US3866754A - Pellet segregation and apparatus therefor - Google Patents

Pellet segregation and apparatus therefor Download PDF

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US3866754A
US3866754A US308309A US30830972A US3866754A US 3866754 A US3866754 A US 3866754A US 308309 A US308309 A US 308309A US 30830972 A US30830972 A US 30830972A US 3866754 A US3866754 A US 3866754A
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pellets
reservoir
conical surface
periphery
pellet
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US308309A
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David Evans
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Huntington Alloys Corp
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International Nickel Co Inc
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • C22B5/20Dry methods smelting of sulfides or formation of mattes from metal carbonyls
    • 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
    • B03B1/00Conditioning for facilitating separation by altering physical properties of the matter to be treated
    • B03B1/02Preparatory heating
    • 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
    • B07B13/00Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
    • 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
    • B07B13/00Grading or sorting solid materials by dry methods, not otherwise provided for; Sorting articles otherwise than by indirectly controlled devices
    • B07B13/003Separation of articles by differences in their geometrical form or by difference in their physical properties, e.g. elasticity, compressibility, hardness

Definitions

  • the present invention relates to pellet size classification and apparatus therefor, and more particularly to a method and apparatus for classifying carbonyl metallic pellets in a carbonyl decomposer.
  • Deposition of nickel on the pellets causes them to increase in size, and at any time the circulating charge includes pellets of all sizes ranging from minute seed particles to fully-grown pellets of the required product size, say inch diameter.
  • the circulating pellets are allowed to fall on to the top of a conical pile of pellets at the top of the preheater. Oversize pellets tend to roll down the surface of this cone and thence down a chute and over a screen to a product vessel, while the remaining smaller pellets, forming the bulk of the feed,,lodge preferentially on the surface of the pile. While the pile is being built up in this way at the top, pellets from the bottom pass downwards into the preheater,.so that the height of the pile remains substantially constant and its surface remains in substantially the same position. Any undersize pellets that have been carried over with the oversize pellets pass through the screen and are put back into circulation.
  • Another object of the invention is to provide improved apparatus for classifying pellets.
  • the present invention contemplates a method for classifying pellets.
  • a reservoir having a continuous periphery is filled with pellets so that the pellets form a pile having a conical surface, apex upwards.
  • a mixture of pellets having oversized and undersized pellets is fed to the conical surface in the vicinity of the apex so that the mixture of pellets can flow over the conical surface.
  • Pellets are removed from the bottom of the reservoir in a uniform manner so as not to disturb the conical surface and at a rate to maintain the pile at a substantially constant height.
  • the rate of flow of the mixture of pellets over the surface is controlled so that the oversized pellets retain sufficient energy to flow over the entire conical surface and over the reservoir periphery while the undersized pellets be come entrapped in interstices of the conical surface.
  • a conical pile of pellets is formed between a horizontal circular dam and a vertically adjustable circular feed nozzle mounted centrally above the dam, and a flexible curtain is mounted with its lower edge touching the surface of the cone between the feed nozzle and the dam.
  • a flexible curtain is mounted with its lower edge touching the surface of the cone between the feed nozzle and the dam.
  • the dam forms the upper rim of a cylindrical pellet reservoir from which the pellets pass into the preheater, and the pellets overflowing the darn fall on to one or more helical chutes around the outside of the reservoir leading to an outlet pipe or pipes to the screen and product vessel.
  • a cylindrical pellet reservoir 1 is mounted on top of a pellet preheater 2, of which only the top is shown, which in turn is mounted on top of the reaction chamber of a carbonyl decomposer.
  • the reservoir carries around its upper edge a circular darn 3 which can be adjusted so as to be accurately horizontal.
  • a discharge nozzle 4 Centrally above the dam is mounted a discharge nozzle 4, the height of which can be varied by means of three adjusting screws 5 (only one being shown) and a flexible circular curtain 6 is mounted on the bottom of a cylindrical holder 7 surrounding the nozzle 4.
  • twin chutes in the form of helices 8 of opposite hand leading down from the level of the dam to an outlet pipe 10 leading to a screen (not shown).
  • the inclination of these helices should be at least 30 to the horizontal so that pellets can slide as well as roll down them.
  • Nickel pellets passing downwards from the reservoir 1 through the preheater 2 and the reaction chamber are then collected and raised by an elevator (not shown) to the top ofa chute 11 from which they pass through the nozzle on to a conical pile of pellets that builds up between the nozzle 4 and the dam 3.
  • the pile builds up at the natural angle of repose of the pellets, and it is important to adjust the height of the nozzle 4 so that pellets may flow freely from it on to the pile. If the nozzle is too low, the pile will build up around it and the flow of pellets will be impeded and may soon be stopped. If the nozzle is too high, the pellets fall with excessive force on to the pile and cause excessive disturbance of the pile, resulting in the larger pellets becoming embedded in the surface instead of rolling freely down the pile, and undersize pellets being forced past the curtain and rolling on to overflow the dam.
  • the nozzle is just clear of the surface of the pile. Most of the pellets leaving the nozzle then begin to roll down the outside of the pile, but small pellets lodge in the interstices or indentations in the surface while larger ones roll over the indentations to reach the dam, where they overflow and fall on to one of the helices and thence pass to the outlet pipe 9.
  • the nozzle 4 should also be accurately centered above the dam and have its lower edge horizontal, so that the pellets issuing from it are distributed uniformly around the pile.
  • the curtain 6 in contact with the surface of the pile allows pellets to roll past and down the surface of the pile but intercepts any pellets that may bounce off the upper part despite all these precautions. In passing the curtain the pellets are slowed down, thus improving the chances of their lodging in a suitable indentation and thereby making segregation more efficient.
  • the material of the curtain should of course be sufficiently flexible to allow pellets to roll past, and it must resist relatively high temperatures, since the temperature of the pellets in the pile is about 180C.
  • a suitable material is polyester fiber cloth.
  • at least the lower part of the curtain is divided vertically into strips, and it is also advantageous to construct the curtain in two layers each of which is divided in this way so that the strips in the two layers overlap.
  • thermocouple 12 is mounted in the top of the casing, which is also provided with a sight-glass 13 through which the surface of the pile can be observed.
  • the height of the reservoir 1 may if desired be reduced by using two or more pairs of helical chutes in place of the single pair in the example, with a correspondingly increased number of outlet pipes.
  • a pellet classifier comprising:
  • feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface;
  • adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow;
  • a pellet classifier as set forth in claim 1 with at least two energy absorbing curtains having slits in the lowermost portions and mounted around the nozzle with the lowermost portion of at least one curtain overlapping the slits in the other curtain.
  • a pellet classifier comprising:
  • feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface;
  • c. means for adjusting the height of the nozzle to control the flow of pellets to the conical surface
  • adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow;
  • a pellet classifier comprising:
  • feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upward, so that oversized pellets can flow over the conical surface and over the reservoir periphery while unthe conical surface to thereby increase the chance dersized pellets become lodged in interstices in the of lodging undersized pellets in the interstices in conical surface; the conical surface; and c. at least one energy absorbing flexible curtain surd. outlet means adapted for removing pellets from rounding and extending downward from the nozzle 5 the reservoir to maintain the height of the pellet and adapted for contacting the conical surface of pile substantially constant. said pellet pile and slowing the flow of pellets down

Abstract

Fully-grown nickel pellets are separated from the circulating load in a pellet carbonyl decomposer by discharging the load on to a conical pile of pellets formed between a horizontal circular dam and a circular feed nozzle, a flexible curtain being mounted with its lower edge touching the surface of the pile. The fullygrown pellets roll preferentially down the pile and overflow the dam with some undersize pellets, which are separated by screening and returned to circulation.

Description

United States Patent 1191 Evans 1 1 Feb. 18, 1975 1 PELLET SEGREGATION AND APPARATUS [56] References Cited THEREFOR UNITED STATES PATENTS [75] Inventor: David Evans, Swansea, Wales 161,840 4/1875 Thomas 209/118 3,414,125 121968 C'k 209112 X [73] Assignee: The International Nickel Company, d Ora Inc, New York, NY. Primary Examiner-Allen N. Knowles 22 Pl d: No 21, 1972 1 16 v 57 ABSTRACT [21] Appl. No.: 308,309
Related US. Application Data Fully-grown nickel pellets are separated from the cir- [62] Division of Ser. No. 156,288,1une 24, 1971, Pat. No. culatmg load in a Pellet Carbonyl decomposer by 3,722464 charging the load on to a conical pile of pellets formed 1 between a horizontal circular dam and a circular feed 30 Foreign Application Priority Data nozzle, a flexible curtain being mounted with its lower July 7 1970 Great Britain 32963/70 edge touching the surface of the pile. The fully-grown pellets roll preferentially down the pile and overflow [52] us CL 209/73 209/115 the dam with some undersize pellets, which are sepa- 51 Int. Cl. D07c ,13671 13/10 rated by Screening and returned to circulation- [58] Field of Search 209/87, 116, 117, 118,
5 Claims, 1 Drawing Figure PELLET SEGREGATION AND APPARATUS THEREFOR The present application is a division of my application Ser. No. l56,288 filed June 24, 1971, now US. Pat. No. 3,722,464.
The present invention relates to pellet size classification and apparatus therefor, and more particularly to a method and apparatus for classifying carbonyl metallic pellets in a carbonyl decomposer.
In the Mond process for producing nickel through the formation and subsequent decomposition of nickel carbonyl, as described in British Pat. No. 620,287, a gas containing nickel carbonyl is brought into contact in a decomposer with nickel pellets that have been preheated to a temperature above the decomposition temperature of the carbonyl. The nickel is deposited on the pellets as the pellets pass downwards through the reaction chamber of the decomposer in counter-current to a stream of carbonyl-containing gas, and the pellets leaving the bottom of the reaction chamber are recirculated through the preheater and then back through the reaction chamber.
Deposition of nickel on the pellets causes them to increase in size, and at any time the circulating charge includes pellets of all sizes ranging from minute seed particles to fully-grown pellets of the required product size, say inch diameter.
In order to separate the pellets that have reached or exceeded a predetermined size, which will be referred to as oversize pellets, the circulating pellets are allowed to fall on to the top of a conical pile of pellets at the top of the preheater. Oversize pellets tend to roll down the surface of this cone and thence down a chute and over a screen to a product vessel, while the remaining smaller pellets, forming the bulk of the feed,,lodge preferentially on the surface of the pile. While the pile is being built up in this way at the top, pellets from the bottom pass downwards into the preheater,.so that the height of the pile remains substantially constant and its surface remains in substantially the same position. Any undersize pellets that have been carried over with the oversize pellets pass through the screen and are put back into circulation.
It has now been discovered that the aforedescribed method and apparatus for classifying carbonyl metallic pellets can be improved to provide a cleaner separation between undersized and oversized pellets.
It is an object of the present invention to provide a method for classifying pellets.
Another object of the invention is to provide improved apparatus for classifying pellets.
Other objects and advantages will become apparent from the following description taken in conjunction with the accompanying FIGURE in which a preferred embodiment of the pellet classifier in accordance with the present invention is shown in sectional elevation.
Generally speaking, the present invention contemplates a method for classifying pellets. A reservoir having a continuous periphery is filled with pellets so that the pellets form a pile having a conical surface, apex upwards. A mixture of pellets having oversized and undersized pellets is fed to the conical surface in the vicinity of the apex so that the mixture of pellets can flow over the conical surface. Pellets are removed from the bottom of the reservoir in a uniform manner so as not to disturb the conical surface and at a rate to maintain the pile at a substantially constant height. The rate of flow of the mixture of pellets over the surface is controlled so that the oversized pellets retain sufficient energy to flow over the entire conical surface and over the reservoir periphery while the undersized pellets be come entrapped in interstices of the conical surface.
Advantageously, a conical pile of pellets is formed between a horizontal circular dam and a vertically adjustable circular feed nozzle mounted centrally above the dam, and a flexible curtain is mounted with its lower edge touching the surface of the cone between the feed nozzle and the dam. To ensure that the pellets overflow the dam uniformly, it is important that the top of the dam is accurately horizontal, and advantageously it is also adjustable for this purpose. The outside edge of the darn should preferably be chamfered.
Advantageously the dam forms the upper rim of a cylindrical pellet reservoir from which the pellets pass into the preheater, and the pellets overflowing the darn fall on to one or more helical chutes around the outside of the reservoir leading to an outlet pipe or pipes to the screen and product vessel.
Referring now to the FIGURE, a cylindrical pellet reservoir 1 is mounted on top of a pellet preheater 2, of which only the top is shown, which in turn is mounted on top of the reaction chamber of a carbonyl decomposer. The reservoir carries around its upper edge a circular darn 3 which can be adjusted so as to be accurately horizontal. Centrally above the dam is mounted a discharge nozzle 4, the height of which can be varied by means of three adjusting screws 5 (only one being shown) and a flexible circular curtain 6 is mounted on the bottom of a cylindrical holder 7 surrounding the nozzle 4. Around the outside of the reservoir 1, between the reservoir and an outer casing 9, are twin chutes in the form of helices 8 of opposite hand leading down from the level of the dam to an outlet pipe 10 leading to a screen (not shown). In order to avoid blockages the inclination of these helices should be at least 30 to the horizontal so that pellets can slide as well as roll down them.
Nickel pellets passing downwards from the reservoir 1 through the preheater 2 and the reaction chamber are then collected and raised by an elevator (not shown) to the top ofa chute 11 from which they pass through the nozzle on to a conical pile of pellets that builds up between the nozzle 4 and the dam 3.
The pile builds up at the natural angle of repose of the pellets, and it is important to adjust the height of the nozzle 4 so that pellets may flow freely from it on to the pile. If the nozzle is too low, the pile will build up around it and the flow of pellets will be impeded and may soon be stopped. If the nozzle is too high, the pellets fall with excessive force on to the pile and cause excessive disturbance of the pile, resulting in the larger pellets becoming embedded in the surface instead of rolling freely down the pile, and undersize pellets being forced past the curtain and rolling on to overflow the dam.
Ideally the nozzle is just clear of the surface of the pile. Most of the pellets leaving the nozzle then begin to roll down the outside of the pile, but small pellets lodge in the interstices or indentations in the surface while larger ones roll over the indentations to reach the dam, where they overflow and fall on to one of the helices and thence pass to the outlet pipe 9.
The nozzle 4 should also be accurately centered above the dam and have its lower edge horizontal, so that the pellets issuing from it are distributed uniformly around the pile.
Further measures which help to reduce the energy of the pellets reaching the pile are to incline the chute 11 to the horizontal at the smallest angle consistent with maintaining a steady flow of pellets, and to provide one or more baffles 14 in the feed pipe or the upper part of the nozzle, or both.
The curtain 6 in contact with the surface of the pile allows pellets to roll past and down the surface of the pile but intercepts any pellets that may bounce off the upper part despite all these precautions. In passing the curtain the pellets are slowed down, thus improving the chances of their lodging in a suitable indentation and thereby making segregation more efficient. The material of the curtain should of course be sufficiently flexible to allow pellets to roll past, and it must resist relatively high temperatures, since the temperature of the pellets in the pile is about 180C. A suitable material is polyester fiber cloth. Advantageously at least the lower part of the curtain is divided vertically into strips, and it is also advantageous to construct the curtain in two layers each of which is divided in this way so that the strips in the two layers overlap.
To monitor the temperature of the pellets a thermocouple 12 is mounted in the top of the casing, which is also provided with a sight-glass 13 through which the surface of the pile can be observed.
The height of the reservoir 1 may if desired be reduced by using two or more pairs of helical chutes in place of the single pair in the example, with a correspondingly increased number of outlet pipes.
It will be appreciated that in a single passage of the whole charge of pellets circulating through the decomposer only a proportion of the oversize pellets will be separated, while the remainder become incorporated in the pile and are recirculated. Furthermore, although the oversize pellets that preferentially overlow the dam are inevitably accompanied by a small number of undersize pellets, these can readily be separated from the oversize pellets by screening and returning them to circulation, whereas it would be completely impractical to carry out the separation by continuously screening the whole circulating load of pellets.
Although the present invention has been described in conjunction with preferred embodiments, it is to be understood that modifications and variations may be resorted to without departing from the spirit and scope of the invention, as those skilled in the art will readily understand. Such modifications and variations are considered to be within the purview and scope of the invention and appended claims.
I claim:
1. A pellet classifier comprising:
a. an open-topped reservoir having a continuous periphery;
b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface;
c. at least one energy absorbing flexible curtain surrounding the nozzle, between the feeding means and the reservoir periphery for slowing the flow of pellets down the conical surface, thereby increasing the chance of lodging undersized pellets in the interstices in the conical surface;
d. a plurality of outlet means in the bottom of the reservoir for removing pellets from the reservoir to maintain the height of the pellet pile substantially constant;
e. adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow;
f. collecting means surrounding the reservoir periphery for collecting pellets overflowing the reservoir periphery; and
g. a screen for screening pellets overflowing the reservoir periphery into oversized and undersized pellets and means for recirculating the undersized pellets to the feeding means.
2. A pellet classifier as set forth in claim 1 with at least two energy absorbing curtains having slits in the lowermost portions and mounted around the nozzle with the lowermost portion of at least one curtain overlapping the slits in the other curtain.
3. A pellet classifier as set forth in claim 1 wherein the curtain is made of a polyester.
4. A pellet classifier comprising:
a. an open-topped reservoir having a continuous periphery;
b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface;
c. means for adjusting the height of the nozzle to control the flow of pellets to the conical surface;
(1. energy absorbing means between the feeding means and the reservoir periphery for slowing the flow of pellets down the conical surface thereby increasing the chance of lodging undersized pellets in the interstices in the conical surface;
e. a plurality of outlet means in the bottom of the reservoir for removing pellets from the reservoir to maintain the height of the pellet pile substantially constant;
f. adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow;
g. collecting means surrounding the reservoir periphery for collecting pellets overflowing the reservoir periphery; and
h. a screen for screening pellets overflowing the reservoir periphery into oversized and undersized pellets and means for recirculating the undersized pellets to the feeding means.
5. A pellet classifier comprising:
a. an open-topped reservoir having a continuous periphery;
b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upward, so that oversized pellets can flow over the conical surface and over the reservoir periphery while unthe conical surface to thereby increase the chance dersized pellets become lodged in interstices in the of lodging undersized pellets in the interstices in conical surface; the conical surface; and c. at least one energy absorbing flexible curtain surd. outlet means adapted for removing pellets from rounding and extending downward from the nozzle 5 the reservoir to maintain the height of the pellet and adapted for contacting the conical surface of pile substantially constant. said pellet pile and slowing the flow of pellets down

Claims (5)

1. A pellet classifier comprising: a. an open-topped reservoir having a continuous periphery; b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface; c. at least one energy absorbing flexible curtain surrounding the nozzle, between the feeding means and the reservoir periphery for slowing the flow of pellets down the conical surface, thereby increasing the chance of lodging undersized pellets in the interstices in the conical surface; d. a plurality of outlet means in the bottom of the reservoir for removing pellets from the reservoir to maintain the height of the pellet pile substantially constant; e. adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow; f. collecting means surrounding the reservoir periphery for collecting pellets overflowing the reservoir periphery; and g. a screen for screening pellets overflowing the reservoir periphery into oversized and undersized pellets and meanS for recirculating the undersized pellets to the feeding means.
2. A pellet classifier as set forth in claim 1 with at least two energy absorbing curtains having slits in the lowermost portions and mounted around the nozzle with the lowermost portion of at least one curtain overlapping the slits in the other curtain.
3. A pellet classifier as set forth in claim 1 wherein the curtain is made of a polyester.
4. A pellet classifier comprising: a. an open-topped reservoir having a continuous periphery; b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upwards, so that oversized pellets flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface; c. means for adjusting the height of the nozzle to control the flow of pellets to the conical surface; d. energy absorbing means between the feeding means and the reservoir periphery for slowing the flow of pellets down the conical surface thereby increasing the chance of lodging undersized pellets in the interstices in the conical surface; e. a plurality of outlet means in the bottom of the reservoir for removing pellets from the reservoir to maintain the height of the pellet pile substantially constant; f. adjustable dam means mounted on the reservoir periphery for maintaining a substantially horizontal dam over which oversized pellets overflow; g. collecting means surrounding the reservoir periphery for collecting pellets overflowing the reservoir periphery; and h. a screen for screening pellets overflowing the reservoir periphery into oversized and undersized pellets and means for recirculating the undersized pellets to the feeding means.
5. A pellet classifier comprising: a. an open-topped reservoir having a continuous periphery; b. feeding means including a nozzle for feeding a mixture of oversized and undersized pellets to the reservoir center to fill the reservoir and for forming a pellet pile having a conical surface, apex upward, so that oversized pellets can flow over the conical surface and over the reservoir periphery while undersized pellets become lodged in interstices in the conical surface; c. at least one energy absorbing flexible curtain surrounding and extending downward from the nozzle and adapted for contacting the conical surface of said pellet pile and slowing the flow of pellets down the conical surface to thereby increase the chance of lodging undersized pellets in the interstices in the conical surface; and d. outlet means adapted for removing pellets from the reservoir to maintain the height of the pellet pile substantially constant.
US308309A 1970-07-07 1972-11-21 Pellet segregation and apparatus therefor Expired - Lifetime US3866754A (en)

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US15628871A 1971-06-24 1971-06-24
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3944075A (en) * 1973-04-23 1976-03-16 Tote Bulk Handling, Inc. Method of preparing and separating mixtures of moldable plastic and additive agents
US20080083565A1 (en) * 2005-02-28 2008-04-10 Roussy Raymond J Method of geothermal loop installation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US161840A (en) * 1875-04-06 Improvement in separating refuse from coal
US3414125A (en) * 1967-04-04 1968-12-03 Tazewell Machine Works Inc Apparatus for separating foundry sand

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US161840A (en) * 1875-04-06 Improvement in separating refuse from coal
US3414125A (en) * 1967-04-04 1968-12-03 Tazewell Machine Works Inc Apparatus for separating foundry sand

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3944075A (en) * 1973-04-23 1976-03-16 Tote Bulk Handling, Inc. Method of preparing and separating mixtures of moldable plastic and additive agents
US20080083565A1 (en) * 2005-02-28 2008-04-10 Roussy Raymond J Method of geothermal loop installation

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