-06-13 1970-11-10 Aeroglide Corp Lower filter assembly
US4915824A (en) * 1985-08-12 1990-04-10 Surtees Guy F Pneumatic classifier for tobacco and method
US5476109A (en) * 1987-08-24 1995-12-19 Universal Leaf Tobacco Co., Inc. Apparatus for separating threshed leaf tobacco
US5325875A (en) * 1987-08-24 1994-07-05 Universal Leaf Tobacco Co., Inc. Apparatus for separating threshed leaf tobacco
US5344025A (en) * 1991-04-24 1994-09-06 Griffin & Company Commingled waste separation apparatus and methods
US5205415A (en) * 1991-07-10 1993-04-27 The Standard Commercial Tobacco Co., Inc. Modular classifier
US5358122A (en) * 1991-07-10 1994-10-25 The Standard Commercial Tobacco Company, Inc. Multiple stage tobacco classifier
US6435191B1 (en) 1999-02-26 2002-08-20 Dimon Inc. Tobacco separator
US6910585B1 (en) 2000-08-31 2005-06-28 Fisher-Klosterman, Inc. Dynamic centrifugal gas classifier and method of classifying performed therewith
US6543619B1 (en) * 2001-03-20 2003-04-08 Advanced Sorting Technologies, Llc Method and apparatus for sorting utilizing a product rake and a relief valve
US20100064953A1 (en) * 2008-09-15 2010-03-18 Alstom Technology Ltd Exhauster bypass system
US8097059B2 (en) * 2008-09-15 2012-01-17 Alstom Technology Ltd Exhauster bypass system
WO2013102451A1 (en) * 2012-01-07 2013-07-11 Dirk Barnstedt Cyclone-like separator, in particular for waste management
US10131507B1 (en) 2017-07-27 2018-11-20 Mss, Inc. Ejector hood
US10464761B1 (en) * 2017-07-27 2019-11-05 Mss, Inc. Ejector hood

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