Process and apparatus for comminuting particle rubber
View Patent ↗A process and apparatus for comminuting rubber particles. In this process and apparatus rubber particles at a temperature below the glass transition temperature are introduced into a comminuting device concurrent with the introduction of an inert gas coolant at a temperature below about −75° F. The rubber particles are comminuted in the comminuting device at a rate proportional to the average particle size of the introduced rubber particles to an average size within the range of crumb or powder rubber particles.
1. A process of comminuting rubber particles comprising:
(a) introducing rubber particles, at a temperature below the glass transition temperature, into a comminuting device;
(b) concurrently introducing an inert gas coolant into said comminuting device at an average overall temperature no higher than about −100° F.; and
(c) comminuting said rubber particles, by impact of said rubber particles in a variable gap, said variable gap being an adjustable width between a stationary outer casing and rotating impact blades disposed on a variable rotational speed rotor, at to a comminuted average particle size within the range of powder rubber particles.
2. A process in accordance with claim 1 wherein said inert coolant is introduced into said comminuting device at an average overall temperature in the range of between about −90° F. and about −125° F.
3. A process in accordance with claim 1 wherein said inert gas coolant is introduced into said comminuting device in two separate streams.
4. A process in accordance with claim 3 wherein said first inert gas coolant stream is introduced with said rubber particles and said second inert gas coolant stream is introduced through nozzles provided on said comminuting device.
5. A process in accordance with claim 3 wherein a first stream of said inert gas coolant is introduced with said rubber particles and a second stream of said inert gas coolant is introduced separately from said rubber particles into said comminuting device.
6. A process in accordance with claim 1 wherein said rubber particles introduced into said comminuting device have an average particle size in the range of between about −⅜ inch and about 40 mesh.
7. A process in accordance with claim 1 wherein said comminuted powder rubber has an average particle size no greater than about 80 mesh.
8. A process in accordance with claim 1 wherein said comminuting rate is varied by varying the volumetric rate of introduction of said inert gas coolant.
9. A process in accordance with claim 1 wherein said comminuting rate is varied by varying the average temperature of said inert gas coolant.
10. A process in accordance with claim 1 wherein said comminution rate is varied by varying said adjustable width between said stationary casing and said impact rotor.
11. A process in accordance with claim 1 wherein said comminution rate is varied by varying the rotational velocity of said rotor.
12. A process in accordance with claim 1 comprising introducing a cryogenic liquid into said comminuting device.
13. A process in accordance with claim 1 wherein said inert gas coolant is gaseous nitrogen.
14. A process of comminuting rubber particles comprising:
introducing a rubber particle feedstock, having an average particle size in the range of between about −⅜ inch and about 40 mesh, at a temperature below the glass transition temperature of the feedstock, into an impact mill;
introducing, concurrently with the introduction of said rubber particle feedstock, a coolant fluid selected from the group consisting of liquid nitrogen, gaseous nitrogen at a temperature in the range of between about −95° F. and about −115° F. and mixtures thereof into said impact mill;
separately introducing gaseous nitrogen, at a temperature below ambient, into said impact mill; and
comminuting said rubber particle feedstock by impact in a variable gap provided between a variable rotational speed rotor, provided with a plurality of blades, and a stationary conically shaped casing wherein powder rubber having an average particle size in the range of between about 80 mesh and about 200 mesh is provided.
15. An apparatus for comminuting rubber particles comprising:
means for introducing rubber particles, at a temperature below the glass transition temperature, into a comminution device;
means for concurrently introducing an inert gas coolant into said comminution device at an average overall temperature no higher than about −100° F.; and
a comminuting device provided with a variable gap between a stationary outer casing and a variable rotational speed impact rotor provided with a plurality of impact blades wherein said rubber particles are comminuted by the impact of said rubber particles between said impact blades and said stationary casing to an average size within the range of powder rubber sized particles.
16. An apparatus in accordance with claim 15 wherein said inert gas coolant is introduced into said comminuting device at an average overall temperature in the range of between about −90° F. and about −125° F.
17. An apparatus in accordance with claim 16 wherein said means for introducing inert gas coolant into said comminuting device comprises a first means for introducing an inert gas into said comminuting means and a second means for introducing an inert gas into said comminuting means.
18. An apparatus in accordance with claim 15 wherein said rubber particles provided by said introducing means have an average particle size in the range of between about −⅜ inch and about 40 mesh.
19. An apparatus in accordance with claim 15 wherein said comminuting device produces powder rubber having an average particle size in the range of between about 80 mesh and about 200 mesh.
20. An apparatus in accordance with claim 15 wherein said comminuting device comminutes said rubber particles as a function of the volumetric rate of introduction of said inert gas coolant into said comminuting device.
21. An apparatus in accordance with claim 15 wherein said comminuting device comminutes said rubber particles as a function of the average temperature of said inert gas coolant.
22. An apparatus in accordance with claim 15 wherein said rate of comminution in said communition device varies as a function of said variable gap width between said impact rotor and said stationary casing.
23. An apparatus in accordance with claim 15 wherein said comminution device rate of comminution varies as a function of the rotational speed of said impact rotor.
24. An apparatus in accordance with claim 15 comprising means for introducing a cryogenic liquid into said comminuting device.
25. An apparatus in accordance with claim 15 wherein said inert gas coolant is gaseous nitrogen.
26. An apparatus for comminuting rubber particles comprising:
means for introducing a rubber particle feedstock, having an average particle size in the range of between about −⅜ inch and about 40 mesh, at a temperature below the glass transition temperature of said rubber particles into an impact mill;
means for introducing, with said rubber particle feedstock, a coolant fluid selected from the group consisting of liquid nitrogen, gaseous nitrogen at a temperature in the range of between about −95° F. and about −115° F. and mixtures thereof into said impact mill;
means for separately introducing gaseous nitrogen, at a temperature below ambient, into said impact mill; and
said impact mill is provided with a variable gap between a stationary conically shaped casing and a variable rotational speed conically shaped rotor for comminuting said rubber particle feedstock therebetween to an average particle size in the range of between about 80 mesh and about 200 mesh.