US3923210A - Automatic discharge regulator - Google Patents

Automatic discharge regulator Download PDF

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Publication number
US3923210A
US3923210A US44450874A US3923210A US 3923210 A US3923210 A US 3923210A US 44450874 A US44450874 A US 44450874A US 3923210 A US3923210 A US 3923210A
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sheets
sleeve
solid particles
discharge
end
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Expired - Lifetime
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Lawrence Donald Alexan Jackson
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LINATEX CANADA Inc
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LAWJACK EQUIPMENT 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
    • B03B11/00Feed or discharge devices integral with washing or wet-separating equipment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/15Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with swinging flaps or revolving sluices; Sluices; Check-valves

Abstract

An automatic discharge regulator is disclosed for a separator or classifier to regulate the discharge of solid particles conveyed in a slurry. Hydrocyclones are frequently used for separating solid particulate material from liquids, but if an open solid discharge exit is provided, the regulation of separation cannot be controlled unless there is a constant flow of solid material in the slurry. The regulator has two sheets of flexible material in side by side relationship held together at two opposing edges to form a sleeve. One end of the sleeve fits over the exit from the separator. The sleeve has reinforcing pads of flexible material which are positioned on the outside surfaces of the sheets of flexible material and keep the other end of the sleeve closed when no solid material passes therethrough. A method of regulating the discharge of solid materials from such a discharge sleeve attached to the exit spigot of a hydrocyclone is disclosed by controlling the vacuum in the hydrocyclone.

Description

United States Patent 1191 1111 3,923,210 Jackson 1 Dec. 2, 1975 AUTOMATIC DISCHARGE REGULATOR [75] Inventor: Lawrence Donald Alexander Pnmary b'mminer s tanley Tollberg Jackson, Montreal, Canada Attorney, Agent, or Firm-Larson, Taylor & Hinds [73] Assignee: Lawjack Equipment Limited, [57] ABSTRACT Montreal Canada An automatic discharge regulator is disclosed for a 22 il d; 21 1974 separator or classifier to regulate the discharge of solid particles conveyed in a slurry. Hydrocyclones are [2]] Appl' NO; 444508 frequently used for separating solid particulate material from liquids, but if an open solid discharge exit is [30] Foreign Application priority Data provided, the regulation of separation cannot be controlled unless there is a constant flow of solid material l' b.22. 1973 U t d K d 8807 73 e m e mg Om in the slurry. The regulator has two sheets of flexible [52] U S CL H 222/494 222/529 material in side by side relationship held together at [5 H Cl 2 B65D 37/00 two opposing edges to form a sleeve. One end of the [58] Field of i i 494 107 sleeve fits over the exit from the separator. The sleeve 6 has reinforcing pads of flexible material which are positioned on the outside surfaces of the sheets of flexi- [56] References Cited ble material and keep the other end of the sleeve UNITED STATES PATENTS closed when no solid material passes therethrough. A method of regulating the discharge of solid materials 1,964,860 7/1934 Rabe ct a1 222/491 X f Such a discharge Sleeve attached to the i n spigot of a hydrocyclone is disclosed by controlling urp y 3,610,477 10 1971 Herzig 222/213 the Vacuum m the hydrocyclone 3,815,794 6/1974 Carlisle 222/491 8 Claims, 4 Drawing Figures Sheet 1 of 2 US. Patent Dec. 2, 1975 US. Patent D'e.2,1975 sh eetzom 3,923,210

AUTOMATIC DISCHARGE REGULATOR This invention relates to hydrocyclone classifiers or centrifugal separators and more particularly to a device for controlling the density of discharging particulate material separated from a fluid in a classifier or separator.

I-Iydrocyclones are generally used for separating solids in the form of fine particulate material from liquids. They are primarily used in both the mining'and aggregate industry. One use of a hydrocyclone is in systems where a pipe line is used for transporting solids in a liquid suspension. In this system, solids in the form of powder or fines such as sand, coal dust, clay, mineral ore, etc., are deposited into a pipe line having a liquid, usually water, flowing therein. The water acts as a carrier and conveys the solid particles along the pipe line. Provided velocity of the water in the pipe line is maintained above a minimum level, the particles do not settle and are kept in suspension throughout the length of the pipe. The hydrocyclone is generally a centrifugal unit. The liquid and solid particles enter the hydrocyclone tangentially and are subjected to a centrifugal force which forces the coarser and higher density material towards the outside wall of the hydrocyclone. The larger solid particles work their way to the apex of the hydrocyclone where they leave the hydrocyclone through an exit. The remaining water and other fine particles are removed through an overflow at the top centre of the unit.

In the metallurgical field, a hydrocyclone is used to classify fine particles according to their size and/or density. For instance a crushed ore is conveyed in water to a hydrocyclone where the heavy and/or coarse particles separated from the fine and/or light rock particles and water. The heavy and/or coarse particles are forced out to the wall of the classifier by centrifugal force, and these travel along the conical wall towards the apex where they are finally discharged through a spigot. The fine and/or light particles are removed with most of the water through an overflow in the centre of the hydrocyclone. The control of separation depends on the size of the hydrocyclone, the speed and quantity of the water entering the hydrocyclone inlet, and the amount of vacuum in the hydrocyclone. Such a system is used for dewatering sand and gravel conveyed in a water pipe line. A hydrocyclone is also used for classifying ground ores into products requiring further processing. Such a product is one requiring further grinding, and then processing through a hydrocyclone again. Another use of hydrocyclones is desliming or dewatering mineral wastes or tailings to improve consolidation properties. Another use of a hydrocyclone is for separating fine clay from concrete sand. In this latter process, the bulk of the water and the finer size clay particles flow to the overflow while the larger solid particles of sand with a reduced amount of water are forced to the wall of the hydrocyclone and then discharged through a spigot at the apex.

The control of a hydrocyclone depends on the size and proportion of the unit, the quantity of solids and liquid flowing into the unit, the ratio of water to solids and pressure of the fluid solids mixture entering the hydrocyclone inlet in the form of a slurry feed. The control is also effected by the size of the overflow and apex opening, and the amount of vacuum in the system. One of the common problems with the hydrocyclones of today, is to regulate the density of the discharge of solid materials. If there is always a constant flow of solid particles in the hydrocyclone feed, then the apex spigot may be adjusted to a particular size opening and the unit discharges a relatively constant output. However, in the majority of cases, the amount of solids in the slurry feed varies. The flow of liquid is usually constant, but batches of solid particles are deposited into the feed pipe line at frequent intervals. In this situation it is necessary to continually adjust the apex spigot, otherwise excess water tends to escape through the spigot producing a material which may be unsuitable for further processing.

It is an object of the present invention to provide a simple discharge regulator for automatically opening and releasing solid particles from a hydrocyclone, and closing when insufficient solid particles are present thus preventing liquid flushing out of the discharge regulator.

It is a further object of the present invention to provide a method of requlating the discharge through an apex spigot of a hydrocyclone so as to control the solids to liquid ratio.

With these and other objects in view, there is provided an automatic discharge regulator for a discharge exit from a separator or classifier comprising two sheets of flexible material in side by side relationship held together at two opposing edges forming a sleeve, a first end of the sleeve adapted to mate with the discharge exit, a reinforcing pad of flexible material positioned on the outer surface of each of the two sheets such that when the first end of the sleeve mates with the discharge exit, the second end of the sleeve remains closed with the two sheets touching, the flexible material having sufiicient resilience to allow the second end of the sleeve to be opened and pass solid particles therethrough.

There is also provided in a method of regulating the discharge of solid materials from a separator through an exit including the steps of controlling the velocity and flow of solid particles conveyed in a fluid suspension to a separator, separating at least a portion of the solid particles from the fluid and removing the majority of the fluid and any particles left therein, the improvement comprising passing the portion of solid particles through a sleeve of resilient material attached to the exit, the resiliency of the sleeve forcing it closed when no solid particles pass therethrough, and varying the vacuum inside the separator to regulate the percent of solid particles separating from the fluid.

With the foregoing objects and features in view and such other objects and features as may become apparent as this specification proceeds, the invention will be understood from the following description of a preferred form thereof taken in conjunction with the accompanying drawings, which illustrate embodiments of the invention.

FIG. 1 shows a schematic diagram of a hydrocyclone with an automatic discharge regulator of the present invention.

FIG. 2 shows a side elevation of one type of an automatic discharge regulator according to the present invention, mounted on a discharge exit of a separator or classifier.

FIG. 3 shows an end view of the automatic discharge regulator shown in FIG. 2.

FIG. 4 shows a cross-section through the automatic discharge regulator shown in FIG. 2 at section 4-4.

Referring now to the drawings, in FIG. 1 an automatic discharge control system is shown with a hydrocyclone 10, a tangential or sweep inlet 11 entering the hydrocyclone l0, and an overflow pipe 12 leading through a flange connection to a siphon leg 13. An air bleed hose 14 attached to the siphon leg 13 has a vacuum control valve 15 which is adjustable to allow bleed air into the siphon leg 13 so as to control the vacuum inside the hydrocyclone 10, thereby controlling the opening and closing of an automatic discharge regulator 16 attached to the apex spigot 17 of the hydrocyclone 10. The vacuum may also be controlled by varying the elevation of the end of the siphon leg 13.

The regulator shown in FIGS. 2, 3 and 4 comprises two flat rectangular sheets 20 of resilient material. This material is preferably synthetic or natural rubber and is abrasion resistant to stop wear from granular particles such as sand passing between the two sheets 20. The material is sufficiently flexible to allow the two sheets 20 to open, but has a configuration which always returns the two sheets to their original flat shape thus closing the regulator. Two strips 21 down opposite edges of the sheets 20 are adhered together preferably by an adhesive or alternatively by clips or other means, thus forming a passageway 22 between the two sheets 20. The regulator fits onto the round exit sleeve 23 at the exit of a separator or classifier such as a hydrocyclone similar to that shown in FIG. 1 and is attached by a circular clip 24 which surrounds a collar 25 of the regulator. The circular clip 24 has a nut and bolt 26 which permits its removal, thus permitting a new regulator to be fitted when necessary. The means by which the clip 24 is held around the collar 25 may be by screw clamps, spring clamps or other well known means. The enntrance to the passageway 22 between the sheets 20 is circular. However, the two sheets 20 come together into their flattened position below the exit 23 to form a seal. When no particulate material is passing through the exit sleeve 23, the passageway 22 is closed.

The construction of the regulator is adapted to control the closure. On the sheets 20 are two circular pads 27 substantially in the center and on the outside surface of each sheet 20 made from the same material as the sheets 20 and firmly adhered to the outside surface of each sheet preferably by an adhesive. A reinforcing strip 28 extending half way down each sheet 20 is attached to the outside of the sheet preferably by an adhesive. The reinforcing strip 28 has a cut out 29 to allow the reinforcing pad 27 to be carefully placed in the centre of each sheet 20. The reinforcing strip 28 and the sheet are attached together at their top end to form the collar 25. The collar 25 comprises an additional strip 30 of resilient material similar to the material used for the sheet 20 surrounding the inside and outside of the regulator and extending across the top. This gives additional reinforcement to the regulator and also aids at the point where the sheets 20 join to form a protective collar and stop leakage of liquid or air therethrough.

As may be seen in FIGS. 3 and 4, the reinforcing pads 27 which aid in returning the sheets 20 to their original flattened state also surprisingly cause the ends of the sheets 20 to curve away in a tail 31. This configuration allows the two sheets to touch and seal more definitely.

In operation the mixture of liquid and solid particles enter the hydrocyclone 10 through the inlet 11 and primarily due to centrifugal force, the coarse particles separate and are forced to the conical walls of the hydrocyclone 10. From this position the particles travel along the walls of the hydrocyclone 10 to the automatic discharge regulator 16 attached to the apex spigot 17. The vacuum from the siphon leg 13 draws the majority of the liquid and any fine particles that remain therein to the overflow pipe 12. The control is by means of the vacuum control valve 15 on the air bleed hose 14. The remaining coarse solid particles travel to the regulator and because they are denser and heavier than the liquid, they force the two sheets 20 apart and pass through the passageway 22. It has been found that with this type of regulator the liquid content of the apex discharge can be dependably regulated as desired. One means of controlling the ratio or mixture of solids and liquids flowing through this regulator is carried out by means of the vacuum control valve 15. Thus if too much liquid is discharging through the regulator with the solid particles then the vacuum inside the hydrocyclone is increased by reducing the air bled into the siphon leg 13. If too many coarse particles are discharging through the overflow pipe 12 then the vacuum is decreased by increasing the air bled into the siphon leg 13. When the particles are no longer conveyed into the hydrocyclone 10 while the flow of liquid still continues, then the passageway 22 closes and the liquid discharges through the overflow pipe 12.

In the case of hydrocyclone being utilized as a classifier, the proportion of solids discharging through the apex spigot may be regulated by a number of different ways. First of all there is a control on the percentage of solids that are conveyed by the liquid, secondly the volume of liquid entering the hydrocyclone may be controlled, thirdly the pressure, hence the velocity of liquid can also be controlled and fourthly the preferred form of control is the amount of vacuum in the system. Other possible variations include the inlet diameter together with the diameter of the overflow l2 and the apex spigot 17. The solids can generally be classified as to size or density. However, when size is mentioned one must also be aware of the shape of the particles, for instance, flaky material with a large surface area tends to stay with the liquid and is more difficult to separate than coarse granular particles. The adjustment of the regulator is generally made on site, adjusting the vacuum flow and velocity of liquid entering the hydrocyclone such that there is barely any liquid discharging from the regulator when the unit is operating only on a liquid, then by slowly adding solid particles to the liquid entering the hydrocyclone and again further adjustment made to the vacuum so that a minimum of liquid discharges with the solid particles. If it is found that too many coarse particles are passing through the overflow pipe, then adjustment must be made again to achieve the maximum solid discharge through the regulator.

In one particular embodiment the automatic discharge regulator was made from a natural rubber material known as Linatex (registered trade mark). The two sheets 20 were each Va inch thick and the two pads 27 were each 54 inch thick. The width of the sheets 20 was I 1% inches and their length was 17 inches and a strong rubber adhesive was used on each strip 21 to join the two sheets 20 together and on each pad 27 to adhere it to the sheet 20. These pads 27 were each 8 inches in diameter. Reinforcing strips 28 and a collar were added to the automatic discharge regulator and the unit was attached to the apex spigot of the hydrocyclone. The hydrocyclone was first tested with only water fed into the unitjand the vacuum control adjusted such that no water escaped through the automatic discharge regulator. Then as the sand and clay were added to the feedwater, it was found that the sand separated and discharged through the regulator whereas most of the clay and water discharged through the overflow.

It will be apparent to those skilled in the art that a number of variations may be made without departing from the scope of the present invention. For instance, the pads 27 need not necessarily be circular, they may be joined to the reinforcing strips 28, alternatively they may be oval or diamond in shape and the sheets need not necessarily be exactly rectangular. In some instances where it is necessary to separate different grades of ore from a liquid, then several classifiers may be used with the conditions inside the classifiers adjusted so that different size particles separate in different classifiers. The device may be constructed from plain sheets of flexible material such as rubber or may be specially moulded. The materials used for the regulator must be selected to suit the particular conditions including the ambient temperature and the type of material passing through the regulator.

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:

1. An automatic discharge regulator for a discharge exit from a separator or a classifier comprising a sleeve comprised of two sheets of resilient flexible material in side by side relationship, abutting one another at one end and adapted to sealingly mate with the discharge exit at the other end, said two sheets being sealingly held together along the length of the two opposing edges thereof, two reinforcing pads of flexible, elastic material, respectively, centrally located on and fixedly attached only to the outer surface of each of said two sheets so that each of said two sheets longitudinally extend in the direction of said one end beyond the corresponding said reinforcing pad, said reinforcing pads aiding in resiliently retaining said sheets at said one end in abutting relationship, thereby closing said one end of said sleeve when said regulator is in mating engagement with the discharge exit, the flexible material of said two sheets and of said reinforcing pads having sufficient resilience to allow said one end of said sleeve to be opened by and pass solid particles therethrough.

2. The automatic discharge regulator according to claim 1 wherein the sheets of flexible material are rectangular and the reinforcing pad on each sheet is circular.

3. In a method of regulating the discharge of solid materials from a separator through an exit including the steps of controlling the velocity and flow of solid particles conveyed in a fluid suspension to a separator, separating at least a portion of the solid particles from the fluid, and removing the majority of the fluid and any particles left therein, the improvement comprising passing the portion of solid particles through a sleeve of resilient material attached to the exit, the resiliency of 6 the sleeve forcing it closed when no solid particles pass therethrough, and varying the vacuum inside the separator to regulate the percent of solid particles separating from the fluid.

4. A method of regulating the discharge of solid particles from a hydrocyclone comprising the steps of conveying a slurry of the solid particles in a liquid to the hydrocyclone, separating at least a portion of the solid particles from the liquid within the hydrocyclone, discharging the portion of the solid particles through a sleeve of resilient material attached to an exit spigot of the hydrocyclone, the resiliency of the material forming the sleeve closed when no solid particles pass therethrough, and varying the vacuum in the hydrocyclone to hold the sleeve closed when no solid particles pass therethrough and regulate the percent of solid particles separating from the liquid.

5. The method of regulating the discharge of solid particles from a hydrocyclone according to claim 4 wherein the vacuum in the hydrocyclone is regulated by varying air bled into a siphon leg from an overflow pipe of the hydrocyclone.

6. An automatic discharge regulator for a discharge exit from a separator or a classifier comprising a sleeve comprised of two sheets of resilient flexible material in side by side relationship, abutting one another at one end and adapted to sealingly mate with the discharge exit at the other end, said two sheets being sealingly held together along the length of the two opposing edges thereof, two reinforcing pads of flexible, elastic material, respectively, centrally located on and fixedly attached only to the outer surface of each of said two sheets, said reinforcing pads aiding in resiliently retaining said sheets at said one end in abutting relationship, thereby closing said one end of said sleeve when said regulator is in mating engagement with the discharge exit, the other end of the sleeve having a reinforced collar of flexible material, the flexible material of said two sheets and of said reinforcing pads having sufficient resilience to allow said one end of said sleeve to be opened by and pass solid particles therethrough; and

said regulator further comprising a reinforcing strip extending from said other end of said sleeve in outer coaxial abutting relationship with said two sheets and terminating at a location spaced from the closure of said one end.

7. The automatic dishcarge regulator of claim 6, wherein said sheets are rectangular, said reinforcing pad on each sheet is circular, and said reinforcing strip partially surrounds, but is spaced from, said reinforcing pad.

8. The automatic discharge regulator of claim 6 wherein the two sheets of flexible material are resilient natural rubber and are held together at two opposing edges by rubber adhesive, and where the reinforcing pads are natural rubber and are positioned on the outside surface of the sheets by a rubber adhesive.

Claims (8)

1. An automatic discharge regulator for a discharge exit from a separator or a classifier comprising a sleeve comprised of two sheets of resilient flexible material in side by side relationship, abutting one another at one end and adapted to sealingly mate with the discharge exit at the other end, said two sheets being sealingly held together along the length of the two opposing edges thereof, two reinforcing pads of flexible, elastic material, respectively, centrally located on and fixedly attached only to the outer surface of each of said two sheets so that each of said two sheets longitudinally extend in the direction of said one end beyond the corresponding said reinforcing pad, said reinforcing pads aiding in resiliently retaining said sheets at said one end in abutting relationship, thereby closing said one end of said sleeve when said regulator is in mating engagement with the discharge exit, the flexible material of said two sheets and of said reinforcing pads having sufficient resilience to allow said one end of said sleeve to be opened by and pass solid particles therethrough.
2. The automatic discharge regulator according to claim 1 wherein the sheets of flexible material are rectangular and the reinforcing pad on each sheet is circular.
3. In a method of regulating the discharge of solid materials from a separator through an exit including the steps of controlling the velocity and flow of solid particles conveyed in a fluid suspension to a separator, separating at least a portion of the solid particles from the fluid, and removing the majority of the fluid and any particles left therein, the improvement comprising passing the portion of solid particles through a sleeve of resilient material attached to the exit, the resiliency of the sleeve forcing it closed when no solid particles pass therethrough, and varying the vacuum inside the separator to regulate the percent of solid particles separating from the fluid.
4. A method of regulating the discharge of solid particles from a hydrocyclone comprising the steps of conveying a slurry of the solid particles in a liquid to the hydrocyclone, separating at least a portion of the solid particles from the liquid within the hydrocyclone, discharging the portion of the solid particles through a sleeve of resilient material attached to an exit spigot of the hydrocyclone, the resiliency of the material forming the sleeve closed when no solid particles pass therethrough, and varying the vacuum in the hydrocyclone to hold the sleeve closed when no solid particles pass therethrough and regulate the percent of solid particles separating from the liquid.
5. The method of regulating the discharge of solid particles from a hydrocyclone according to claim 4 wherein the vacuum in the hydrocyclone is regulated by varying air bled into a siphon leg from an overflow pipe of the hydrocyclonE.
6. An automatic discharge regulator for a discharge exit from a separator or a classifier comprising a sleeve comprised of two sheets of resilient flexible material in side by side relationship, abutting one another at one end and adapted to sealingly mate with the discharge exit at the other end, said two sheets being sealingly held together along the length of the two opposing edges thereof, two reinforcing pads of flexible, elastic material, respectively, centrally located on and fixedly attached only to the outer surface of each of said two sheets, said reinforcing pads aiding in resiliently retaining said sheets at said one end in abutting relationship, thereby closing said one end of said sleeve when said regulator is in mating engagement with the discharge exit, the other end of the sleeve having a reinforced collar of flexible material, the flexible material of said two sheets and of said reinforcing pads having sufficient resilience to allow said one end of said sleeve to be opened by and pass solid particles therethrough; and said regulator further comprising a reinforcing strip extending from said other end of said sleeve in outer coaxial abutting relationship with said two sheets and terminating at a location spaced from the closure of said one end.
7. The automatic dishcarge regulator of claim 6, wherein said sheets are rectangular, said reinforcing pad on each sheet is circular, and said reinforcing strip partially surrounds, but is spaced from, said reinforcing pad.
8. The automatic discharge regulator of claim 6 wherein the two sheets of flexible material are resilient natural rubber and are held together at two opposing edges by rubber adhesive, and where the reinforcing pads are natural rubber and are positioned on the outside surface of the sheets by a rubber adhesive.
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Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4128474A (en) * 1977-03-24 1978-12-05 Linatex Corporation Of America Process for cleaning and dewatering fine coal
US4174275A (en) * 1978-01-23 1979-11-13 Krebs Engineers Hydrocyclone apparatus and method for underflow density control
US4203834A (en) * 1978-01-23 1980-05-20 Krebs Engineers Hydrocyclone underflow density control
US4224143A (en) * 1979-01-11 1980-09-23 Liller Delbert I Construction of shallow dish with tapered orifice for streamlined flow cyclone washing of crushed coal
US4341352A (en) * 1979-08-06 1982-07-27 Liller Delbert I Method of coal washing at low speed pumping
US4342383A (en) * 1980-04-17 1982-08-03 Burnett William C Method and apparatus for controlling the fall of grain through a conduit
US4454967A (en) * 1982-04-19 1984-06-19 Carr Michael A Drip preventer
US4482276A (en) * 1981-10-13 1984-11-13 Atlantic Bridge Company Limited Air lock valve for pneumatic conveying system
EP0135242A2 (en) * 1983-08-12 1985-03-27 HARRISONS & CROSFIELD (AUSTRALIA) LTD. Improvements in or relating to hydrocyclones
US4566612A (en) * 1983-09-15 1986-01-28 Popsicle Industries, Inc. Apparatus for dispensing flowable material
US4942911A (en) * 1987-06-30 1990-07-24 Btr Industrial Holdings, Ltd. Hopper assemblies
US5405063A (en) * 1993-12-09 1995-04-11 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Energy Mines And Resources Nozzle for fluidizing particulate material
US6085987A (en) * 1998-06-02 2000-07-11 Haraway; Coy N. Counter balance assembly for grain conduit
US20050285063A1 (en) * 2004-06-29 2005-12-29 Nelson Boice Bag valve
US20080201832A1 (en) * 2007-01-31 2008-08-28 Airbus Deutschland Gmbh Draining system having an odor seal for a vacuum toilet drain system
WO2010144939A1 (en) * 2009-06-17 2010-12-23 Linatex Australia Pty Ltd Mining and mineral process, system and method
US8490897B1 (en) * 2010-01-05 2013-07-23 Loren C. Magnus Granular spreader and method
US9434544B1 (en) 2013-04-12 2016-09-06 Coy N. Haraway Dustless spout assembly
US9694995B2 (en) 2013-04-12 2017-07-04 Coy N. Haraway Dustless spout assembly

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US3121578A (en) * 1961-07-24 1964-02-18 Railroad Rubber Products Inc Sand pipe nozzle
US3330448A (en) * 1965-01-04 1967-07-11 Murphy Willard Jerry Dispensing container
US3610477A (en) * 1969-07-16 1971-10-05 Albert M Herzig Automatic closure for containers
US3815794A (en) * 1972-03-02 1974-06-11 R Carlisle Plastic-film containers with self-sealing orifices

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US1964860A (en) * 1932-07-22 1934-07-03 John F Rabe Collapsible tube
US3121578A (en) * 1961-07-24 1964-02-18 Railroad Rubber Products Inc Sand pipe nozzle
US3330448A (en) * 1965-01-04 1967-07-11 Murphy Willard Jerry Dispensing container
US3610477A (en) * 1969-07-16 1971-10-05 Albert M Herzig Automatic closure for containers
US3815794A (en) * 1972-03-02 1974-06-11 R Carlisle Plastic-film containers with self-sealing orifices

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4128474A (en) * 1977-03-24 1978-12-05 Linatex Corporation Of America Process for cleaning and dewatering fine coal
US4174275A (en) * 1978-01-23 1979-11-13 Krebs Engineers Hydrocyclone apparatus and method for underflow density control
US4203834A (en) * 1978-01-23 1980-05-20 Krebs Engineers Hydrocyclone underflow density control
US4224143A (en) * 1979-01-11 1980-09-23 Liller Delbert I Construction of shallow dish with tapered orifice for streamlined flow cyclone washing of crushed coal
US4341352A (en) * 1979-08-06 1982-07-27 Liller Delbert I Method of coal washing at low speed pumping
US4342383A (en) * 1980-04-17 1982-08-03 Burnett William C Method and apparatus for controlling the fall of grain through a conduit
US4482276A (en) * 1981-10-13 1984-11-13 Atlantic Bridge Company Limited Air lock valve for pneumatic conveying system
US4454967A (en) * 1982-04-19 1984-06-19 Carr Michael A Drip preventer
EP0135242A2 (en) * 1983-08-12 1985-03-27 HARRISONS & CROSFIELD (AUSTRALIA) LTD. Improvements in or relating to hydrocyclones
EP0135242A3 (en) * 1983-08-12 1987-06-24 HARRISONS & CROSFIELD (AUSTRALIA) LTD. Improvements in or relating to hydrocyclones
US4566612A (en) * 1983-09-15 1986-01-28 Popsicle Industries, Inc. Apparatus for dispensing flowable material
US4942911A (en) * 1987-06-30 1990-07-24 Btr Industrial Holdings, Ltd. Hopper assemblies
US5405063A (en) * 1993-12-09 1995-04-11 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Energy Mines And Resources Nozzle for fluidizing particulate material
US6085987A (en) * 1998-06-02 2000-07-11 Haraway; Coy N. Counter balance assembly for grain conduit
US20050285063A1 (en) * 2004-06-29 2005-12-29 Nelson Boice Bag valve
US7011286B2 (en) * 2004-06-29 2006-03-14 Nelson Boice Bag valve
US20080201832A1 (en) * 2007-01-31 2008-08-28 Airbus Deutschland Gmbh Draining system having an odor seal for a vacuum toilet drain system
US9126686B2 (en) * 2007-01-31 2015-09-08 Airbus Operations Gmbh Draining system having an odor seal for a vacuum toilet drain system
WO2010144939A1 (en) * 2009-06-17 2010-12-23 Linatex Australia Pty Ltd Mining and mineral process, system and method
US8490897B1 (en) * 2010-01-05 2013-07-23 Loren C. Magnus Granular spreader and method
US9434544B1 (en) 2013-04-12 2016-09-06 Coy N. Haraway Dustless spout assembly
US9694995B2 (en) 2013-04-12 2017-07-04 Coy N. Haraway Dustless spout assembly

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