US1660682A - Air-blast classifier - Google Patents

Air-blast classifier Download PDF

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Publication number
US1660682A
US1660682A US79935A US7993526A US1660682A US 1660682 A US1660682 A US 1660682A US 79935 A US79935 A US 79935A US 7993526 A US7993526 A US 7993526A US 1660682 A US1660682 A US 1660682A
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air
blast
casing
materials
air blast
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US79935A
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Albert H Stebbins
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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
    • B07B7/04Selective separation of solid materials carried by, or dispersed in, gas currents by impingement against baffle separators

Definitions

  • This invention relates to classifiers for separating fine dust-like materials and employs a strong air blast having the materials erally out of the direct path of the air blast.
  • This-tendency of the lighter particles to separate out of the direct path of an air blast is taken advantage of in carrying out the present invention, and one important feature of the present invention resides in the arrangement whereby a strong blast of air bearing the materials to be separated is subjected to air currents that move transversely to the path of the air blast and carry off the lighter particles without disturbing the heavier particles.
  • a more specific feature of the" invention resides in a casing having a nozzle for delivering a strong blast of air bearing the materials to be treated into the casing, and in means for exhausting air from the casing at one side of the air blast to produce air currents traveling around and laterally from the air blast to carry 01f the lighter particles.
  • FIG. 1 is a vertical sectional view thru an air blast classifier constructed in accordance with the present invention
  • Fig. 2 is a sectional view taken on the line 2-2 of Fig. 1;
  • Fig. 3 is 8.,S60t10n2l1 view taken on the line 3-3 of F ig. 1.
  • the classifier of the present invention is designed more particularly for the treatment of fine, dust-like" materials and the casing 10 in which the separation ofthe materials is effected may be given any desired shape, but. is shown as comprising an upright casing having the opposite side walls 11 and 12 and the end walls 13, l iand 15.
  • the materials to be treated are'blown into the easmg 10 thru the pipe or nozzle 16 which may enter the casing thru the end wall 13.
  • the opposite end walls 14 and 15 are shown as disposed a substantial distance from the wall 13 so that the air blast discharged by the nozzle 16 may travel a substantial distance before reaching the opposite walls of the casing.
  • Air under pressure is supplied to the nozzle 16 by the conduit 17 which may be provided with a fan or blower 18 of any suitable construction, but since the air should be discharged from the nozzle 16 in the form of a strong blast the fan or blower 18 should be so constructed that .it will force air into the conduit 17 under relatively high pressure.
  • the fine dust-like materials to be treated are carried into the casing 10 with the blast of air, and in the construction shown means is provided for feeding a contmuous supply of materials to the air passing to the nozzle 16.
  • the fine, dust-like materials are fed to the conduit 17' by a hopper 19 which is provided near its lower end-with the spaced inclined walls or floor plates 20 arranged to form a slot between them thru which the materials may pass into the conduit 17
  • the lower end of the hopper 19 is preferably secured to an enlarged portion 21 formed upon the conduit 17
  • the fine, dust-likematerials supplied by the hopper 19 may tend to pack in the lower portion of the hopper against the inclined floor plates 20, and in" order to insure -a continuous flow of'these materials to the conduit, a feed disk 22 may be provided secured to the operating shaft 23' the opposite ends of which shaft are journaled in the side walls of the hopper 19, and this shaft may be rotated by a pulley 24 secured to one end of the shaft.
  • the disk 22 is preferably provided with
  • This type of feeding means will feed the materials to the conduit 17 as long as the disk is rotated by the pulley 24, but the feeding of these materials will stop when the disk 22 stops rotating,-
  • Air currents which travel at substantially a right angle to the path of the air blast are pro vided for carrying out of the casing 10 the lighter particles that tend to separate out of the air blast, and while various constructions might be provided for producing these air currents, they are produced in the present case by exhausting air from the upper portion of the casing 10. This is accomplished by providing a pipe or conduit 26 which leads from the upper end of the casing 10 to a suction fan 27 and the amount of air drawn out of the casing by the suction fan 27 may be controlled by adjusting the valve 28 within the pipe 26.
  • the casing 10 is preferably made relatively narrow in cross section, as will be apparent from Fig. 2, this construction being desirable because it will cause air currents rising within the casing 10 to pass relatively close to the air blast.
  • the casing is provided with the openings 32 and 33 which may be controlled by the sliding gates 34 and 35. From the construction just described it will be seen that the gates 31,34 and 35 may be adjusted to determine whether air will be delivered to the casing 10 at points below or above the air blast.
  • the heavier materials that are carried a substantial distance across the casing 10 by the force of the air blast will settle in the chamber 25 and move downwardly into the discharge hopper 36 having the discharge gate 37, and the particles which settle out of the air blast before they reach the chamber 25 will move downwardly into the hopper 38 from which they may be discharged thru the gate 39. It may be desirable to provide a partition or wall 40 within the.
  • the successful operation of the present classifier is due largely to the fact that when air under pressure is discharged from a nozzle it expands laterally from the central path of the air jet in more or less of the form of a cone, and the lighter particles are carried out of the direct path of the air jet by this expansion whereupon they are carried upwardly by the rising air currents within the receptacle.
  • the heavier particles due to their greater momentum will not be deflected appreciably by the lateral expansion otthe air just mentioned or by the rising air currents, and will be carried by their propelling force against the walls 14, 15.
  • Such lighter particles as may be carried by the force of the blast into the second chamber 25 before they separate out of the air blast will be carried upwardly by the air exhausted from the chamber 25 through the opening 41, while the heavier particles that settle in the chamber 25 will move downwardly into the hopper 36 as above pointed out.
  • the rotating disk 22 serves to feed the fine, dust-like materials continuously to the conduit 17 to be carried into the casing 1O.
  • An air blast classifier for separating fine dust-like materials, comprising in combination, a casing constructed to form a long narrow treatment chamber within which an air blast may travel a substantial distance along a straight uninterrupted path, a nozzle having a reduced discharge end located at one end of the casing to direct a jet-like blast of dust-laden air lengthwise of the treatment chamber so that in the air jet, means for introducing air into means for exhausting air from the upper portion of the casing to produce rising air currents that flow upwardly around the air jet to carry upwardly the lighter particles as they work out of the direct path of the air jet.
  • An air blast classifier for separating fine dust-like materials comprising in combination, acasing constructed to form a long narrow treatment chamber within which an air blast ma travel a substantial distance along a straig t uninterrupted path, means for dividing the chamber transversely into different compartments, a nozzle having areduced discharge end located at one end of the casing to direct a-jet-like blast of dustladen air lengthwise of the treatment chamher so that the heavier particles will be.

Description

Feb. 28, 1928. wwssz A. H. STEBBINS AIR BLAST CLASS IFIER Filed Jan. 8. 1926 flTTO FNEY Patented Feb. 28, 1928 UNITED STATES PATENT OFFICE.
AIR-BLAST cmxssirrnn.
Application filed January 8, 1926. Serial No. 79,985.
This invention relates to classifiers for separating fine dust-like materials and employs a strong air blast having the materials erally out of the direct path of the air blast.
This-tendency of the lighter particles to separate out of the direct path of an air blast is taken advantage of in carrying out the present invention, and one important feature of the present invention resides in the arrangement whereby a strong blast of air bearing the materials to be separated is subjected to air currents that move transversely to the path of the air blast and carry off the lighter particles without disturbing the heavier particles.
A more specific feature of the" invention resides in a casing having a nozzle for delivering a strong blast of air bearing the materials to be treated into the casing, and in means for exhausting air from the casing at one side of the air blast to produce air currents traveling around and laterally from the air blast to carry 01f the lighter particles.
Other; features of the invention and novel combination of parts, in addition to the above, will be hereinafter described in connection with the accompanying drawings which illustrate one good, practical form of the invention.
In the drawings- Fig. 1 is a vertical sectional view thru an air blast classifier constructed in accordance with the present invention;
.Fig. 2 is a sectional view taken on the line 2-2 of Fig. 1; and
' Fig. 3 is 8.,S60t10n2l1 view taken on the line 3-3 of F ig. 1.
The classifier of the present invention is designed more particularly for the treatment of fine, dust-like" materials and the casing 10 in which the separation ofthe materials is effected may be given any desired shape, but. is shown as comprising an upright casing having the opposite side walls 11 and 12 and the end walls 13, l iand 15. The materials to be treated are'blown into the easmg 10 thru the pipe or nozzle 16 which may enter the casing thru the end wall 13. The opposite end walls 14 and 15 are shown as disposed a substantial distance from the wall 13 so that the air blast discharged by the nozzle 16 may travel a substantial distance before reaching the opposite walls of the casing.
Air under pressure is supplied to the nozzle 16 by the conduit 17 which may be provided with a fan or blower 18 of any suitable construction, but since the air should be discharged from the nozzle 16 in the form of a strong blast the fan or blower 18 should be so constructed that .it will force air into the conduit 17 under relatively high pressure.
As stated, the fine dust-like materials to be treated are carried into the casing 10 with the blast of air, and in the construction shown means is provided for feeding a contmuous supply of materials to the air passing to the nozzle 16. In the present case the fine, dust-like materials are fed to the conduit 17' by a hopper 19 which is provided near its lower end-with the spaced inclined walls or floor plates 20 arranged to form a slot between them thru which the materials may pass into the conduit 17 The lower end of the hopper 19 is preferably secured to an enlarged portion 21 formed upon the conduit 17 The fine, dust-likematerials supplied by the hopper 19 may tend to pack in the lower portion of the hopper against the inclined floor plates 20, and in" order to insure -a continuous flow of'these materials to the conduit, a feed disk 22 may be provided secured to the operating shaft 23' the opposite ends of which shaft are journaled in the side walls of the hopper 19, and this shaft may be rotated by a pulley 24 secured to one end of the shaft. The disk 22 is preferably provided with ribs 22, at its opposite sides which will engage the ma-.
terials in the hopper when the disk is rotated, and will force the materials thru the slot into the conduit 17. This type of feeding means will feed the materials to the conduit 17 as long as the disk is rotated by the pulley 24, but the feeding of these materials will stop when the disk 22 stops rotating,-
as they tend."to pack between the floor plates 22 and the sides of the disk. Due to the pressure of the air within the conduit 17 this air may tend to force its way up thru the materials in the hopper l9 and the hopper is therefore made relatively tall as shown so that it will contain sufiici'ent materials to prevent the air "from moving upwardly thru the entire mass of materials As stated, the heavier materials within the blast of air delivered by the nozzle 16 will be carried. further by the force of the air blast than the lighter particles, and as a result these heavierparticles will be carried by the air blast over into the chamber 25 ofthe casing 10, while the lighter particles willtend to separate out of the air blast bebefore they reach the chamber 25. Air currents which travel at substantially a right angle to the path of the air blast are pro vided for carrying out of the casing 10 the lighter particles that tend to separate out of the air blast, and while various constructions might be provided for producing these air currents, they are produced in the present case by exhausting air from the upper portion of the casing 10. This is accomplished by providing a pipe or conduit 26 which leads from the upper end of the casing 10 to a suction fan 27 and the amount of air drawn out of the casing by the suction fan 27 may be controlled by adjusting the valve 28 within the pipe 26. The casing 10 is preferably made relatively narrow in cross section, as will be apparent from Fig. 2, this construction being desirable because it will cause air currents rising within the casing 10 to pass relatively close to the air blast.
It is desirable to admit air from the atmos phere into the lower portion of the casing 10 so that it will be drawn upwardly toward and around the air blast to carry 1 ofi? the lighter particles, and in the construction shown the airinlet openings or slots 29 are provided in the lower portion of the casing 10, as Will be apparent from Figs. 1 and 2. Thesize of these openings may be varied by providing the swinging doors 30 secured to the side walls 11 and 12 of the casing by hinges 31. These hinges may be made relatively stiff so that the will retain the doors in any position to w ich they may be adjusted; or other means may. be provided for retaining the doors 30 in the desiredvposition of adjustment. It may be desirable to admit air into the casing 10 at points above the air blast to vary the operation of the classifier, and to this end the casing is provided with the openings 32 and 33 which may be controlled by the sliding gates 34 and 35. From the construction just described it will be seen that the gates 31,34 and 35 may be adjusted to determine whether air will be delivered to the casing 10 at points below or above the air blast.
The heavier materials that are carried a substantial distance across the casing 10 by the force of the air blast will settle in the chamber 25 and move downwardly into the discharge hopper 36 having the discharge gate 37, and the particles which settle out of the air blast before they reach the chamber 25 will move downwardly into the hopper 38 from which they may be discharged thru the gate 39. It may be desirable to provide a partition or wall 40 within the.
further treatment. \a
The successful operation of the present classifier is due largely to the fact that when air under pressure is discharged from a nozzle it expands laterally from the central path of the air jet in more or less of the form of a cone, and the lighter particles are carried out of the direct path of the air jet by this expansion whereupon they are carried upwardly by the rising air currents within the receptacle. The heavier particles due to their greater momentum will not be deflected appreciably by the lateral expansion otthe air just mentioned or by the rising air currents, and will be carried by their propelling force against the walls 14, 15. Such lighter particles as may be carried by the force of the blast into the second chamber 25 before they separate out of the air blast will be carried upwardly by the air exhausted from the chamber 25 through the opening 41, while the heavier particles that settle in the chamber 25 will move downwardly into the hopper 36 as above pointed out. The rotating disk 22 serves to feed the fine, dust-like materials continuously to the conduit 17 to be carried into the casing 1O.
What is claimed is 1. An air blast classifier for separating fine dust-like materials, comprising in combination, a casing constructed to form a long narrow treatment chamber within which an air blast may travel a substantial distance along a straight uninterrupted path, a nozzle having a reduced discharge end located at one end of the casing to direct a jet-like blast of dust-laden air lengthwise of the treatment chamber so that in the air jet, means for introducing air into means for exhausting air from the upper portion of the casing to produce rising air currents that flow upwardly around the air jet to carry upwardly the lighter particles as they work out of the direct path of the air jet.
2. An air blast classifier for separating fine dust-like materials, comprising in combination, acasing constructed to form a long narrow treatment chamber within which an air blast ma travel a substantial distance along a straig t uninterrupted path, means for dividing the chamber transversely into different compartments, a nozzle having areduced discharge end located at one end of the casing to direct a-jet-like blast of dustladen air lengthwise of the treatment chamher so that the heavier particles will be. shot by the force of the blast lengthwise of the entire casin and against the opposite end wall thereo means for forcing air bearing the materials to be separated through the nozzle under high pressure to impart to the different materialsthe same initial velocity so that as they travel along the path of the air jet the finer particles will be carried laterallfir by t e expansion of the air within the air jet, and means for exhausting air from the casing at one side of the air blast to produce air currents flowing around said air blast to carry off the lighter particles as they work out of the direct path of the air jet.
In testimony whereof, I have signed my name to this specification.
ALBERT H. STEBBINS.
out of the direct path of the air jet
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2461584A (en) * 1944-06-14 1949-02-15 Smidth & Co As F L Air separation method for slurry separation
US2652371A (en) * 1949-12-20 1953-09-15 Sinclair Refining Co Process of forming spheroidal catalyst particles
US2681477A (en) * 1950-08-23 1954-06-22 Lummus Cotton Gin Co Apparatus for separating trash from lint cotton and the like
US2681476A (en) * 1949-09-12 1954-06-22 Lummus Cotton Gin Co Process and apparatus for separating trash from lint cotton and the like
US2861299A (en) * 1958-11-25 Apparatus for and method of cleaning lint cotton
US2993598A (en) * 1957-08-13 1961-07-25 Fuller Co Harvesting method and apparatus
US3009574A (en) * 1957-08-13 1961-11-21 Hub Mfg Corp Harvesting apparatus
US3026789A (en) * 1959-12-03 1962-03-27 William H Mead Abrasive-blasting system
US3164548A (en) * 1961-06-15 1965-01-05 Imp Tobacco Co Ltd Tower type pneumatic separator
US3312343A (en) * 1964-05-07 1967-04-04 Hesston Corp Air separator
US3859205A (en) * 1972-01-31 1975-01-07 Crown Zellerbach Corp Apparatus and method for transporting fluid-entrainable particles
US4699710A (en) * 1985-02-26 1987-10-13 Williams Paul J Separator for particulates
US4851110A (en) * 1986-11-28 1989-07-25 T.D.J. Co., Inc. Air pump separator method and apparatus
US5348163A (en) * 1993-01-19 1994-09-20 Cabot Corporation Method and apparatus for separating fine particles
US6015048A (en) * 1994-09-21 2000-01-18 Canon Kk Gas current classifier and process for producing toner
US6540087B2 (en) * 2001-01-25 2003-04-01 Inter-Source Recovery Systems, Inc. Part separator having multiple inlets and method of supplying wet chips through multiple inlets
US9968944B2 (en) 2013-03-15 2018-05-15 Inter-Source Recovery Systems Parts separator

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2861299A (en) * 1958-11-25 Apparatus for and method of cleaning lint cotton
US2461584A (en) * 1944-06-14 1949-02-15 Smidth & Co As F L Air separation method for slurry separation
US2681476A (en) * 1949-09-12 1954-06-22 Lummus Cotton Gin Co Process and apparatus for separating trash from lint cotton and the like
US2652371A (en) * 1949-12-20 1953-09-15 Sinclair Refining Co Process of forming spheroidal catalyst particles
US2681477A (en) * 1950-08-23 1954-06-22 Lummus Cotton Gin Co Apparatus for separating trash from lint cotton and the like
US2993598A (en) * 1957-08-13 1961-07-25 Fuller Co Harvesting method and apparatus
US3009574A (en) * 1957-08-13 1961-11-21 Hub Mfg Corp Harvesting apparatus
US3026789A (en) * 1959-12-03 1962-03-27 William H Mead Abrasive-blasting system
US3164548A (en) * 1961-06-15 1965-01-05 Imp Tobacco Co Ltd Tower type pneumatic separator
US3312343A (en) * 1964-05-07 1967-04-04 Hesston Corp Air separator
US3859205A (en) * 1972-01-31 1975-01-07 Crown Zellerbach Corp Apparatus and method for transporting fluid-entrainable particles
US4699710A (en) * 1985-02-26 1987-10-13 Williams Paul J Separator for particulates
US4851110A (en) * 1986-11-28 1989-07-25 T.D.J. Co., Inc. Air pump separator method and apparatus
US5348163A (en) * 1993-01-19 1994-09-20 Cabot Corporation Method and apparatus for separating fine particles
US6015048A (en) * 1994-09-21 2000-01-18 Canon Kk Gas current classifier and process for producing toner
US6540087B2 (en) * 2001-01-25 2003-04-01 Inter-Source Recovery Systems, Inc. Part separator having multiple inlets and method of supplying wet chips through multiple inlets
US9968944B2 (en) 2013-03-15 2018-05-15 Inter-Source Recovery Systems Parts separator

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