referring to the drawing , a rotary mill 1 comprises a housing 10 , a material delivery system 12 and an exhaust fan 14 . the housing 10 comprises a rotor 16 , a primary reduction chamber 18 , a secondary reduction chamber 20 and an outlet chamber 22 , as shown in fig1 . the primary reduction chamber 18 comprises an inlet opening 24 , an intake guide surface 26 and a plurality of shatter bars 28 . the inlet opening 24 provides access to the interior of the housing 10 for incoming material and for airflow generated by the exhaust fan 14 . in this embodiment , the inlet opening 24 is positioned beneath the material delivery system 12 . the intake guide surface 26 is arranged to direct material from the inlet opening 24 into the swept area of the rotor 16 . the plurality of shatter bars 28 are arranged to further reduce particles deflected by the rotor 16 and direct these particles back toward the rotor 16 as described below . the secondary reduction chamber 20 is connected to the primary reduction chamber 18 by a curved portion 30 as described below . the secondary reduction chamber 18 includes reduction elements 32 positioned between the secondary reduction chamber 20 and the outlet chamber 22 , arranged such that particles above a given size are prevented from entering the outlet chamber 22 . the reduction elements 32 may comprise staggered bars , perforated metal plates , wire screens or combinations thereof . the outlet chamber 22 comprises an outlet opening 34 in one wall of the chamber 22 , a fan control flap 36 and a lower material outlet 38 . the outlet 34 comprises the exit from the housing 10 for fine particles and for airflow generated by the exhaust fan 14 as described below which generates an airflow through the chambers by injecting air at the inlet 24 as indicated at 14 a . the lower material outlet 38 comprises a balanced door 40 situated at the base of the outlet chamber 22 for removal of heavy particles . specifically , once a mass of material equal to the balance weight has gathered , the balanced door 40 opens and expels the material from the housing 10 . the fan control flap 36 comprises a movable baffle 42 located within the outlet chamber 22 for controlling airflow through the housing 10 so that the amount and size of particles drawn off at the outlet 34 and the lower material outlet 38 may be varied as described below . the rotor 16 is arranged for rotation within the housing 10 and is driven by a motor , the details of which are not shown as these will be obvious to one skilled in the art . the rotor 16 includes peripheral impact hammers 44 and is situated below the intake guide surface 26 . while a rotor that exposes more blades will move more air , durable construction and suitable mass for reducing incoming material conflict with ideal air moving capabilities . however , generation of airflow by the rotor 16 is not an important consideration due to the airflow generated by the exhaust fan 14 . thus , the rotor 16 is arranged so that the impact hammers 44 have the largest mass possible within the swept area of the rotor 16 . in this embodiment , the rotor 16 includes three impact hammers 44 , although it is of note that the construction of the rotor 16 may vary greatly . the exhaust fan 14 is arranged to produce an airflow through the housing . specifically , the exhaust fan 14 connected to the fan outlet such that the airflow generated by the exhaust fan 14 is drawn into the housing 10 via the inlet opening 24 and is drawn out of the housing 10 via the outlet 34 . the details of the exhaust fan 14 are not shown as these will be obvious to one skilled in the art . the material delivery system 12 transports material to the rotary mill 1 . in this embodiment , the material delivery system 12 comprises a conveyor 46 . for reasons that will become apparent , the rotary mill 1 cannot be “ choke ” loaded . as a result , computerized control of the conveyor 46 may be used to provide a steady input volume regardless of input material size . specifically , rotor speed and airflow may be monitored to determine loading efficiency and this information may be used to control the power source driving the conveyor 46 . in this manner , the mass of material within the rotary mill 1 may be closely controlled so that attrition of material occurs at a steady rate . in operation , the material to be reduced is transported by the conveyor 46 to the inlet opening 24 . the material passes therethrough onto the intake guide surface 26 at a speed at or near free fall . the intake guide surface 26 directs the material into the swept area of the impact hammers 44 of the rotor 16 . of note is that the intake guide surface 26 is positioned such that a maximum amount of the kinetic energy generated by the rotor 16 is transferred to the material with minimal strain on the rotor 16 , so that the rotor 16 needs only to tip or bump the incoming material . this transfer of kinetic energy shatters the material along natural fault planes , producing smaller particles . the smaller particles are accelerated away from the rotor 16 and into the shatter bars 28 where further reductions occur as a result of collisions between the shatter bars 28 and the smaller particles . of note is that the shatter bars 28 do not have to be of massive structure or unusual hardness because of the reduced size of the particles . the shatter bars 28 also direct the smaller particles back towards the swept area of the rotor 16 where , in a continuous feed situation , the smaller particles encounter new particles produced by the impact hammers 44 of the rotor 16 striking newly introduced material and these secondary impacts between reflected material and recently shattered material result in further reduced particles . of note is that the rotor 16 causes a localized increase in the pressure of the airflow generated by the exhaust fan 14 . this forces entrained particles , which are naturally quite abrasive , away from the housing 10 , thereby drastically reducing scrubbing and wear on the rotary mill 1 . furthermore , the reduced particles are swept by the airflow drawn through the housing generated by the exhaust fan 14 around the curved portion 30 into the secondary reduction chamber 20 . as noted above , the curved portion 30 is arranged such that the airflow generated by the exhaust fan 14 directs the reduced particles toward the reduction elements 32 in the secondary reduction chamber 20 . as noted above , the reduction elements 32 are arranged such that only particles below a given size , or fine particles , pass through the reduction elements 32 and enter the outlet chamber 22 while oversized particles are directed back into the flow of reduced particles leaving the rotor path . thus , the reduction elements 32 provide the particle size control , forming a restriction in the path that material follows through the housing 10 . furthermore , the close , staggered configuration of the reduction elements 32 causes the airflow generated by the exhaust fan 14 to change direction rapidly several times before being drawn out of the secondary impact chamber 20 . this turbulent airflow prevents particle build - up from occurring on the reduction elements 32 . of note is that the position and orientation of the reduction elements 32 is not critical as they may be placed either vertically or horizontally with little or no change in their effectiveness . upon entry into the outlet chamber 22 , the fine particles remain in the airflow generated by the exhaust fan 14 and are drawn off through the outlet 34 while heavy particles fall to the lower material outlet 38 until a mass accumulates that equals the balance weight , which opens the balanced door 40 and releases the heavy particles . the balanced door 40 ensures that air is drawn into the rotary mill 1 only through the inlet opening 24 , thereby keeping a negative pressure on all parts of the housing 10 and serving as a form of dust control . furthermore , the position of the movable baffle 42 within the outlet chamber 22 may be altered to vary the intensity of the airflow , thereby varying the amount and size of the particles drawn off through the outlet 34 . in cases where this fine product has value , the flow of fine particles may , for example , be blown into a bag house or cyclone or may be turned into a slurry by the addition of a water spray . furthermore , the heavy material which exits the lower opening can be fed into any suitable classification machinery for further processing . thus , this arrangement also serves as a simple means of material classification . of note is that the position of the rotor 16 within the housing 10 is quite critical . in this embodiment , a clearance of 0 . 125 inches is optimum , wherein clearance refers to the ideal spacing between the rotor 16 and the housing 10 as well as the clearance between the impact hammers 44 and the housing 10 . if too much clearance is allowed , turbulence occurs and entrained particles build up which greatly increase the wear on the rotary mill 1 . the importance of having a constant and steady flow of incoming material can be shown when a large particle is introduced and allowed to pass through the rotary mill 1 alone . the resulting pile of reduced material consists of a light scattering of larger particles on the top and bottom of a cross section with the majority in the center finely pulverized , as there are few particles to carry out the attrition process . however , with a constant , regulated flow of input material , there is a steady impingement between fractured particles and the particle size distribution is more even . clearly , time of material residency is an important factor in the successful operation of the above - described rotary mill 1 . however , the tendency to return particles to the new product flow can cause a buildup of material in the system . this has been overcome by the addition of a supplementary airflow generated by the exhaust fan 14 . the exhaust fan 14 creates a path of steadily moving air from the inlet opening 24 to the outlet 34 . furthermore , the airflow overcomes turbulence created by the rotor 16 and ensures that all material continues to follow the desired path through the rotary mill 1 . the housing 10 thus provides the impact chamber 18 defined within the housing with the rotor 16 mounted in the impact chamber 18 of the housing 10 rotatable about a longitudinal axis 16 a of the rotor 16 . the impact chamber 18 of the housing has a peripheral wall 18 a which forms generally a cylinder surrounding the axis 16 a of the rotor . the feed opening 24 in the peripheral wall 18 a of the impact chamber forms a space in the cylindrical wall defined by edges 18 b and 18 c . the feed opening is arranged for deposit of the feed material onto the rotor so that rotation of the rotor acts to throw the solid materials against the peripheral wall 18 a . the rotor 16 has a plurality of axially extending , angularly spaced impact hammers 44 at its periphery for rotation about the axis 16 a of the rotor which is transverse to the feed opening 24 so that the materials are fed generally radially inwardly toward the axis . the rotor 16 is positioned relative to the feed opening such that the impact hammers 44 impact and deflect the solid materials entering through the feed opening , thereby fragmenting the solid materials to form finer and coarser particles and throw the particles outwardly toward the plurality of shatter bars 28 located at the peripheral wall 18 a of the impact chamber arranged such that the shatter bars contact the deflected solid materials , thereby further fragmenting the solid material into said particles . the shatter bars extend parallel to the axis and are arranged at angularly spaced positions around the axis . the second outlet chamber 22 is defined within the housing downstream of the rotor 16 with the first impact chamber and the second outlet chamber being connected by the chamber 20 and the separate elements 32 so that the particles pass from the first chamber 18 to the second chamber 22 . the finer particle outlet duct 34 is connected to the outlet chamber 22 and is arranged to so that the airstream acts to extract the particles from the chamber 22 to a separator outside the outlet 34 . the coarser particles are collected at the bottom discharge 38 for allowing release of coarser particles from a bottom of the outlet chamber . the guide surface 26 forms an inclined guide wall at the feed opening 24 starting at the edge 18 c in the peripheral wall of the impact chamber which is directed from the opening toward the rotor 16 . the guide wall 26 forms a planar surface 26 a which is inclined downwardly into the impact chamber 18 and transversely across the opening 24 so that the solid material falling from the conveyor 46 slides along the guide wall surface 26 a into the chamber to the rotor . a bottom edge 26 b of the guide wall is located closely adjacent the impact hammers 44 as they rotate with the rotor 16 so that the solid material is fed off the bottom edge onto the impact hammers . each of the impact hammers has along its axial length a leading blade element 44 a carried on a support 44 b of the impact hammer 44 . the leading blade element , when viewed in the cross - section of fig2 extends generally radially outwardly of the axis of the rotor from an inner edge 44 c to an outer edge 44 d which passes closely adjacent the edge 26 b . thus the blade element 44 a forms a leading or front face 44 e so as to engage and carry the solid material angularly forwardly around the axis of the rotor as it falls from the bottom edge 26 b . the leading blade elements 44 a are formed of a hardened steel material harder than the support 44 b of the impact hammer . as previously explained , the impact hammers 44 are arranged to form elements of a large mass so that the support of the impact hammer comprises a metal block extending longitudinally of the rotor and radially outwardly of the axis so that the leading blade element is mounted on a front face of the block . the hardened steel material is an iron based steel overlay wear plate material with a near nanoscale submicron microstructure . this provides a 68 to 71 hrc single and double pass deposit and maintains a high hardness after exposure to high temperatures . this provides an exceptional resistance to severe sliding abrasion ad a toughness equivalent to 400 brinell q & amp ; t plate . it provides a forming or cutting response similar to standard chrome carbide plate . this is a steel alloy with a unique glass forming chemistry that allow high undercooling to be achieved during application . this results in a considerable refinement of the crystalline microstructure to a near nanosize range . it has a density of the order of 7 . 36 g / cm3 . the leading blade element has a planar front face lying which is inclined relative to a bottom portion of the guide surface at the bottom edge at the location around the axis when the front face passes the bottom edge so that the outer edge 44 d of the front face is angularly advanced relative to the inner edge 44 c . in order to improve the fracturing of the particles , the shatter bars are also formed of the same hardened steel material . as shown in fig3 , the above grinding machine is used to generate ground glass from waste glass materials 60 . this generates ground materials of different grade of particle size from the size of crystals to fine powder . this includes fine materials 61 , medium materials 62 , coarse materials 63 and oversize materials 64 . the materials fine and medium materials 61 , 62 are mixed in a chamber 65 with a base material from a supply 66 such as epoxy which is liquid in an initial state for application and sets or cures to form a solid layer after application . in a process after the grinding as shown at 67 including heating in a suitable container , the ground glass is impregnated with a colorant and / or with a luminescent material . the base material is colorless so that , when the ground glass is mixed through the base material , the color of the road markings is provided by the impregnated or applied colorant and the base material does not impede or hide the reflection of light from the glass particles within the base material . the mixing of the ground glass through the base material acts to increase the hardness of the base material . the base material with the ground glass admixed therein is applied simultaneously by a spray coating or brush coating process shown schematically at 68 onto a road surface and the base material 70 is cured . thus there is provided a system 67 where the fine and medium ground glass 61 , 62 is impregnated or coated with a colorant and / or with the luminescent material and a second system 67 a where the coarse material 63 is coated with the colorant and / or with the luminescent material . the mixing chamber 65 receives the materials 61 , 62 for mixing the particles into the base material 66 where the finer material is mixed into the base material . as shown at 71 , the coarser material 63 is applied on the surface of the base material 70 on the road surface . as explained previously the coarser material 72 is collected at a bottom of a discharge chamber 22 and at least some of the finer material 61 is collected in an air stream at opening 34 at a top of the discharge chamber 22 . the material 72 collected from the bottom of the discharge material is separated at a separator 1 into a medium grind material 62 for mixing with the fine material in the base material 66 and a coarse grind material 73 . the material 73 is fed to a second separator 2 where it is separated into the material 63 for application separately onto a surface of the base material and the oversize material 64 as a return material for return to the rotary mill . in some cases the glass can be coated with both colourant and the luminescent material . however typically the product is used in an arrangement in which there is no colourant so that any colouring required is provided by the underlying markings over which the coating is applied . in this way the colourant from the underlying markings is visible through the coating of the impregnated ground glass . at the same time the product is luminescent since the glass particles at the top surface provide luminescence the top surface which is visible by adjacent observers . the application of heat to a temperature less than a melting point of the glass so as to expand the glass which can cause the binder and the luminescent material to be drawn into the outer surface of the glass particles as the particles cool so that there is a partial impregnation of the material into the outer surface of the glass with some of the material also remaining as a coating on the glass particles . as the glass is ground into individual particles , the coating material is applied over the outer surface of all the particles and thus creates a ground glass product which is luminescent from the luminescent material carried on the outer surface of the particles . since various modifications can be made in my invention as herein above described , and many apparently widely different embodiments of same made within the spirit and scope of the claims without department from such spirit and scope , it is intended that all matter contained in the accompanying specification shall be interpreted as illustrative only and not in a limiting sense .