Particulate compositions of particulate metal and polymer binder
a technology which is applied in the field of particulate metal and polymer binder, can solve the problems of increased lead levels in the ecosystem and food chain, difficulty in maintaining two or more metal powders in a desired proportion prior to the molding of the projectile, and insufficient flow of metal powders of such small particle siz
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example a
Preparation of Particulate Metal Mixture
[0076] A particulate metal mixture was prepared by mixing 5443 grams of particulate tungsten (having an average particle size of 5 μm), and 1361 grams of particulate tin (having an average particle size of 12 μm) in a TURBULA shaker-mixer (available commercially from Glenn Mills, Inc.). The particulate tungsten and tin were mixed in the mixer for 20 minutes, and the resulting particulate metal mixture was determined to be substantially homogenously mixed by means of visual inspection. The particulate metal mixture of tungsten and tin was substantially dry and free flowing.
[0077] The average particle sizes of the particulate tungsten and particulate tin, from which the particulate metal mixture was prepared, were each determined in accordance with ASTM B 822. The particulate tungsten was obtained commercially from H.C. Stark Inc., and the particulate tin was obtained commercially from OMG Americas Inc.
example b
Preparation of Slurry
[0078] A slurry was prepared by mixing 5 grams of Antifoam 221 silicone-glycol emulsion (obtained commercially from Dow Corning Corporation) with 1270 grams of water, and then 91 grams of polyvinyl alcohol was added to the mixture of water and defoamer. The mixture of water, polyvinyl alcohol and defoamer was thoroughly mixed with an impeller. Next, 6803 grams of the particulate metal mixture of Example A was added to the mixture of water, polyvinyl alcohol and defoamer to form the slurry, which was continuously mixed using an impeller.
example c
Preparation of the Particulate Composition
[0079] The slurry of Example B, while continually being stirred with an impeller, was passed through a spray drier comprising a dual-fluid nozzle, at a rate of 907 grams / min. The spray drier was operated at an inlet temperature of 260° C. and an outlet temperature of 149° C.
[0080] The particulate composition resulting from the spray drying operation had: an average particle size of 75 μm (as determined in accordance with ASTM B 214); a Hall flow of less than 25 seconds / 50 g (as determined in accordance with ASTM B 213); and an apparent density of approximately 4 g / cm3 (as determined in accordance with ASTM B 329).
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