US3664824A - Agglomerated metal shot - Google Patents
Agglomerated metal shot Download PDFInfo
- Publication number
- US3664824A US3664824A US787278A US3664824DA US3664824A US 3664824 A US3664824 A US 3664824A US 787278 A US787278 A US 787278A US 3664824D A US3664824D A US 3664824DA US 3664824 A US3664824 A US 3664824A
- Authority
- US
- United States
- Prior art keywords
- powder
- shot
- adhesive
- aqueous
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F42—AMMUNITION; BLASTING
- F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
- F42B7/00—Shotgun ammunition
- F42B7/02—Cartridges, i.e. cases with propellant charge and missile
- F42B7/04—Cartridges, i.e. cases with propellant charge and missile of pellet type
- F42B7/046—Pellets or shot therefor
Definitions
- This invention is concerned with the production of metal shot from fine metallic powders such as lead and iron.
- a process is provided for agglomerating the powder into balls of good sphericity, low porosity and acceptable strength, without the use of expensive dies or molds, or large shot towers.
- the resulting balls are held together by a cold-welding effect between particles or by an adhesive.
- the invention provides strong spherical agglomerates of metal powder prepared in two-phase liquid systems, with the dispersed liquid phase preferentially wetting the powder being aqueous or an aqueous-base adhesive.
- the agglomerated powder becomes bound together by the adhesive or by a cold-welding effect on impact shaping.
- the adhesive may be water-sensitive causing the pellet to disintegrate slowly in a moist environment.
- metal shot has been prepared by melting and casting, by powder metallurgy techniques, or by shot tower techniques where molten metal is sprayed into a cooling fluid and shaped by surface tension effect. It has been diflicult to obtain good sphericity without a surface finishing or grinding step, and the equipment needed for large volume production is quite extensive.
- An object of the present invention is to provide a process for uniting and shaping metal powder into pellets having good sphericity, strength and density. Another object is to provide such pellets of heavy metal powder united by an adhesive or by a cold-welding or -forging effect. A further object is to provide such pellets which will slowly disintegrate in a moist or aqueous environment.
- metal shot that would disintegrate under moist conditions would be useful to prevent the ingestion and retention of spent shot by feeding water fowl and thus reduce the incidence of poisoning that is believed to occur when massive shot composed of toxic materials such as lead, is ingested. Should such a pellet be picked up it would disintegrate reasonably quickly in the birds crop and pass through the digestive tract rapidly.
- the shot should be as dense as possible and have suflicient strength (in compression) to withstand the acceleration in the gun barrel, as well as the impact of hitting the target.
- the process of the invention includes adding the metal powder and an aqueous liquid which wets the powder to an inert organic liquid and agitating to form agglomerates of powder plus aqueous liquid the agglomerates then being forced to undergo a continued impact and ricocheting action.
- This may suitably be accomplished by enclosing the mixture in an incompletely filled container having rounded inner surfaces.
- the container is then shaken at a frequency and in a pattern causing agglomerates of the powder and aqueous liquid to undergo an impact and ricocheting action against the container walls. This shaking is prolonged until the desired balls have been produced. This shaking action is more fully described in Canadian application 971,606, filed Sept. 28, 1966.
- the non-aqueous or organic liquid can be any low viscosity compound or mixture substantially inert with respect to the powder and aqueous liquid, and should form the continuous phase.
- Suitable liquids include petroleum spirits, e.g. Varsol (trademark), halogenated hydrocarbons, aromatic hydrocarbons, silicone fluids and light petroleum oils.
- the aqueous liquid should preferentially wet the metal powder. It may be necessary or desirable to treat the particle surface to render it preferentially wetted by water, e.g. by polar organic compounds substantially insoluble in the organic liquid such as ethanolamine, wetting agents (e.g. soaps detergents and glycerine, or to add such polar compounds to the water phase.
- the aqueous liquid can be more viscous than the organic liquid-and may comprise a dissolved or dispersed adhesive.
- the proportions of the aqueous liquid are not critical. There should be sufficient to agglomerate the powder but insuflicient to form large soft masses. Preferably about 5 to by volume of the metal powder is used.
- the size of the final pellets is determined by the amount of aqueous liquid used and also by the factors mentioned in the following paragraph.
- the container should be only partially filled, e.g. to about 20 to by vol. to allow a good translational motion of the agglomerates.
- the container geometry, shaking pattern and frequently, loading and the organic liquid viscosity should be selected to give thedesired impact and ricocheting resonance.
- the container walls should be relatively inert to the organic and especially to the aqueous liquid. Tetrafluoroethylene polymers make a desirable wall surface.
- the metal powder is desirably lead or iron but other metals such as copper, aluminum, zinc, etc. may be used. Where no adhesive is used the metal powder should be susceptible to cold welding. Lead, copper and alloys such as Woods metal can be cold-welded under the impact.
- the particle size is not critical and can be the size used for pigments, powder metallurgy, fillers and other applications. A preferred powder size is about 01-100 micron diameter.
- the powder loading should be less than about 35% by vol. of the organic liquid, or less than that giving an insufficiently fluid system.
- the adhesive is not critical but should be chosen to give a suitable disintegration time and strength.
- the amount of the adhesive may range up to about 50 or more percent by volume based on the metal powder. A preferred range is 10-20% vol.
- Adhesives in dispersed or dissolved form which have been used are polyvinyl acetate, commercial mucilage, polyvinyl alcohol, starch, white and orange shellac, sodium silicate, animal glue and dextrin (in order of decreasing disintegration times in water).
- Thermosetting or polymerizable adhesives dissolved or dispersed in water can also be used.
- EXAMPLE 1 The following ingredients were added to a polytetrafluoroethylene-lined cylindrical container (capacity cc.) having rounded ends and shaken in a three dimensional pattern in a Pica Blender for 10 minutes.
- Powdered lead 200 mesh
- Petroleum aliphatic solvent Varsol
- Polyvinyl acetate emulsion 55% solids)-1.6 cc.
- Lead powder (325 mesh)75 gm. Petroleum aliphatic solvent (Varsol)-50 ml. Polyvinyl acetate emulsion (48% solids in water)30 ml.
- Iron powder (325 mesh)-18 gm. Petroleum aliphatic solvent (Varsol)-50 ml. Commercial mucilage (45% solids in water)--1.9 ml.
- the crushing strengths of the spheres for Examples 2 and 3 were approximately proportional to the square of the diameter indicating uniform binding throughout the pellet. Crushing strengths (calculated for one inch pellets) ranged from about 1200-2400 lbs. The size of the pellets was varied slightly by changing the speed of shaking and/ or the amount and composition of the adhesive.
- More permanent bonding of the primary particles is available through the selection of suitable adhesives for each metal, the use of solvents (as bridging liquid) capable of allowing recrystallization of the adhesive solids at the junction points, the use of clean or activated particle surfaces and/ or through a final sintering or heat treatment.
- Bird shot pellets which will disintegrate in a moist environment, comprising agglomerated powdered lead bonded by a minor amount of a water-sensitive adhesive.
- Bird shot pellets which will disintegrate in a moist environment, comprising agglomerated powdered iron bonded by a minor amount of water-sensitive adhesive.
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Adornments (AREA)
Abstract
AGGLOMERATED METAL SHOT PREPARATION BY ADDING METAL POWDER AND AQUEOUS FLUID TO A NON-AQUEOUS LIQUID PHASE, AGITATING TO AGGLOMERATE POWDER AND AQUEOUS FLUID, AND IMPACTING AND RICOCHETING THE AGGLOMERATES UNTIL STRONG PELLETS ARE FORMED (BY COLD-WELDING OR AQUEOUS ADHESIVE) E.G. GIVING BIRD SHOT WHICH MAY BE WATER-DECOMPOSABLE.
Description
3,654,824 Patented May 23, 1972 Int. e1. 1322: 9/00 U.S. CL 75-.5 R 2 Claims ABSTRACT OF THE DISCLOSURE Agglomerated metal shot preparation by adding metal powder and aqueous fluid to a non-aqueous liquid phase, agitating to agglomerate powder and aqueous fluid, and impacting and ricocheting the agglomerates until strong pellets are formed (by cold-welding or aqueous adhesive) e.g. giving bird shot which may be water-decomposable.
This invention is concerned with the production of metal shot from fine metallic powders such as lead and iron. A process is provided for agglomerating the powder into balls of good sphericity, low porosity and acceptable strength, without the use of expensive dies or molds, or large shot towers. The resulting balls are held together by a cold-welding effect between particles or by an adhesive.
The invention provides strong spherical agglomerates of metal powder prepared in two-phase liquid systems, with the dispersed liquid phase preferentially wetting the powder being aqueous or an aqueous-base adhesive. The agglomerated powder becomes bound together by the adhesive or by a cold-welding effect on impact shaping. For bird shot, the adhesive may be water-sensitive causing the pellet to disintegrate slowly in a moist environment.
Previously such metal shot has been prepared by melting and casting, by powder metallurgy techniques, or by shot tower techniques where molten metal is sprayed into a cooling fluid and shaped by surface tension effect. It has been diflicult to obtain good sphericity without a surface finishing or grinding step, and the equipment needed for large volume production is quite extensive.
An object of the present invention is to provide a process for uniting and shaping metal powder into pellets having good sphericity, strength and density. Another object is to provide such pellets of heavy metal powder united by an adhesive or by a cold-welding or -forging effect. A further object is to provide such pellets which will slowly disintegrate in a moist or aqueous environment.
It has recently been suggested that metal shot that would disintegrate under moist conditions would be useful to prevent the ingestion and retention of spent shot by feeding water fowl and thus reduce the incidence of poisoning that is believed to occur when massive shot composed of toxic materials such as lead, is ingested. Should such a pellet be picked up it would disintegrate reasonably quickly in the birds crop and pass through the digestive tract rapidly. For ballistic reasons the shot should be as dense as possible and have suflicient strength (in compression) to withstand the acceleration in the gun barrel, as well as the impact of hitting the target.
The process of the invention includes adding the metal powder and an aqueous liquid which wets the powder to an inert organic liquid and agitating to form agglomerates of powder plus aqueous liquid the agglomerates then being forced to undergo a continued impact and ricocheting action. This may suitably be accomplished by enclosing the mixture in an incompletely filled container having rounded inner surfaces. The container is then shaken at a frequency and in a pattern causing agglomerates of the powder and aqueous liquid to undergo an impact and ricocheting action against the container walls. This shaking is prolonged until the desired balls have been produced. This shaking action is more fully described in Canadian application 971,606, filed Sept. 28, 1966.
The non-aqueous or organic liquid can be any low viscosity compound or mixture substantially inert with respect to the powder and aqueous liquid, and should form the continuous phase. Suitable liquids include petroleum spirits, e.g. Varsol (trademark), halogenated hydrocarbons, aromatic hydrocarbons, silicone fluids and light petroleum oils.
The aqueous liquid should preferentially wet the metal powder. It may be necessary or desirable to treat the particle surface to render it preferentially wetted by water, e.g. by polar organic compounds substantially insoluble in the organic liquid such as ethanolamine, wetting agents (e.g. soaps detergents and glycerine, or to add such polar compounds to the water phase. The aqueous liquid can be more viscous than the organic liquid-and may comprise a dissolved or dispersed adhesive. The proportions of the aqueous liquid are not critical. There should be sufficient to agglomerate the powder but insuflicient to form large soft masses. Preferably about 5 to by volume of the metal powder is used. The size of the final pellets is determined by the amount of aqueous liquid used and also by the factors mentioned in the following paragraph.
The container should be only partially filled, e.g. to about 20 to by vol. to allow a good translational motion of the agglomerates. The container geometry, shaking pattern and frequently, loading and the organic liquid viscosity should be selected to give thedesired impact and ricocheting resonance. The container walls should be relatively inert to the organic and especially to the aqueous liquid. Tetrafluoroethylene polymers make a desirable wall surface.
By passing or recycling the organic liquid-plus-agglomerates through a series of rapidly rotating blades or vanes, sufficient impact and ricocheting action on the pellets may be achieved for some purposes. However, shaking in the container is preferred.
The metal powder is desirably lead or iron but other metals such as copper, aluminum, zinc, etc. may be used. Where no adhesive is used the metal powder should be susceptible to cold welding. Lead, copper and alloys such as Woods metal can be cold-welded under the impact. The particle size is not critical and can be the size used for pigments, powder metallurgy, fillers and other applications. A preferred powder size is about 01-100 micron diameter. The powder loading should be less than about 35% by vol. of the organic liquid, or less than that giving an insufficiently fluid system.
The adhesive is not critical but should be chosen to give a suitable disintegration time and strength. The amount of the adhesive may range up to about 50 or more percent by volume based on the metal powder. A preferred range is 10-20% vol. Adhesives in dispersed or dissolved form which have been used are polyvinyl acetate, commercial mucilage, polyvinyl alcohol, starch, white and orange shellac, sodium silicate, animal glue and dextrin (in order of decreasing disintegration times in water). Thermosetting or polymerizable adhesives dissolved or dispersed in water can also be used.
The following examples are illustrative.
EXAMPLE 1 The following ingredients were added to a polytetrafluoroethylene-lined cylindrical container (capacity cc.) having rounded ends and shaken in a three dimensional pattern in a Pica Blender for 10 minutes.
Powdered lead (200 mesh)26 gm. Petroleum aliphatic solvent (Varsol)-30 cc. Polyvinyl acetate emulsion (55% solids)-1.6 cc.
EXAMPLE 2 Similar to Example 1 except the following proportions and a Spex Mixer Mill were used:
Lead powder (325 mesh)75 gm. Petroleum aliphatic solvent (Varsol)-50 ml. Polyvinyl acetate emulsion (48% solids in water)30 ml.
Shaking for 10 minutes gave quite uniform spheres about 0.12 inch diameter and of density 8 gm./cc. Disintegration time in water varied from several days to two weeks.
EXAMPLE 3 Similar to Example 1 except the following ingredients were used.
Iron powder (325 mesh)-18 gm. Petroleum aliphatic solvent (Varsol)-50 ml. Commercial mucilage (45% solids in water)--1.9 ml.
Shaking for 10 min. gave quite uniform spheres about 0.06 inch diameter and of density gm./cc.
The crushing strengths of the spheres for Examples 2 and 3 were approximately proportional to the square of the diameter indicating uniform binding throughout the pellet. Crushing strengths (calculated for one inch pellets) ranged from about 1200-2400 lbs. The size of the pellets was varied slightly by changing the speed of shaking and/ or the amount and composition of the adhesive.
Further examples with lead and adhesive showed that with less adhesive considerably increased density and a more permanent structure were obtained. In the absence of adhesive, bonds were produced apparently by a coldwelding or -forging effect. Densities as high as 10 were obtained indicating a void volume of about 10% only. Although these shot were very strong, accurate crushing strengths were difiicult to estimate owing to plastic flow.
More permanent bonding of the primary particles (and more strength) is available through the selection of suitable adhesives for each metal, the use of solvents (as bridging liquid) capable of allowing recrystallization of the adhesive solids at the junction points, the use of clean or activated particle surfaces and/ or through a final sintering or heat treatment.
We claim:
1. Bird shot pellets which will disintegrate in a moist environment, comprising agglomerated powdered lead bonded by a minor amount of a water-sensitive adhesive.
2. Bird shot pellets which will disintegrate in a moist environment, comprising agglomerated powdered iron bonded by a minor amount of water-sensitive adhesive.
References Cited UNITED STATES PATENTS 2,592,421 4/ 1952 Hellman 2641 11 3,102,024- 8/ 1963 Knapp -.5 R 3,463,637 8/1969 Foerster 75-.5 R 2,986,772 6/1961 Patton, Jr. et al 75-.5 R 2,995,780 8/1961 West et a1. 264-111 L. DEWAYNE RUTLEDGE, Primary Examiner W. W. STALLARD, Assistant Examiner US. Cl. X.R.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA11770 | 1968-02-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3664824A true US3664824A (en) | 1972-05-23 |
Family
ID=4084012
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US787278A Expired - Lifetime US3664824A (en) | 1968-02-06 | 1968-12-26 | Agglomerated metal shot |
Country Status (2)
Country | Link |
---|---|
US (1) | US3664824A (en) |
CA (1) | CA890833A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3900317A (en) * | 1973-03-06 | 1975-08-19 | Canadian Patents Dev | Fe-sn-cu-pb sintered composite metal article and process |
US3987730A (en) * | 1973-03-06 | 1976-10-26 | Canadian Patents And Development Limited | Iron and lead-containing composite metal shot |
US4027594A (en) * | 1976-06-21 | 1977-06-07 | Olin Corporation | Disintegrating lead shot |
FR2517819A1 (en) * | 1981-12-09 | 1983-06-10 | Herstal Sa | LEAD GRAIN IMPROVEMENT FOR HUNTING AMMUNITION |
US4947754A (en) * | 1987-12-10 | 1990-08-14 | General Dynamics Corporation, Pomona Division | System and method for penetrating orbiting targets |
US5076812A (en) * | 1990-06-06 | 1991-12-31 | Arcanum Corporation | Coal treatment process and apparatus therefor |
US20180037973A1 (en) * | 2016-08-08 | 2018-02-08 | Mt2, Llc | Method for the treatment of metallic particles and objects contaminated with metallic particles |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2320456B (en) | 1996-12-18 | 2001-09-05 | Fip Holdings Ltd | Polymer processing method |
GB2340835B (en) | 1998-08-26 | 2003-01-15 | Pvax Ploymers Ltd | PVA-containing compositions |
GB0005016D0 (en) | 2000-03-01 | 2000-04-26 | Jumik Technologies Limited | PVA-Containing compositions |
-
1968
- 1968-02-06 CA CA890833A patent/CA890833A/en not_active Expired
- 1968-12-26 US US787278A patent/US3664824A/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3900317A (en) * | 1973-03-06 | 1975-08-19 | Canadian Patents Dev | Fe-sn-cu-pb sintered composite metal article and process |
US3987730A (en) * | 1973-03-06 | 1976-10-26 | Canadian Patents And Development Limited | Iron and lead-containing composite metal shot |
US4027594A (en) * | 1976-06-21 | 1977-06-07 | Olin Corporation | Disintegrating lead shot |
JPS53700A (en) * | 1976-06-21 | 1978-01-06 | Olin Corp | Collapsible metallic canister pellet |
FR2517819A1 (en) * | 1981-12-09 | 1983-06-10 | Herstal Sa | LEAD GRAIN IMPROVEMENT FOR HUNTING AMMUNITION |
US4947754A (en) * | 1987-12-10 | 1990-08-14 | General Dynamics Corporation, Pomona Division | System and method for penetrating orbiting targets |
US5076812A (en) * | 1990-06-06 | 1991-12-31 | Arcanum Corporation | Coal treatment process and apparatus therefor |
US20180037973A1 (en) * | 2016-08-08 | 2018-02-08 | Mt2, Llc | Method for the treatment of metallic particles and objects contaminated with metallic particles |
US10781504B2 (en) * | 2016-08-08 | 2020-09-22 | Mt2, Llc | Method for the treatment of metallic particles and objects contaminated with metallic particles |
US10837082B2 (en) | 2016-08-08 | 2020-11-17 | Mt2, Llc | Method for the treatment of an object contaminated with metallic particles |
Also Published As
Publication number | Publication date |
---|---|
CA890833A (en) | 1972-01-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3664824A (en) | Agglomerated metal shot | |
US5258151A (en) | Molding composition for the production of inorganic sintered products | |
US4027594A (en) | Disintegrating lead shot | |
WO1993022089A1 (en) | High density projectile and method of making | |
KR102011166B1 (en) | Silver-coated copper alloy powder and method for manufacturing same | |
US4106932A (en) | Lubricants for powdered metals, and powdered metal compositions containing said lubricants | |
CA2429093A1 (en) | Powder additive for powder metallurgy, iron-based powder mixture for powder metallurgy, and method for manufacturing the same | |
US5766304A (en) | Iron-base powder mixture for powder metallurgy and manufacturing method therefor | |
US4002474A (en) | Lubricants for powdered metals | |
JP2003526693A (en) | Improved metallurgical composition containing binder / lubricant and method of making same | |
US3900317A (en) | Fe-sn-cu-pb sintered composite metal article and process | |
JPH03162502A (en) | Manufacture of iron base powder mixed material for powder metallurgy | |
US3987730A (en) | Iron and lead-containing composite metal shot | |
US3368004A (en) | Forming balls from powder | |
JPH0234701A (en) | Tantalum powder granulated body | |
BRPI0807180A2 (en) | DIFFUSION ALLOY IRON POWDER | |
JPH0442441B2 (en) | ||
DE60128128T2 (en) | METAL AND METAL OXYDE CONTAINING GRANULATE AND METHOD OF PREPARING THEREOF | |
JPS54115237A (en) | Magnetic toner and production of the same | |
JPS5946124A (en) | Preparation of microcapsule | |
US3497345A (en) | Titanium dioxide coated pesticidal granule | |
JP2004190051A (en) | Iron based powdery mixture for power metallurgy, and production method therefor | |
KR101916761B1 (en) | The manufacturing method of silver powder with high specific surface | |
US4256521A (en) | Porous metal agglomerates | |
JPH0367737B2 (en) |