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US2427423A - Reciprocating mechanism for inclined mineral separating pneumatic tables - Google Patents

Reciprocating mechanism for inclined mineral separating pneumatic tables Download PDF

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US2427423A
US2427423A US626807A US62680745A US2427423A US 2427423 A US2427423 A US 2427423A US 626807 A US626807 A US 626807A US 62680745 A US62680745 A US 62680745A US 2427423 A US2427423 A US 2427423A
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coal
links
reciprocating mechanism
shale
air
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US626807A
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George E Shawcross
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LLOYDS BANK Ltd
SAXON ENGINEERING Co Ltd
SAXON ENGINEERING COMPANY Ltd
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LLOYDS BANK Ltd
SAXON ENGINEERING Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B4/00Separating by pneumatic tables or by pneumatic jigs
    • B03B4/02Separating by pneumatic tables or by pneumatic jigs using swinging or shaking tables

Definitions

  • the invention relates mainly to the dry cleaning of coal, particularly of the smaller sizes, but may also be used for the dry separation of other minerals such as tin ore from gangue. While wet processes will produce a satisfactory separation of coal and shale or dirt, the subsequent elimination of the water or other liquid involves heavy additional expense when small coal is in question. Proposals have been made for the dry cleaning of small coal, but no such proposal has been entirely successful in practice in that it provided an output of shale completely free of coal and of coal without appreciable admixture of shale.
  • the usual form of apparatus for the dry cleaning of coal comprises a perforated table set on a slope and oscillated in an oblique direction making also an oblique angle with the table.
  • the table is perforated for the passage of air to keep the bed of raw coal in a floating state during treatment, so that the shale may sink to the bottom of the layer and be conveyed to the top end of thetable, while the cleaned coal slides down over the shale to be discharged at the lower end.
  • the present invention relates to apparatus in'accordance with this general description. It is, of course, understood that with other mnerals the heavier constituent is usually the wanted product, but this makes no difference to the apparatus in question, which always discharges the heavier constituent at the upper end of the table.
  • the apparatus has three features in combination, rstly the direction of oscillation is not the same at both ends, having a larger vertical component at the'lower end, secondly means such as discharge weirs are tted at both ends of the active surface of the table to maintain the depth of material under treatment at a suitable value, and thirdly the table surface is made rough or uneven in such a manner as to ensure transmission of the conveying effect to the material in contact with it.
  • the perforations in the table should preferably be small and closely spaced. They may for instance be diameter at 1/2" spacing, giving a perforation area less than 3% of the table area.
  • the preferred form of the table surface is of serrated longitudinal section with low steep fronts facing towards the upper end and with the reverse slopes quite gentle. It is then convenient to place a row of holes near the bottom of each dip and a second row part way up the slope; the next row of holes would then be in the next dip.
  • Adjustable dampers may run transversely of the table on its under side to modify the distribution of air so as to secure the best results. These may be flaps adjustable through a right angle on fixed bars attached to the table. Usual-i ⁇ ly it is desirable to vshut off the air completely or nearly so for a short distance at the top end and to reduce the air discharge a little for perhaps a quarter or a fifth of the table length at the lower end, but other adjustments may be better vfor certain varieties of coal.
  • the discharge Weir at the upper end is preferably made sloping to provide a gentle ramp over which the shale will glide easily. Such a feature is of less value at the lower end because of the smaller friction of coal.
  • Either or both of the discharge weirs may be made adjustable in slope or height or both. It is preferable to set the coal discharge Weir higher than the shale discharge Weir to equalise the resistance to the'passage of air through the bed, since the heavier shale imposes a greater resistance than an equally thick layer of coal. For the smaller sizes the bed may be 1%" thick at the shale end and 21/2 thick at the coal end, ⁇ but with larger sizes the depth should be made commensurate with the size of the pieces of material. Two other adjustments are desirable. One is 3 that of the slope of the table itself and the other is that of the directions of oscillation.
  • Figures v2 and 3 fragmental views in section and plan respectively of a portion of the bed on an enlarged scale.
  • a table I of suitable width for the quantity of material t be treated is supported on two longitudinal girders 2, one at each side.
  • the girders are set at a suitable slope, the left hand end as viewed in Figure 1 being the lower one.
  • one girder has a bearing housing 3 in which is rotatably mounted one end of a shaft 4, the other end being similarly mounted in a bearing housing on the otherY girder 2.
  • each girder has another bearing housing 5, in which is rotatably mounted one end of a shaft 6. All the bearings are of the solid rubber type.
  • a link 1 is keyed to the shaft 4 and is keyed at its lower end to a shaft 8, which is mounted at each end by a solid rubber bearing in a, housing 9 fixed to the stationary framework I0 of the apparatus.
  • a link II is keyed to the shaft 6 just inside each bearing and is keyed at its lower end to av-shaft I2, which is mounted at each end by a solid rubber bearing in a housing I3 xed to the framework I0.
  • the links 1 and II slope as shown, but the links II are more nearly upright than the links 1, so that the vertical component of the table movement is less at the right hand or higher end than at the left.
  • the two links 1 are united ⁇ by a plate I4 and the two links II by a plate I5 to ensure that there shall be no lateral oscillation of the table I.
  • the links ⁇ 1 A are extended upwards beyond the bearings 3, each carrying a short length of shaft I5 to which an eccentric strap I1 is linked by a solid 'rubber bearing.
  • the two eccentrics are mounted on a shaft I8 journalled in bearings I9 on the framework I0.
  • a pulley 20 on the shaft I8 is ldriven from any suitable source of power.
  • the links 'I have extensions 2
  • the bearings I9 can be adjusted in a left and right direction to adjust the slope of the table by a small amount.
  • the slope is varied by this adjustment because the links 1 are shorter than the links I I between shaft centres.
  • The'surface of the table is of a serrated section with steep fronts 23 facing to the right as shown inl- Figure 2.
  • Perforations 24 as shown in Figure 3 are provided in the table surface. The perforations are arranged in transverse rows at equal spacings, each alternate row being at the bottom of a serration.
  • the lower side of the table is enclosed by a casing 25 connected by flexible material 26 such as canvas to a xed casing 21, which is supplied with clean air at low pressure from a fan (not shown).
  • bailles 28, 28 project downwards from the table surface ⁇ to form airA chambers.
  • Each of the five air chambers shown- has a buttery valve 29 to regulate the vposition by means of a quadrant 49.
  • the table has side walls 30 to prevent the material from falling off the sides.
  • a weir 3I is provided at the left hand end of the table to maintain a suitable depth of material.
  • the height of the Weir can be adjusted by means of a rack ⁇ 32 and pinion 33 at veach ⁇ .end,.a hand lever 34 being provided for rotatingthe pinion shaft.
  • the Weir 3l is locked in its adjusted
  • the clean coal is discharged by a chute 35 into another chute 36.
  • the table is unperforated from the highest baille 28 to the end, and here there is a sloping Weir 31 set to give an easy glide angle for the shale.
  • the weir 31 is adjustable in height by means of a rack 38 and pinion 39 at each end, the pinions 39 being mounted on a common shaft, which can be rotated by a hand lever 40 and locked in adjusted position by means of a quadrant 50.
  • the shale falling over the top of the weir 31 is discharged into a chute 4I.
  • the raw coal is fed into a stationary hopper 42 of which the discharge end is in close proximity to a plate 43 hinged at its left hand end.
  • the plate 43 is supported on a structure 44 attached to the girders 2 so as to participate in the vibration imparted to the latter. As a result the coal feedis only in operation while the apparatus is working, and no separate device is required to stop the feed when shutting down.
  • the plate 43 is hinged to adjust the rate of feed.
  • the ⁇ coal falls in succession on to a series of plates 45, 45 and then onto a corrugated plate 46, by which it is distributed over the whole width of the table.
  • the plates 43, 45and 46 are enclosed in a casing 41.from which air for dedusting is drawn through a ilexible connection 48 by a fan (not shown). If dedusting is not required, the casing 41 is omitted andthe corrugated plate 46 4is extendedup to the plate 43, the plates 45 being omitted, since their sole function is to provide a coal cascade through which dedusting air can be drawn.
  • the upper side of the table is left open, as practically no dust isv produced in the process of cleaning.
  • the operator can see at any time how the apparatus is working and can at once make any .adjustments which he may deem advisable.
  • the air pressure does not need to be high, in fact it should konly be sufficient in conjunction with the table vibration to maintain fluidity of the bed of coal.
  • the raw coal is first screened into suitable ranges of particle size, and each fraction is treated on a separatetable.
  • a suitable grading may be into six sizes, 1% to in", 1% to B/Bl 1%', lll glr lill S/l sie to 0, but it is advisable to de-dust the smallest size.
  • Apparatus for the dry separation of minerals comprisingga sloping perforated table, air supply means lon the underside of the table,v a fixed supporting structure for the table, links pivoted on the supporting structure and on' the table near the lower end thereof and sloping upwards towards the lower end of the table, links pivoted on the supporting structure and on the table near the upper end thereof and sloping upwards towards the lower end of the table but with less deviation from the vertical than the mst-mentioned links, the said links constituting the sole support of the table from the supporting structure, said second mentioned links being longer than said mst-mentioned links between pivot centres, an eccentric having its strap linked to the table and its sheave driven by a source of power, and means for adjusting the position of the eccentric sheave to vary the slope of the table.

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Description

G. E. SHWCROSSSv RECIPROCATING MECHANISM FOR INCLINED MINERAL sept. 16, 1,947.
SEPARATING PNEUMATIC TABLES Filed NOV. 5, 1945 www Patented Sept. 16, `1947 RECIPROCATING MECHANISM FOR IN- CLINED DHNERAL SEPARATING PNEU- MATIC TABLES George E. Shawcross, Fenton, YStoke-on-Trent,
England, assi'gnor of one-half to Saxon Engineering Company, Limited, Staffordshire, England; Lloyds Bank Limited, London, England, executor of said George E. Shawcross, deceased Application November 5, 1945, Serial No. 626,807 In Great Britain November 16, 1944 1 Claim.
. 1 The invention relates mainly to the dry cleaning of coal, particularly of the smaller sizes, but may also be used for the dry separation of other minerals such as tin ore from gangue. While wet processes will produce a satisfactory separation of coal and shale or dirt, the subsequent elimination of the water or other liquid involves heavy additional expense when small coal is in question. Proposals have been made for the dry cleaning of small coal, but no such proposal has been entirely successful in practice in that it provided an output of shale completely free of coal and of coal without appreciable admixture of shale.
The usual form of apparatus for the dry cleaning of coal comprises a perforated table set on a slope and oscillated in an oblique direction making also an oblique angle with the table. The table is perforated for the passage of air to keep the bed of raw coal in a floating state during treatment, so that the shale may sink to the bottom of the layer and be conveyed to the top end of thetable, while the cleaned coal slides down over the shale to be discharged at the lower end. The present invention relates to apparatus in'accordance with this general description. It is, of course, understood that with other mnerals the heavier constituent is usually the wanted product, but this makes no difference to the apparatus in question, which always discharges the heavier constituent at the upper end of the table.
According to the invention the apparatus has three features in combination, rstly the direction of oscillation is not the same at both ends, having a larger vertical component at the'lower end, secondly means such as discharge weirs are tted at both ends of the active surface of the table to maintain the depth of material under treatment at a suitable value, and thirdly the table surface is made rough or uneven in such a manner as to ensure transmission of the conveying effect to the material in contact with it.
Other features are desirable for improving the results still further, and these will first be enumerated. The perforations in the table should preferably be small and closely spaced. They may for instance be diameter at 1/2" spacing, giving a perforation area less than 3% of the table area. The preferred form of the table surface is of serrated longitudinal section with low steep fronts facing towards the upper end and with the reverse slopes quite gentle. It is then convenient to place a row of holes near the bottom of each dip and a second row part way up the slope; the next row of holes would then be in the next dip.
Where a very fine fraction of coal or other material is to be treated, such as from 53s" to als", this construction would not be suitable. A fine wire mesh may be used for material of the smaller particle sizes. The natural roughness of the Wire mesh due to the crossings of warp and weft is suflicient for ensuring that the heavier fraction in Contact with the table has the conveying effect transmitted to it. In fact, its greater conveying power will usually necessitate a greater slope of the table.
Adjustable dampersmay run transversely of the table on its under side to modify the distribution of air so as to secure the best results. These may be flaps adjustable through a right angle on fixed bars attached to the table. Usual-i` ly it is desirable to vshut off the air completely or nearly so for a short distance at the top end and to reduce the air discharge a little for perhaps a quarter or a fifth of the table length at the lower end, but other adjustments may be better vfor certain varieties of coal.
The discharge Weir at the upper end is preferably made sloping to provide a gentle ramp over which the shale will glide easily. Such a feature is of less value at the lower end because of the smaller friction of coal. l
Other features of the invention may be regarded as having the more immediate purpose of providing convenience in adjusting the table to the best operating conditions for whatever material is to be treated.
Either or both of the discharge weirs may be made adjustable in slope or height or both. It is preferable to set the coal discharge Weir higher than the shale discharge Weir to equalise the resistance to the'passage of air through the bed, since the heavier shale imposes a greater resistance than an equally thick layer of coal. For the smaller sizes the bed may be 1%" thick at the shale end and 21/2 thick at the coal end,` but with larger sizes the depth should be made commensurate with the size of the pieces of material. Two other adjustments are desirable. One is 3 that of the slope of the table itself and the other is that of the directions of oscillation.
The invention is illustrated by a table for the dry cleaning of small coal shown in the accompanying drawing, in which Figure 1 is a side elevation of the whole table, and
Figures v2 and 3 fragmental views in section and plan respectively of a portion of the bed on an enlarged scale.
Referring to the drawing, a table I of suitable width for the quantity of material t be treated is supported on two longitudinal girders 2, one at each side. The girders are set at a suitable slope, the left hand end as viewed in Figure 1 being the lower one. At the left hand end one girder has a bearing housing 3 in which is rotatably mounted one end of a shaft 4, the other end being similarly mounted in a bearing housing on the otherY girder 2.
At the right hand end each girder has another bearing housing 5, in which is rotatably mounted one end of a shaft 6. All the bearings are of the solid rubber type.
Just inside each bearing 3 a link 1 is keyed to the shaft 4 and is keyed at its lower end to a shaft 8, which is mounted at each end by a solid rubber bearing in a, housing 9 fixed to the stationary framework I0 of the apparatus. Similarly a link II is keyed to the shaft 6 just inside each bearing and is keyed at its lower end to av-shaft I2, which is mounted at each end by a solid rubber bearing in a housing I3 xed to the framework I0.
The links 1 and II slope as shown, but the links II are more nearly upright than the links 1, so that the vertical component of the table movement is less at the right hand or higher end than at the left. The two links 1 are united `by a plate I4 and the two links II by a plate I5 to ensure that there shall be no lateral oscillation of the table I.
To' provide for the reciprocation of the table, the links `1 Aare extended upwards beyond the bearings 3, each carrying a short length of shaft I5 to which an eccentric strap I1 is linked by a solid 'rubber bearing. The two eccentrics are mounted on a shaft I8 journalled in bearings I9 on the framework I0. A pulley 20 on the shaft I8 is ldriven from any suitable source of power. The links 'I have extensions 2| to press on springs 22 supported by their lower ends on the framework I0 to economise in driving power.
The bearings I9 can be adjusted in a left and right direction to adjust the slope of the table by a small amount. The slope is varied by this adjustment because the links 1 are shorter than the links I I between shaft centres.
The'surface of the table is of a serrated section with steep fronts 23 facing to the right as shown inl-Figure 2. Perforations 24 as shown in Figure 3 are provided in the table surface. The perforations are arranged in transverse rows at equal spacings, each alternate row being at the bottom of a serration. The lower side of the table is enclosed by a casing 25 connected by flexible material 26 such as canvas to a xed casing 21, which is supplied with clean air at low pressure from a fan (not shown).
It has been found advisable to regulate the current of air passing through the bed of material near the ends, and for this purpose bailles 28, 28 project downwards from the table surface `to form airA chambers. Each of the five air chambers shown-has a buttery valve 29 to regulate the vposition by means of a quadrant 49.
air flow. No such regulation is required ai; the central portion of the table.
The table has side walls 30 to prevent the material from falling off the sides. A weir 3I is provided at the left hand end of the table to maintain a suitable depth of material. The height of the Weir can be adjusted by means of a rack `32 and pinion 33 at veach `.end,.a hand lever 34 being provided for rotatingthe pinion shaft. The Weir 3l is locked in its adjusted The clean coal is discharged by a chute 35 into another chute 36.
At the upper end the table is unperforated from the highest baille 28 to the end, and here there is a sloping Weir 31 set to give an easy glide angle for the shale. The weir 31 is adjustable in height by means of a rack 38 and pinion 39 at each end, the pinions 39 being mounted on a common shaft, which can be rotated by a hand lever 40 and locked in adjusted position by means of a quadrant 50. The shale falling over the top of the weir 31 is discharged into a chute 4I.
The raw coal is fed into a stationary hopper 42 of which the discharge end is in close proximity to a plate 43 hinged at its left hand end. The plate 43 is supported on a structure 44 attached to the girders 2 so as to participate in the vibration imparted to the latter. As a result the coal feedis only in operation while the apparatus is working, and no separate device is required to stop the feed when shutting down. The plate 43 is hinged to adjust the rate of feed.
From the plate 43 the `coal falls in succession on to a series of plates 45, 45 and then onto a corrugated plate 46, by which it is distributed over the whole width of the table. The plates 43, 45and 46 are enclosed in a casing 41.from which air for dedusting is drawn through a ilexible connection 48 by a fan (not shown). If dedusting is not required, the casing 41 is omitted andthe corrugated plate 46 4is extendedup to the plate 43, the plates 45 being omitted, since their sole function is to provide a coal cascade through which dedusting air can be drawn.
The upper side of the table is left open, as practically no dust isv produced in the process of cleaning. The operator can see at any time how the apparatus is working and can at once make any .adjustments which he may deem advisable. The air pressure does not need to be high, in fact it should konly be sufficient in conjunction with the table vibration to maintain fluidity of the bed of coal.
In operation the raw coal is first screened into suitable ranges of particle size, and each fraction is treated on a separatetable. A suitable grading may be into six sizes, 1% to in", 1% to B/Bl 1%', lll glr lill S/l sie to 0, but it is advisable to de-dust the smallest size.
The more thorough separation achieved by means of the invention makes it possible to reduce the active length of the table to about six feet, which further conduces to economy in rst cost vand lin operating power. As already mentioned above, a very low vair pressure is sufficient, and this again represents a saving in power over existing apparatus for the same purpose.
What I claim is:
Apparatus for the dry separation of minerals comprisingga sloping perforated table, air supply means lon the underside of the table,v a fixed supporting structure for the table, links pivoted on the supporting structure and on' the table near the lower end thereof and sloping upwards towards the lower end of the table, links pivoted on the supporting structure and on the table near the upper end thereof and sloping upwards towards the lower end of the table but with less deviation from the vertical than the mst-mentioned links, the said links constituting the sole support of the table from the supporting structure, said second mentioned links being longer than said mst-mentioned links between pivot centres, an eccentric having its strap linked to the table and its sheave driven by a source of power, and means for adjusting the position of the eccentric sheave to vary the slope of the table.
G. E. SHAWCROSS.
REFERENCES CI'rE The following references are of record in the le of this patent:
UNITED STATES PATENTS
US626807A 1944-11-16 1945-11-05 Reciprocating mechanism for inclined mineral separating pneumatic tables Expired - Lifetime US2427423A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2928545A (en) * 1956-07-16 1960-03-15 Arthur R Forsberg Gravity separator
US3444996A (en) * 1966-03-14 1969-05-20 Nat Res Dev Dry separation of mixtures of solid materials
US3693794A (en) * 1968-04-17 1972-09-26 Buehler Ag Geb Method and apparatus for separating granular goods
US4278537A (en) * 1979-03-27 1981-07-14 Alpine Aktiengesellschaft Apparatus for separating heavy solids and light solids from a mixture thereof
US4793918A (en) * 1986-07-08 1988-12-27 Oliver Manufacturing Co., Inc. Gravity separator
US5087351A (en) * 1990-08-02 1992-02-11 Golden Peanut Company, A Georgia General Partnership Fluidized bed peanut sorter
US8770412B2 (en) * 2012-12-07 2014-07-08 Gerald Lee Miller Gravimetric mineral processing device and method for its use

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1579993A (en) * 1924-01-30 1926-04-06 Prod A Flenu Sa Des Apparatus for sorting granular materials of different specific gravities
GB332291A (en) * 1929-05-27 1930-07-24 Colin William Higham Holmes Improvements in and relating to the separation of dry materials
US1786739A (en) * 1922-06-07 1930-12-30 Peale Davis Company Method and mechanism for separating divided materials
GB439972A (en) * 1934-06-18 1935-12-18 Ivor Lloyd Bramwell Improvements in and relating to the separation of dry materials
US2063533A (en) * 1933-06-10 1936-12-08 Vissac Gustave Andre Air cleaner and classifier for fine coals
US2204379A (en) * 1935-12-20 1940-06-11 Gustave A Overstrom Vibrating screen structure
US2348344A (en) * 1941-11-25 1944-05-09 Birtley Co Ltd Process of separating intermixed divided materials

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1786739A (en) * 1922-06-07 1930-12-30 Peale Davis Company Method and mechanism for separating divided materials
US1579993A (en) * 1924-01-30 1926-04-06 Prod A Flenu Sa Des Apparatus for sorting granular materials of different specific gravities
GB332291A (en) * 1929-05-27 1930-07-24 Colin William Higham Holmes Improvements in and relating to the separation of dry materials
US2063533A (en) * 1933-06-10 1936-12-08 Vissac Gustave Andre Air cleaner and classifier for fine coals
GB439972A (en) * 1934-06-18 1935-12-18 Ivor Lloyd Bramwell Improvements in and relating to the separation of dry materials
US2204379A (en) * 1935-12-20 1940-06-11 Gustave A Overstrom Vibrating screen structure
US2348344A (en) * 1941-11-25 1944-05-09 Birtley Co Ltd Process of separating intermixed divided materials

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2928545A (en) * 1956-07-16 1960-03-15 Arthur R Forsberg Gravity separator
US3444996A (en) * 1966-03-14 1969-05-20 Nat Res Dev Dry separation of mixtures of solid materials
US3693794A (en) * 1968-04-17 1972-09-26 Buehler Ag Geb Method and apparatus for separating granular goods
US4278537A (en) * 1979-03-27 1981-07-14 Alpine Aktiengesellschaft Apparatus for separating heavy solids and light solids from a mixture thereof
US4793918A (en) * 1986-07-08 1988-12-27 Oliver Manufacturing Co., Inc. Gravity separator
US5087351A (en) * 1990-08-02 1992-02-11 Golden Peanut Company, A Georgia General Partnership Fluidized bed peanut sorter
US8770412B2 (en) * 2012-12-07 2014-07-08 Gerald Lee Miller Gravimetric mineral processing device and method for its use

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