US2597434A - Surface treating apparatus - Google Patents

Surface treating apparatus Download PDF

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US2597434A
US2597434A US67462A US6746248A US2597434A US 2597434 A US2597434 A US 2597434A US 67462 A US67462 A US 67462A US 6746248 A US6746248 A US 6746248A US 2597434 A US2597434 A US 2597434A
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valve
chamber
pressure
hopper
air
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Lewis H Bishop
John S Finn
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B24GRINDING; POLISHING
    • B24CABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
    • B24C3/00Abrasive blasting machines or devices; Plants
    • B24C3/02Abrasive blasting machines or devices; Plants characterised by the arrangement of the component assemblies with respect to each other
    • B24C3/06Abrasive blasting machines or devices; Plants characterised by the arrangement of the component assemblies with respect to each other movable; portable
    • B24C3/065Abrasive blasting machines or devices; Plants characterised by the arrangement of the component assemblies with respect to each other movable; portable with suction means for the abrasive and the waste material

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  • This invention relates to a method for continface treating methods and apparatus of the type I described in the patent to William H. Mead, No. 2,455,514, issued December 7, 1948. That device simultaneously impels treating material against a surface and suction-removes the spent abrasive and waste material.
  • a grit reclaimer such as that described in the copending application No. 778,378, filed October 7, 1947, the spent abrasive can be separated from the-waste material and re-used.
  • the problems solved by this present invention are those having to do with makin possible continuous operation of such or similar apparatus,
  • the problems arise from the fact that the abrasive, which is impelled against a surface by a high-pressure blast of air or by an impeller wheel and is removed from-the surface bya vacuum pump, carries along with it the waste inaterial which is abraded from the surface.
  • the abrasive grit is next separated from the waste material while still under extremely low pressure conditions.
  • One problem'which had to be solved before the apparatus could operate continuously was how to restore the" abrasive from the low pressure atmospherewithout either interfering with the low pressure conditions'in the abrasive-removing line, or reducing the high pressure in the abrasive-impelling line.
  • One important object of this invention is to provide an apparatus enabling continuous operation of such a machine. This invention automatically replenishes the feed hopper during use, and there is no need to interrupt operations for refilling the hopper.
  • Another object of the invention is to provide an apparatus for transferring material between chambers under different pressure conditions.
  • Another object of the invention is to provide a transfer apparatus of the type described which will not adversely affect the pressure conditions in the chambers.
  • Another object of the apparatus is to provide an apparatus for transferring granular material from a low pressure chamber to a high-pressure chamber without substantially altering the pressure conditions in either chamber.
  • a further object of the invention is to provide an automatic transfer device of the type described.
  • Another object of the invention is to provide a time-controlled transfer apparatus.
  • a further object of the invention is to provide an apparatus suitable for continuous sand-blasting with a relatively small quantity of grit.
  • a further .object is to achieve continuous sand blasting over a long period of time, without having to supplement a relatively small, mobile supply of abrasive.
  • Fig. 1 is a view in elevation, partly in section, of a continuous surface treating apparatus embodying the principles of the invention
  • Fig. 2 is a diagram of the piping circuit in the transfer apparatus
  • Fig. 3 is a diagram of the electrical circuit employed
  • Fig. 4 is an enlarged view in elevation and in section of the lower dump valve
  • Fig. 5 is a view in perspective and in section of the apparatus in the vicinity of the lower dump valve.
  • the apparatus employs an intermediate chamber between the low pressure reclaimer hopper and the high pressure feed hopper.
  • the intermediate chamber By connecting the intermediate chamber to only one of the said chambers at a time, the material is transferred first from the low pressure hopper to the intermediate chamber and subsequently from'th'e intermediate chamber to the feed hopper.
  • the pressure of the intermediate chamber is raised before the valve to the high pressure chamber is to be open, and after this valve is; closed the pressure in the chamber is reduced before the valve to the low pressure chamber isopened. All of these valves and pressure adaptors are controlled by a timing device which alternates them according to a predetermined cycle. 7 I
  • Fig. 1 shows a device embodying the principles of this invention used in conjunction with'a'surface-treating apparatus .of the type described more fully in'Patent No.:2,'455;514.
  • a compressor sends air under pressure through aeonduit At a manifold
  • This valve I6 is preferably of a type described in the copending application by William H. Mead, Sei', No. 55,243, filed October 18, 1948,-which'issued as Patent No. 2,521,931, dated September 12, 1950.
  • Grit is introduced from the hopper into the blast current at the valve l5 and is fed through a conduit I! to an operating head l8, where it is impelled against .asurfacel 9.
  • a suction pump draws the spent abrasive and waste material (such as paint flakes, rust, sawdust, etc.) out of the head l8 through a suction conduit 2
  • the abrasive and waste are separated, and the waste is carried out through a conduit 23 to any form of dust collector.
  • the reclaimed abrasive falls down into a reclaimer hopper 25, still under'nearvacuum conditions.
  • and 32 comprise airactuated, cone-shaped plugs 33, which are closed against the respective openings 34 or 35by' compressed air entering through openings 33 at the lower end of the valves.
  • opens by a combination of spring pressure and gravity, dropping when the air pressure inside the valve falls below a certain level, and then permits grit to fall from the reclaimer hopper 25 into the intermediate transfer chamber 30.
  • the lower valve 32 is adapted for quicker and more positive control. As shown in Fig. 4, the lower valve 32 is supported by a housing 31 which is suspended from the feed hopper housing H. The lower end of the housing 31 is closed except for the-opening '35, and the upper end is also closed, preferably by a hood 38.
  • a valve stem 40 which depends from the "cone 33, is slidable up and down through an opening 4
  • a flexible, collapsible sleeve or boot 42 is secured tightly around the stem 48 and around the opening 4
  • annular flexible-din phr-agm 43 Below the hood 38 is an annular flexible-din phr-agm 43. Its inner periphery is secured to the stem and its outer periphery is secured to the 4 housing 31.
  • the diaphragm 43 and the hood 38 enclose an upper chamber 44, having an opening 45 through which compressed air may enter from the duct 31, in a manner to be explained.
  • a lower chamber 46 open only to the air pressure inlet 36.
  • a stretched spring 41 surrounds the stem 43 inthe lower chamber 46.
  • the lower end 52 of the spring 41 is secured to the stem 40, while upper end 53 of the spring is anchored to the valve housing 37.
  • the spring 41 biases the valve 32 downwarciytcward its open position.
  • the force of the-spring 41 augments the force of gravity an'd aids in providing a quicker opening action a'galnst'the'Trictionof the stem 40 in its guides -4
  • the spring 41 is a light one; for example, a very successful valve uses a spring which exerts "a force of about ten .pounds.
  • a typical diaphragm 43 having an area of 20 square inches
  • the spring will not open the valve until the air pressure in the upper chamber-reaches about 1990 lbs., or 99.5 p. s. 'i. Due to this relationship, the valve 32 and the whole apparatusmay be operated over a very wide range of pressures without changing the spring 41, and the valve 32 will not open until the pressureinchamber 44almost balances the pressure inchamber 46.
  • the chamber 46 is kept under pressure continuously during operation of the machine, and this air pressure holds the cone 33 normally up against the'opening '35. However, when the air pressure in the upper chamber 44 (in a manner to be described) balances the air pressure in the lower chamber 46, the weight of the cone and other moving. parts overbalances the spring 41 and the cone 33 drops, opening the valve 32.
  • a battle [plate 48, 49 is positioned above each opening 34, 35 just above where the point of the cone 33 rests when the cone is in its upper or closed position. These'baffles 48, 49 prevent the grit from stacking up over the openings 34, 35 and keep the space above the openings free so that the cones 33 'canclose quickly and easily. Otherwise, when the pressure changes in the chamber 30 there might-be disruption of the system hy'a leak from the high pressure chamber 14 .into the lower pressure chamber 25. Allthe grit must pass through the spaces 50 between the periphery of the baffle plates and the hopper walls: f Then it slides down the inclined hopper walls andfinto the verticalopening.
  • hangs down underneath-and-around-each opening 34 and 35 to keep grit out of the air openings adjacent the upper ends of the hoppers l4 and 30.
  • the pressure in the reclaimer hopper 25 is normally about ten inches of mercury, while the pressure in the feed hopper chamber
  • timing mechanism 80 may also, if desired, be used to turn on and ofi the timing mechanism 80.
  • conduit 63 leads to the lower opening 36 of the lower dump valve 32 and air pressure therein urges the valve 32 toward a closed position when the machine is operating.
  • the conduit 64 leads through a second solenoid valve 65, which can efiect control of the valves 3
  • a second solenoid valve 65 which can efiect control of the valves 3
  • Another X fitting 66 from which three conduits 61, 68 and 69 lead out.
  • the conduit 6'! leads to the opening 45 in the upper chamber 44 of the lower dump valve 32.
  • Compressed air which passes through the solenoid valve 65 is conducted to the chamber 44 and opens the valve 32.
  • the pressures above and below the diaphragm 43 balance each other and gravity and the spring 41 open the valve 32.
  • the conduit 68 leads to a third solenoid valve I0, and thence vents to the atmosphere when the valve I6 is open.
  • the solenoid valve I0 is opened only when and at the same moment as the solenoid valve 65 is closed, and at that time quickly bleeds the air from the chamber 44, so that the lower valve 32 closes.
  • the conduit 69 leads up through a check valve II (which prevents air from flowing backwards through the conduit 69 and out the valve I0 when the latter is open) to a T fitting I2.
  • the conduit 69 is divided into a conduit I3 passing into the tank 30 and a conduit I4 leading to the dump valve 3
  • the conduits are of sufliciently small diameter so that the pressure does not build up instantaneously in the upper chamber 46 of the valve 32 or inside the intermediate chamber 36.
  • three or four seconds may elapse before the pressure in the chamber 46 and in the chamber 30 approximates the pressure in the hopper I4. In this way there will be no drop in pressure when the valve 32 opens. Otherwise, there will not be complete continuity, and a portion of the surface I9 may be skipped and not treated during the time necessary to equalize the pressure. This is one problem which the present device solves in the manner just indicated.
  • a bleed conduit 15 leads out from the tank 30 through a strainer I6 to a solenoid valve 11, and when the valve 11 is open, air may pass out through a muiiier I8 to the open air.
  • the strainer I6 prevents any grit from getting into solenoid I1 and damaging it, and the check valve II performs the same function for the solenoid valve I6.
  • the muffler I8 silences the noise from the rush of air.
  • the solenoid valve 60 Since the solenoid valve 60 is open whenever the machine is operatingthe air current then flows through the blast conduit I1 and through the conduit 63 to fill the lower chamber 46 of the dump valve 32 to hold it closed.
  • the other 6 three solenoid valves 65, III and 11 are controlled by a timer 80. When the valve 65 is open, the valves I6 and 11 are closed, and vice versa.
  • the electrical circuit is shown in Fig. 3.
  • a three line A. C. supply is used, with one wire 8
  • wires 84 and 85 lead to a 110-volt-6-volt transformer 86.
  • wires 81 and 86 lead to a 6-volt relay 89, line 88 passing through the master switch 6
  • a wire 96 leads to the side 82 of the 110 volt input line.
  • leads to the master solenoid 66, and another wire 92 leads to post 93 of the timer 80.
  • the solenoid 60 is thus independent from the timer 80, but both the timer 80 and the valve 66 are energized by the switch 6
  • Wires 94, 95 and 96 each lead from the timer post 93 to one side of the solenoids 65, I0 and 11, respectively.
  • Wires 91 and 98 lead back from the opposite sides of the solenoids I0 and TI to a switch element 99 of the timer 86, and a wire I66 leads from the opposite side of the-solenoid 65 to a switch element
  • 02 leads from the timer post I63 to the A. C. line 82.
  • All three solenoids 65, I0 and I1 operate simultaneously but not in the same direction. That is, when the circuit controlling the valve 65 is closed so that the valve 65 is open, the circuit controlling the valves I0 and I1 is open so that the valves I0 and 11 are closed. Air will then pass into and be confined in the tank 30. When the circuit controlling the valve 65 is open, the valve 65 is closed, and no air passes beyond it. Simultaneously, the other circuit is closed, and the valve I6 is opened to bleed oil" the valve 32 so that the latter closes almost instantly on a short drop in pressure. ously opens the valve 11 to bleed out the tank 30 and valve 3
  • the solenoid valve 60 is opened to admit air from the compressor I6 through the conduit II to the feed tank I4 and feed valve I6, so that abrasive is sent to the head I8.
  • the timer 86 is started and runs its cycle.
  • the solenoid valve 65 is closed to begin with. Therefore, no air flowsfrom the conduit II into the conduit 64, and consequently none flows in the conduits 61, I3 and I4.
  • is held open by its spring and by gravity.
  • the lower dump valve 32 is closed, because there is no pressure in the upper chamber 44 and the lower chamber 46 isunder high pressure.
  • the suction pump 20 is operating, and it keeps the reclaimer hopper 25 at a vacuum of about 10 inches of mercury. Any reclaimed grit remaining in the reclaimer 25 falls through the slits 50 around the edges of the plate 48 and is stored in the tank 30.
  • the timer 80 throws a switch which opens the solenoid 65 and closes the solenoids I6 and I1. Air then flowsfrom the conduit I, through the con 'duit 64, mm the conduits 61, I3 and I4. From the conduit 74 air passes into-the upper dump The same circuit simultanevalve 31. and closes it almost immediately. Air Passing through the conduit 13 fills the tank 30, and the pressure soon approaches and equals the pressure in the feed hopper 14. At the same time, air fills the upper chamber 44 of the valve 32, and when it reaches a pressure closely approaching that in chamber 46, the valve is opened by its spring 41 and its co-acting forces. Grit inside the tank 30 can then fall down through the slits 50 around the baflle 49 and down into the feed hopper, l4, replenishing it without interfering with the pressure conditions in the blast line. y, 4
  • the solenoid valve 65 When the timerSO reaches another predetermined position, the solenoid valve 65 is closed and the valves 10 and H are opened. Conduits 61, 13 and 14 are cut off from their supply of air, while'conduits 68 and 15 are opened to the atmosphere. Airimmediately bleeds out of the upper chamber 44 of the lower dump valve 32, while the check valve H prevents any cushioning efiect from the conduits 73 and 14. When the pressure has dropped only a short way (usually a pound, or less) the air pressure in the chamber 46 closes the lower dump valve 32. The air in the tank 30 fiows to atmosphere out the conduit l through the strainer 16, solenoid valve 11, and muffler l8.
  • fiows back through the conduit 14 into the conduit 13, through the tank 30 and the conduit 15, and out to atmosphere.
  • the upper dump valve 3! opens, and what little air remains is immediately sucked out by the pump 20.
  • the pump 20 draws 300 cubic feet of air per minute. Since the volume of the chamber 30 is only a cubic foot or so, this small pressure differential. will not affect the operation at the head.
  • opens, the grit stored up in the chamber25 may then fall down again into the chamber 30, completing the cycle.
  • An apparatus for continuous abrasive-blasting comprising a feed hopper for storing abrasive material, an air blast line, a feed valve for feeding said material into said line, an operating head where said material is impinged against a surface, a suction line for withdrawing said material and waste from said surface, a separator for salvaging said material out of said waste, a reclaimer hopper for receiving said withdrawn material, an intermediate hopper between said reclaimer hopper and said feed hopper, a first transfer valve between said reclaimer hopper and said intermediate hopper, a second transfer valve between said intermediate hopper and said feed hopper, a timing device, and an electrical relay operated by said timing device to alternately close said first valve and open said second valve and close said second valve and open said first valve.
  • An apparatus for continuous abrasive-blasting comprising a feed hopper for storing abrasive material, an air blast line, a feed valve for feeding said material into said line, an operating head where said material is impinged against a surface, a suction line for withdrawing said material and waste from said surface, a separator for salvaging said material out of said waste, a reclaimer hopper for receiving said salvaged material, an intermediate hopper between said reclaimer hopper and said feed hopper, a first transfer valve between said reclaimer hopper and said intermediatehopper, a second transfer valve between said intermediate hopper and said feed hopper, a timing device, an electrical relay operated by said timing device to alternately close said first valve and open said second valve and close said second valve and open said first valve, means to admit air to said intermediate hopper when said first valve is closed, and means to bleed air from said intermediate hopper when said second valve is closed.
  • An apparatus for transferring granular material from a low pressure chamber to a high pressure chamber comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber, a first valve between said intermediate chamber and said low pressure chamber,-a second valve between said intermediate chamber and said high pressure chamber, a timing device, and means operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
  • An apparatus for transferring granular material from a low pressure chamber to a high pressure chamber comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber, a first valve between said intermediate chamber and said low pressure chamber, a second valve between said intermediate chamber and said high pressure chamber, a timing device, and an electrical relay control operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
  • An apparatus for transferring granular material from a low pressure chamber to a chamber maintained at high pressure by a high pressure line without upsetting the pressures concerned comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber; an air operated valve between said intermediate chamber and each of the other said chambers; a first solenoid valve adapted to open for simultaneously admitting air from said high pressure line to the upper of said valves to close it and for admitting air from said high pressure line to said intermediate chamber to build up the pressure therein and for admitting air from said high pressure line to said lower valve to open it when its pressure and the pressure in said intermediate chamber reach a predetermined value, said solenoid valve also being adapted to close for simultaneously cutting off all air from the high pressure line to said valves and said intermediate chamber; a second solenoid valve adapted to open to bleed air from said lower valve to close it; a third solenoid valve adapted to open for bleeding air from said intermediate chamber so that its pressure may be reduced and from said upper valve so that it may open when its pressure drops below a
  • An apparatus for continuous abrasive-blasting comprising: a feed hopper for storing abrasive material; an air blast conduit; means for feeding said material into said conduit; means for impinging said material from said conduit against a surface to be treated; means for withdrawing said material from said surface; a reclaimer hopper for receiving said withdrawn material; an intermediate hopper between said reclaimer hopper and said feed hopper; a first transfer valve between said reclaimer hopper and said intermediate hopper; a second transfer valve between said intermediate hopper and said feed hopper; a timing device; and means actuated by said timing device for alternately closing said first valve and opening said second valve, and closing said second valve and opening said first valve.
  • An apparatus for continuous abrasiveblasting comprising a feed hopper for storing abrasive material; an air blast conduit; means for feeding said material into said conduit; means for impinging said material from said conduit against a surface; means for withdrawing said material from said surface; a reclaimer hopper for receiving said withdrawn material; an intermediate hopper between said reclaimer hopper and said feed hopper; a first transfer valve between said reclaimer hopper and said intermedi ate hopper; a second transfer valve between said intermediate hopper and said feed hopper; a timing device; means actuated by said timing device for alternately closing said first valve and opening said second valve, and closing said second valve and opening said first valve; means for admitting air to said intermediate hopper when said first valve is closed; and means for bleeding air from said intermediate hopper when said second valve is closed.
  • An apparatus for transferring granular material from a first chamber to a second chamber comprising an intermediate chamber placed between said first and second chambers; a first valve between said intermediate chamber and said first chamber; a second valve between said intermediate chamber and said second chamber; a timing device; and means operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
  • An apparatus for transferring granular material from a low pressure chamber to a chamber maintained at high pressure by a high pressure line, without upsetting the pressures concerned comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber; a pair of pneumatic valves, one being located between said intermediate chamber and each of the other saidchambers to open and close the passages between said chambers; a first control valve adapted when opened to simultaneously admit gas from said high pressure line to the upper of said pneumatic valves to close it and to admit gas from said high pressure line to said intermediate chamber to build up the pressure therein and to admit gas from said high pressure line to the lower of said pneumatic valves to open it when its pressure and the pressure in said intermediate chamber reach a predetermined value, said first control valve also being adapted when closed to simultaneously cut off all gas from the high pressure line to said pneumatic valves and said intermediate chamber; a second control valve adapted when opened to bleed gas from said lower pneumatic valve to close it; a third control valve adapted when opened to bleed gas from said intermediate chamber so

Description

y 1952 L. H. BISHOP ET AL SURFACE TREATING APPARATUS 5 Sheets-Sheet 1 Filed Dec. 27, 1948 DusT COLLECTOR INVENTORS BISHOP Fl/V/V ATTOR/Vf) y 1952 L. H. BISHOP ET AL 2,597,434
SURFACE TREATING APPARATUS Filed Dec. 2'7, 1948 5 Sheets-Sheet 2 25 i T' 2 0 Z INVENTOR LEW/5 H. BISHOP 5 JOHN S. FINN A TTOR/VEY y 0, 1952 H. BISHOP ET AL 2,597,434
' SURFACE TREATING APPARATUS Filed Dec. 27, 1948 a Sheets-Sheet 5 a/ IIOM IN ENTO LEW/5 H. B/ HOP JOHN S. FIN/V ATTORNEY Patented May 20, 1952 SURFACE TREATING APPARATUS Lewis H. Bishop and John S. Finn, Burlingame, Calif., assignors, by mesne assignments, to William H. Mead, Oakland, Calif.
Application December 2'7, 1348, Serial No. 67,462
11 Claims. (Cl. 51-12) This invention relates to a method for continface treating methods and apparatus of the type I described in the patent to William H. Mead, No. 2,455,514, issued December 7, 1948. That device simultaneously impels treating material against a surface and suction-removes the spent abrasive and waste material. By employing a grit reclaimer, such as that described in the copending application No. 778,378, filed October 7, 1947, the spent abrasive can be separated from the-waste material and re-used.
The problems solved by this present invention are those having to do with makin possible continuous operation of such or similar apparatus, The problems arise from the fact that the abrasive, which is impelled against a surface by a high-pressure blast of air or by an impeller wheel and is removed from-the surface bya vacuum pump, carries along with it the waste inaterial which is abraded from the surface. The abrasive grit is next separated from the waste material while still under extremely low pressure conditions. One problem'which had to be solved before the apparatus could operate continuously was how to restore the" abrasive from the low pressure atmospherewithout either interfering with the low pressure conditions'in the abrasive-removing line, or reducing the high pressure in the abrasive-impelling line.
Heretofore, it was necessary to shut ofi the machine during such transfer, so that the pressure in the blast line dropped to atmospheric 2 the operator had to stop the machine to refill the hopper.-
One important object of this invention is to provide an apparatus enabling continuous operation of such a machine. This invention automatically replenishes the feed hopper during use, and there is no need to interrupt operations for refilling the hopper.
Another object of the invention is to provide an apparatus for transferring material between chambers under different pressure conditions.
Another object of the invention is to provide a transfer apparatus of the type described which will not adversely affect the pressure conditions in the chambers.
Another object of the apparatus is to provide an apparatus for transferring granular material from a low pressure chamber to a high-pressure chamber without substantially altering the pressure conditions in either chamber.
" A further object of the invention is to provide an automatic transfer device of the type described.
Another object of the invention is to provide a time-controlled transfer apparatus.
A further object of the invention is to provide an apparatus suitable for continuous sand-blasting with a relatively small quantity of grit.
A further .object is to achieve continuous sand blasting over a long period of time, without having to supplement a relatively small, mobile supply of abrasive. I
' Other objects and advantages of the invention will appear from the following detailed description of an embodiment, presented in accordance with U. S. Revised Statutes, Sec. 4888. It is appreciated that changes in detail may be made in accordance with the principles set forth, so that a machine differing in some details-from this embodiment would still be within the spirit of the invention as described in the appended claims.
In the drawings:
Fig. 1 is a view in elevation, partly in section, of a continuous surface treating apparatus embodying the principles of the invention;
Fig. 2 is a diagram of the piping circuit in the transfer apparatus;
Fig. 3 is a diagram of the electrical circuit employed;
Fig. 4 is an enlarged view in elevation and in section of the lower dump valve; and
Fig. 5 is a view in perspective and in section of the apparatus in the vicinity of the lower dump valve.
The apparatus employs an intermediate chamber between the low pressure reclaimer hopper and the high pressure feed hopper. By connecting the intermediate chamber to only one of the said chambers at a time, the material is transferred first from the low pressure hopper to the intermediate chamber and subsequently from'th'e intermediate chamber to the feed hopper. The pressure of the intermediate chamber is raised before the valve to the high pressure chamber is to be open, and after this valve is; closed the pressure in the chamber is reduced before the valve to the low pressure chamber isopened. All of these valves and pressure adaptors are controlled by a timing device which alternates them according to a predetermined cycle. 7 I
Fig. 1 shows a device embodying the principles of this invention used in conjunction with'a'surface-treating apparatus .of the type described more fully in'Patent No.:2,'455;514. A compressor sends air under pressure through aeonduit At a manifold |2 the air eurrentis'divided, a conduit |3 shunting some of the air into a grit feed hopper l4, while the rest of the airifed through a conduit |5 into a grit-feed valve Hi. This valve I6 is preferably of a type described in the copending application by William H. Mead, Sei', No. 55,243, filed October 18, 1948,-which'issued as Patent No. 2,521,931, dated September 12, 1950. Grit is introduced from the hopper into the blast current at the valve l5 and is fed through a conduit I! to an operating head l8, where it is impelled against .asurfacel 9.
A suction pump draws the spent abrasive and waste material (such as paint flakes, rust, sawdust, etc.) out of the head l8 through a suction conduit 2| into a grit reclaimer 22, preferablyoi the type disclosed in pending application Serial No. 778,378, filed October 7, 1947. Here the abrasive and waste are separated, and the waste is carried out through a conduit 23 to any form of dust collector. The reclaimed abrasive falls down into a reclaimer hopper 25, still under'nearvacuum conditions.
Between the reclaimer hopper 25 and the feed hopper I4 is positioned an intermediat transfer chamber 30. At its upper end is an upper dump valve 3|, and at its lower end is a lower dump valve 32. Both valves 3| and 32 comprise airactuated, cone-shaped plugs 33, which are closed against the respective openings 34 or 35by' compressed air entering through openings 33 at the lower end of the valves.
The upper valve 3| opens by a combination of spring pressure and gravity, dropping when the air pressure inside the valve falls below a certain level, and then permits grit to fall from the reclaimer hopper 25 into the intermediate transfer chamber 30.
The lower valve 32 is adapted for quicker and more positive control. As shown in Fig. 4, the lower valve 32 is supported by a housing 31 which is suspended from the feed hopper housing H. The lower end of the housing 31 is closed except for the-opening '35, and the upper end is also closed, preferably by a hood 38. A valve stem 40, which depends from the "cone 33, is slidable up and down through an opening 4| in the hood 38. To prevent grit from working down through the opening 4|, a flexible, collapsible sleeve or boot 42 is secured tightly around the stem 48 and around the opening 4|.
Below the hood 38 is an annular flexible-din phr-agm 43. Its inner periphery is secured to the stem and its outer periphery is secured to the 4 housing 31. The diaphragm 43 and the hood 38 enclose an upper chamber 44, having an opening 45 through which compressed air may enter from the duct 31, in a manner to be explained. Below the diaphragm is a lower chamber 46, open only to the air pressure inlet 36.
A stretched spring 41 surrounds the stem 43 inthe lower chamber 46. The lower end 52 of the spring 41 is secured to the stem 40, while upper end 53 of the spring is anchored to the valve housing 37. The spring 41 biases the valve 32 downwarciytcward its open position. The force of the-spring 41 augments the force of gravity an'd aids in providing a quicker opening action a'galnst'the'Trictionof the stem 40 in its guides -4| and. and the force necessary to compress the boot.
Preferably the spring 41 is a light one; for example, a very successful valve uses a spring which exerts "a force of about ten .pounds. When the blastilineis operated at p. s. i., a typical diaphragm 43 (having an area of 20 square inches) will be iorced up with 2000 lbs. pressure by air inthechamber-46. Thus the spring will not open the valve until the air pressure in the upper chamber-reaches about 1990 lbs., or 99.5 p. s. 'i. Due to this relationship, the valve 32 and the whole apparatusmay be operated over a very wide range of pressures without changing the spring 41, and the valve 32 will not open until the pressureinchamber 44almost balances the pressure inchamber 46.
The chamber 46 is kept under pressure continuously during operation of the machine, and this air pressure holds the cone 33 normally up against the'opening '35. However, when the air pressure in the upper chamber 44 (in a manner to be described) balances the air pressure in the lower chamber 46, the weight of the cone and other moving. parts overbalances the spring 41 and the cone 33 drops, opening the valve 32.
A baiile [ plate 48, 49 is positioned above each opening 34, 35 just above where the point of the cone 33 rests when the cone is in its upper or closed position. These'baffles 48, 49 prevent the grit from stacking up over the openings 34, 35 and keep the space above the openings free so that the cones 33 'canclose quickly and easily. Otherwise, when the pressure changes in the chamber 30 there might-be disruption of the system hy'a leak from the high pressure chamber 14 .into the lower pressure chamber 25. Allthe grit must pass through the spaces 50 between the periphery of the baffle plates and the hopper walls: f Then it slides down the inclined hopper walls andfinto the verticalopening.
Preferably a shroud 5| hangs down underneath-and-around-each opening 34 and 35 to keep grit out of the air openings adjacent the upper ends of the hoppers l4 and 30.
The pressure in the reclaimer hopper 25 is normally about ten inches of mercury, while the pressure in the feed hopper chamber |4, during typical operating conditions, is normally kept at about'one hundred pounds per square inch; therefore, valves 31 and 32 are never allowed to open at'the same time while the apparatus is operating. Moreover, the air inside theintermediate chamber 30 is brought to a pressure approaching the pressure in the feed hopper |4 (approximately one hundred pounds per square inch in this case) before. the valve 32-is opened.- The pressure-is reduced after thevalve closes and before the valve-opens. These conditions are obtained by means of the pressure control circuits shown in Fig. 2 andthe electrical control circuits shown 6| on the operating head I8. This switch 6| is thus used to shut the blast line off and on; it
may also, if desired, be used to turn on and ofi the timing mechanism 80.
Between the valve 60 and the T fitting I2 on the conduit I I is an X fitting 62. At the fitting 62 two conduits 63 and 64 open off the line II The conduit 63 leads to the lower opening 36 of the lower dump valve 32 and air pressure therein urges the valve 32 toward a closed position when the machine is operating.
The conduit 64 leads through a second solenoid valve 65, which can efiect control of the valves 3| and 32 as well as the pressure inside the intermediate chamber 30. Beyond the solenoid valve 65, is another X fitting 66, from which three conduits 61, 68 and 69 lead out. The conduit 6'! leads to the opening 45 in the upper chamber 44 of the lower dump valve 32. Compressed air which passes through the solenoid valve 65 is conducted to the chamber 44 and opens the valve 32. The pressures above and below the diaphragm 43 balance each other and gravity and the spring 41 open the valve 32. r
The conduit 68 leads to a third solenoid valve I0, and thence vents to the atmosphere when the valve I6 is open. The solenoid valve I0 is opened only when and at the same moment as the solenoid valve 65 is closed, and at that time quickly bleeds the air from the chamber 44, so that the lower valve 32 closes.
The conduit 69 leads up through a check valve II (which prevents air from flowing backwards through the conduit 69 and out the valve I0 when the latter is open) to a T fitting I2. There, the conduit 69 is divided into a conduit I3 passing into the tank 30 and a conduit I4 leading to the dump valve 3|. Thus, when the solenoid valve 65 is open, the valve 3| is closed almost immediately and when the pressure inside the tank 30 reaches approximately the level of the pressure inside the hopper I4, the valve 32 opens.
Preferably the conduits are of sufliciently small diameter so that the pressure does not build up instantaneously in the upper chamber 46 of the valve 32 or inside the intermediate chamber 36. After the valve 3| has closed, three or four seconds may elapse before the pressure in the chamber 46 and in the chamber 30 approximates the pressure in the hopper I4. In this way there will be no drop in pressure when the valve 32 opens. Otherwise, there will not be complete continuity, and a portion of the surface I9 may be skipped and not treated during the time necessary to equalize the pressure. This is one problem which the present device solves in the manner just indicated.
A bleed conduit 15 leads out from the tank 30 through a strainer I6 to a solenoid valve 11, and when the valve 11 is open, air may pass out through a muiiier I8 to the open air. The strainer I6 prevents any grit from getting into solenoid I1 and damaging it, and the check valve II performs the same function for the solenoid valve I6. The muffler I8 silences the noise from the rush of air.
Since the solenoid valve 60 is open whenever the machine is operatingthe air current then flows through the blast conduit I1 and through the conduit 63 to fill the lower chamber 46 of the dump valve 32 to hold it closed. The other 6 three solenoid valves 65, III and 11 are controlled by a timer 80. When the valve 65 is open, the valves I6 and 11 are closed, and vice versa.
The electrical circuit is shown in Fig. 3. Preferably a three line A. C. supply is used, with one wire 8| grounded. From the second side 82 and the third side 83 of a 110-volt A. C. supply, wires 84 and 85 lead to a 110-volt-6-volt transformer 86. From each pole of the 6-volt side, wires 81 and 86 lead to a 6-volt relay 89, line 88 passing through the master switch 6|. From one pole of the relay actuator, a wire 96 leads to the side 82 of the 110 volt input line. From the other side of the relay actuator 89, one wire 9| leads to the master solenoid 66, and another wire 92 leads to post 93 of the timer 80. The solenoid 60 is thus independent from the timer 80, but both the timer 80 and the valve 66 are energized by the switch 6|. When the current is on, the valve 66 is always open, and the timer 80 operates continuously.
Wires 94, 95 and 96 each lead from the timer post 93 to one side of the solenoids 65, I0 and 11, respectively. Wires 91 and 98 lead back from the opposite sides of the solenoids I0 and TI to a switch element 99 of the timer 86, and a wire I66 leads from the opposite side of the-solenoid 65 to a switch element |6| on the timer 80. Another wire |02 leads from the timer post I63 to the A. C. line 82.
All three solenoids 65, I0 and I1 operate simultaneously but not in the same direction. That is, when the circuit controlling the valve 65 is closed so that the valve 65 is open, the circuit controlling the valves I0 and I1 is open so that the valves I0 and 11 are closed. Air will then pass into and be confined in the tank 30. When the circuit controlling the valve 65 is open, the valve 65 is closed, and no air passes beyond it. Simultaneously, the other circuit is closed, and the valve I6 is opened to bleed oil" the valve 32 so that the latter closes almost instantly on a short drop in pressure. ously opens the valve 11 to bleed out the tank 30 and valve 3|, which opens when the pressure has dropped.
In operation, when the master switch 6| is turned on, the solenoid valve 60 is opened to admit air from the compressor I6 through the conduit II to the feed tank I4 and feed valve I6, so that abrasive is sent to the head I8. At the same time, the timer 86 is started and runs its cycle.
For convenience, we shall assume that the solenoid valve 65 is closed to begin with. Therefore, no air flowsfrom the conduit II into the conduit 64, and consequently none flows in the conduits 61, I3 and I4. The upper dump valve 3| is held open by its spring and by gravity. The lower dump valve 32 is closed, because there is no pressure in the upper chamber 44 and the lower chamber 46 isunder high pressure. The suction pump 20 is operating, and it keeps the reclaimer hopper 25 at a vacuum of about 10 inches of mercury. Any reclaimed grit remaining in the reclaimer 25 falls through the slits 50 around the edges of the plate 48 and is stored in the tank 30.
After a period of time determined to occur before all thegrit is used out of the tank I4 the timer 80 throws a switch which opens the solenoid 65 and closes the solenoids I6 and I1. Air then flowsfrom the conduit I, through the con 'duit 64, mm the conduits 61, I3 and I4. From the conduit 74 air passes into-the upper dump The same circuit simultanevalve 31. and closes it almost immediately. Air Passing through the conduit 13 fills the tank 30, and the pressure soon approaches and equals the pressure in the feed hopper 14. At the same time, air fills the upper chamber 44 of the valve 32, and when it reaches a pressure closely approaching that in chamber 46, the valve is opened by its spring 41 and its co-acting forces. Grit inside the tank 30 can then fall down through the slits 50 around the baflle 49 and down into the feed hopper, l4, replenishing it without interfering with the pressure conditions in the blast line. y, 4
When the timerSO reaches another predetermined position, the solenoid valve 65 is closed and the valves 10 and H are opened. Conduits 61, 13 and 14 are cut off from their supply of air, while'conduits 68 and 15 are opened to the atmosphere. Airimmediately bleeds out of the upper chamber 44 of the lower dump valve 32, while the check valve H prevents any cushioning efiect from the conduits 73 and 14. When the pressure has dropped only a short way (usually a pound, or less) the air pressure in the chamber 46 closes the lower dump valve 32. The air in the tank 30 fiows to atmosphere out the conduit l through the strainer 16, solenoid valve 11, and muffler l8. Simultaneously the air in the upper dump valve 3| fiows back through the conduit 14 into the conduit 13, through the tank 30 and the conduit 15, and out to atmosphere. When the pressure is low enough (i. e., approaching atmospheric), the upper dump valve 3! opens, and what little air remains is immediately sucked out by the pump 20. In a typical installation the pump 20 draws 300 cubic feet of air per minute. Since the volume of the chamber 30 is only a cubic foot or so, this small pressure differential. will not affect the operation at the head. When the valve 3| opens, the grit stored up in the chamber25 may then fall down again into the chamber 30, completing the cycle.
What is claimed is:
1. An apparatus for continuous abrasive-blasting, comprising a feed hopper for storing abrasive material, an air blast line, a feed valve for feeding said material into said line, an operating head where said material is impinged against a surface, a suction line for withdrawing said material and waste from said surface, a separator for salvaging said material out of said waste, a reclaimer hopper for receiving said withdrawn material, an intermediate hopper between said reclaimer hopper and said feed hopper, a first transfer valve between said reclaimer hopper and said intermediate hopper, a second transfer valve between said intermediate hopper and said feed hopper, a timing device, and an electrical relay operated by said timing device to alternately close said first valve and open said second valve and close said second valve and open said first valve.
2. An apparatus for continuous abrasive-blasting, comprising a feed hopper for storing abrasive material, an air blast line, a feed valve for feeding said material into said line, an operating head where said material is impinged against a surface, a suction line for withdrawing said material and waste from said surface, a separator for salvaging said material out of said waste, a reclaimer hopper for receiving said salvaged material, an intermediate hopper between said reclaimer hopper and said feed hopper, a first transfer valve between said reclaimer hopper and said intermediatehopper, a second transfer valve between said intermediate hopper and said feed hopper, a timing device, an electrical relay operated by said timing device to alternately close said first valve and open said second valve and close said second valve and open said first valve, means to admit air to said intermediate hopper when said first valve is closed, and means to bleed air from said intermediate hopper when said second valve is closed.
3. An apparatus for transferring granular material from a low pressure chamber to a high pressure chamber, comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber, a first valve between said intermediate chamber and said low pressure chamber,-a second valve between said intermediate chamber and said high pressure chamber, a timing device, and means operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
4. The apparatus of claim 3 in which there is mean controlled by said timer for increasing the pressure in said intermediate chamber between the time said first valve closes and the time said second valve opens, and means controlled by said timer for reducing the pressure in said intermediate chamber between the time said second valve closes and the time said first valve opens.
5. An apparatus for transferring granular material from a low pressure chamber to a high pressure chamber, comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber, a first valve between said intermediate chamber and said low pressure chamber, a second valve between said intermediate chamber and said high pressure chamber, a timing device, and an electrical relay control operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
6. An apparatus for transferring granular material from a low pressure chamber to a chamber maintained at high pressure by a high pressure line without upsetting the pressures concerned, comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber; an air operated valve between said intermediate chamber and each of the other said chambers; a first solenoid valve adapted to open for simultaneously admitting air from said high pressure line to the upper of said valves to close it and for admitting air from said high pressure line to said intermediate chamber to build up the pressure therein and for admitting air from said high pressure line to said lower valve to open it when its pressure and the pressure in said intermediate chamber reach a predetermined value, said solenoid valve also being adapted to close for simultaneously cutting off all air from the high pressure line to said valves and said intermediate chamber; a second solenoid valve adapted to open to bleed air from said lower valve to close it; a third solenoid valve adapted to open for bleeding air from said intermediate chamber so that its pressure may be reduced and from said upper valve so that it may open when its pressure drops below a certain point; an electrical circuit to operate said solenoid valves; and a timer which adapted to alternately open said first solenoid valve and simultaneously close said second and third solenoid valves for one part of a cycle, and to close said first solenoid valve and simultaneously open said second and third solenoid valves over another part of said cycle.
7. An apparatus for continuous abrasive-blasting, comprising: a feed hopper for storing abrasive material; an air blast conduit; means for feeding said material into said conduit; means for impinging said material from said conduit against a surface to be treated; means for withdrawing said material from said surface; a reclaimer hopper for receiving said withdrawn material; an intermediate hopper between said reclaimer hopper and said feed hopper; a first transfer valve between said reclaimer hopper and said intermediate hopper; a second transfer valve between said intermediate hopper and said feed hopper; a timing device; and means actuated by said timing device for alternately closing said first valve and opening said second valve, and closing said second valve and opening said first valve.
8. An apparatus for continuous abrasiveblasting, comprising a feed hopper for storing abrasive material; an air blast conduit; means for feeding said material into said conduit; means for impinging said material from said conduit against a surface; means for withdrawing said material from said surface; a reclaimer hopper for receiving said withdrawn material; an intermediate hopper between said reclaimer hopper and said feed hopper; a first transfer valve between said reclaimer hopper and said intermedi ate hopper; a second transfer valve between said intermediate hopper and said feed hopper; a timing device; means actuated by said timing device for alternately closing said first valve and opening said second valve, and closing said second valve and opening said first valve; means for admitting air to said intermediate hopper when said first valve is closed; and means for bleeding air from said intermediate hopper when said second valve is closed.
9. An apparatus for transferring granular material from a first chamber to a second chamber, comprising an intermediate chamber placed between said first and second chambers; a first valve between said intermediate chamber and said first chamber; a second valve between said intermediate chamber and said second chamber; a timing device; and means operated by said timing device for alternately opening said first valve while said second valve is closed and opening said second valve while said first valve is closed.
10. The apparatus of claim 9 in which there is means controlled by said timer for increasing the pressure in said intermediate chamber between the time said first valve closes and the time mediate: chamber between the time said second valve closes and the time said first valve opens.
11. An apparatus for transferring granular material from a low pressure chamber to a chamber maintained at high pressure by a high pressure line, without upsetting the pressures concerned, comprising an intermediate chamber placed below said low pressure chamber and above said high pressure chamber; a pair of pneumatic valves, one being located between said intermediate chamber and each of the other saidchambers to open and close the passages between said chambers; a first control valve adapted when opened to simultaneously admit gas from said high pressure line to the upper of said pneumatic valves to close it and to admit gas from said high pressure line to said intermediate chamber to build up the pressure therein and to admit gas from said high pressure line to the lower of said pneumatic valves to open it when its pressure and the pressure in said intermediate chamber reach a predetermined value, said first control valve also being adapted when closed to simultaneously cut off all gas from the high pressure line to said pneumatic valves and said intermediate chamber; a second control valve adapted when opened to bleed gas from said lower pneumatic valve to close it; a third control valve adapted when opened to bleed gas from said intermediate chamber so that its pressure may be reduced and from said upper pneumatic valve so that it may open when its pressure drops below a certain amount; and timing means adapted to alternately open said first control valve and simultaneously close said second and third control valves for one part of a cycle, and to close said first control valve and simultaneously open said second and third control valves for another part of said cycle.
LEWIS H. BISHOP. JOHN S. FINN.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Niunber Name Date 584,021 Tilghman June 8, 1897 681,867 Bardwell Sept. 3, 1901 1,706,737 Moore Mar. 26, 1929 1,752,664 Forcier Apr. 1, 1930 1,814,616 Boesger July 14, 1931 FOREIGN PATENTS Number Country Date 459,086 France Aug. 25, 1913
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Cited By (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2770924A (en) * 1954-04-01 1956-11-20 William H Mead Instant stop and start blasting device
US2810991A (en) * 1955-02-18 1957-10-29 William H Mead Abrasive blasting apparatus
DE1031172B (en) * 1954-04-01 1958-05-29 William Howard Mead Device for surface treatment
US2867950A (en) * 1955-09-15 1959-01-13 Kent Moore Organization Inc Apparatus for removing carbon from the combustion chamber of an internal combustion engine
US3034263A (en) * 1959-08-07 1962-05-15 Ruric N Mcdaniel Sand blasting apparatus
US3075318A (en) * 1960-09-28 1963-01-29 Allen E Dilliard Abrasive drilling apparatus
US3089285A (en) * 1962-04-19 1963-05-14 Pangborn Corp Abrasive blasting apparatus
US3141264A (en) * 1963-03-25 1964-07-21 Pangborn Corp Blasting with abrasive particles
US3148484A (en) * 1963-01-15 1964-09-15 Jaroco Internat Inc Sandblast generator
US3516204A (en) * 1967-08-21 1970-06-23 Pennwalt Corp Abrading apparatus
US3521407A (en) * 1967-06-13 1970-07-21 Carborundum Co Metal cleaning device
US3675374A (en) * 1970-11-09 1972-07-11 Carborundum Co Direct pressure treating device
US3715838A (en) * 1970-03-06 1973-02-13 Vacu Blast Ltd Apparatus for correcting misprinted matter on sheet material
US3805453A (en) * 1970-12-09 1974-04-23 Schmall Auto & Elekt Sand blasting apparatus
US4222205A (en) * 1977-08-15 1980-09-16 Worldwide Blast Cleaning Limited Blast cleaning machine for pipes and other cylindrical objects
US4232487A (en) * 1978-05-25 1980-11-11 Knox Manufacturing Co. Abrading device
US4375740A (en) * 1978-05-25 1983-03-08 Jpd Manufacturing Limited Portable abrading cabinet device for recycling abrasive blasting system
US4395850A (en) * 1978-05-25 1983-08-02 Jpd Manufacturing Limited Adapter device for tools of an abrasive blasting system
WO1985002356A1 (en) * 1983-11-23 1985-06-06 Aberlan Equipment & Service Co Ltd. Liquid recovery unit
EP0274783A1 (en) * 1986-12-09 1988-07-20 LTC International B.V. Abrasive blasting apparatus
US5056275A (en) * 1989-04-17 1991-10-15 Mitsubishi Jukogyo Kabushiki Kaisha Continuously-operable abrasive blasting apparatus
US5107630A (en) * 1989-09-07 1992-04-28 L.T.C. International B.V. Abrasive blasting apparatus
US5181348A (en) * 1991-04-05 1993-01-26 Target Products, Inc. Abrasive cleaning apparatus
US5207034A (en) * 1990-06-25 1993-05-04 Lynn William R Pliant media blasting device
US5234470A (en) * 1992-02-28 1993-08-10 Lynn William R Media for use in pressurized device and method of farming
US5344472A (en) * 1991-09-12 1994-09-06 Lynn William R Method of recycling media for use in pressurized device
DE9408944U1 (en) * 1994-06-01 1994-09-08 Olren Instr Erich Leibinger Sand whirling device for sandblasting devices
WO1995018685A1 (en) * 1994-01-06 1995-07-13 Ricom Engineering Limited Liquid recovery apparatus
WO1995032839A1 (en) * 1994-06-01 1995-12-07 Macbride, Thomas, Joseph Apparatus for blasting with abrasive particles
US5529589A (en) * 1994-09-02 1996-06-25 Technology Trust Inc. Fiber media blasting material, method of recycling same, and equipment for discharging same
US5545074A (en) * 1994-12-28 1996-08-13 Jacobs; Patrick T. Abrasive blasting system with waste water recycling
US5839951A (en) * 1994-04-22 1998-11-24 Rich Hill, Inc. Separator for blasting apparatus
US6152810A (en) * 1996-07-05 2000-11-28 Pct, Inc. Blasting media apparatus
US6884070B2 (en) * 2001-03-23 2005-04-26 Ferton Holding S.A. Powder reservoir for a dental abrasive sprayer
US20160059385A1 (en) * 2014-08-28 2016-03-03 Fuji Jukogyo Kabushiki Kaisha Blast treatment device and blast treatment method
US20160059386A1 (en) * 2014-08-28 2016-03-03 Fuji Jukogyo Kabushiki Kaisha Blast treatment device and blast treatment method

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FR459086A (en) * 1913-02-15 1913-10-25 Lentz & Zimmermann Sandblasting apparatus
US1706737A (en) * 1923-09-19 1929-03-26 American Foundry Equip Co Sand-blast tank and filling valve
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US584021A (en) * 1897-06-08 Sand-blasting apparatus
US681867A (en) * 1896-01-24 1901-09-03 Yale & Towne Mfg Co Sand-blast machine.
FR459086A (en) * 1913-02-15 1913-10-25 Lentz & Zimmermann Sandblasting apparatus
US1706737A (en) * 1923-09-19 1929-03-26 American Foundry Equip Co Sand-blast tank and filling valve
US1814616A (en) * 1926-10-09 1931-07-14 W W Sly Mfg Company Pressure operated sand blast valve
US1752664A (en) * 1929-07-27 1930-04-01 George J Forcier Apparatus for cleaning walls

Cited By (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2770924A (en) * 1954-04-01 1956-11-20 William H Mead Instant stop and start blasting device
DE1031172B (en) * 1954-04-01 1958-05-29 William Howard Mead Device for surface treatment
US2810991A (en) * 1955-02-18 1957-10-29 William H Mead Abrasive blasting apparatus
US2867950A (en) * 1955-09-15 1959-01-13 Kent Moore Organization Inc Apparatus for removing carbon from the combustion chamber of an internal combustion engine
US3034263A (en) * 1959-08-07 1962-05-15 Ruric N Mcdaniel Sand blasting apparatus
US3075318A (en) * 1960-09-28 1963-01-29 Allen E Dilliard Abrasive drilling apparatus
US3089285A (en) * 1962-04-19 1963-05-14 Pangborn Corp Abrasive blasting apparatus
US3148484A (en) * 1963-01-15 1964-09-15 Jaroco Internat Inc Sandblast generator
US3141264A (en) * 1963-03-25 1964-07-21 Pangborn Corp Blasting with abrasive particles
US3521407A (en) * 1967-06-13 1970-07-21 Carborundum Co Metal cleaning device
US3516204A (en) * 1967-08-21 1970-06-23 Pennwalt Corp Abrading apparatus
US3715838A (en) * 1970-03-06 1973-02-13 Vacu Blast Ltd Apparatus for correcting misprinted matter on sheet material
US3675374A (en) * 1970-11-09 1972-07-11 Carborundum Co Direct pressure treating device
US3805453A (en) * 1970-12-09 1974-04-23 Schmall Auto & Elekt Sand blasting apparatus
US4222205A (en) * 1977-08-15 1980-09-16 Worldwide Blast Cleaning Limited Blast cleaning machine for pipes and other cylindrical objects
US4232487A (en) * 1978-05-25 1980-11-11 Knox Manufacturing Co. Abrading device
US4375740A (en) * 1978-05-25 1983-03-08 Jpd Manufacturing Limited Portable abrading cabinet device for recycling abrasive blasting system
US4395850A (en) * 1978-05-25 1983-08-02 Jpd Manufacturing Limited Adapter device for tools of an abrasive blasting system
WO1985002356A1 (en) * 1983-11-23 1985-06-06 Aberlan Equipment & Service Co Ltd. Liquid recovery unit
EP0274783A1 (en) * 1986-12-09 1988-07-20 LTC International B.V. Abrasive blasting apparatus
US4984397A (en) * 1986-12-09 1991-01-15 Ltc International B.V. Abrasive blasting apparatus
US5056275A (en) * 1989-04-17 1991-10-15 Mitsubishi Jukogyo Kabushiki Kaisha Continuously-operable abrasive blasting apparatus
US5107630A (en) * 1989-09-07 1992-04-28 L.T.C. International B.V. Abrasive blasting apparatus
US5207034A (en) * 1990-06-25 1993-05-04 Lynn William R Pliant media blasting device
US5181348A (en) * 1991-04-05 1993-01-26 Target Products, Inc. Abrasive cleaning apparatus
US5344472A (en) * 1991-09-12 1994-09-06 Lynn William R Method of recycling media for use in pressurized device
US5234470A (en) * 1992-02-28 1993-08-10 Lynn William R Media for use in pressurized device and method of farming
WO1995018685A1 (en) * 1994-01-06 1995-07-13 Ricom Engineering Limited Liquid recovery apparatus
US5839951A (en) * 1994-04-22 1998-11-24 Rich Hill, Inc. Separator for blasting apparatus
WO1995032839A1 (en) * 1994-06-01 1995-12-07 Macbride, Thomas, Joseph Apparatus for blasting with abrasive particles
DE9408944U1 (en) * 1994-06-01 1994-09-08 Olren Instr Erich Leibinger Sand whirling device for sandblasting devices
US5529589A (en) * 1994-09-02 1996-06-25 Technology Trust Inc. Fiber media blasting material, method of recycling same, and equipment for discharging same
US5545074A (en) * 1994-12-28 1996-08-13 Jacobs; Patrick T. Abrasive blasting system with waste water recycling
US6152810A (en) * 1996-07-05 2000-11-28 Pct, Inc. Blasting media apparatus
US6884070B2 (en) * 2001-03-23 2005-04-26 Ferton Holding S.A. Powder reservoir for a dental abrasive sprayer
US20160059385A1 (en) * 2014-08-28 2016-03-03 Fuji Jukogyo Kabushiki Kaisha Blast treatment device and blast treatment method
US20160059386A1 (en) * 2014-08-28 2016-03-03 Fuji Jukogyo Kabushiki Kaisha Blast treatment device and blast treatment method
US10118275B2 (en) * 2014-08-28 2018-11-06 Subaru Corporation Blast treatment device and blast treatment method
US10144112B2 (en) * 2014-08-28 2018-12-04 Subaru Corporation Blast treatment device and blast treatment method

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