reference will now be made to a preferred embodiment of the present invention , an example of which is illustrated in the accompanying drawings . a preferred embodiment of the invention is illustrated in fig1 . in one preferred embodiment , the present invention is a process for making an effective and environmentally acceptable abrasive product from the effluent of industrial incinerators and emission control dusts of , for example , the aluminum industry . these industrial wastes typically contain significant percentages of alumina . included with the alumina may be siliceous materials , calcium compounds , magnesium compounds , iron compounds and heavy metal compounds . fig1 illustrates the process in accordance with one preferred embodiment of the present invention . as shown in fig1 the process preferably comprises the general steps of : pre - processing the waste stream ; using a computer - based matrix system to group the waste stream into different batches ; mixing the feed stream with other glass - making materials to form a batch mixture ; melting the batch mixture to form a glass ; and fritting the glass to form an abrasive . the process also oxidizes the organics and vaporizes the heavy metal oxides contained in the mixed batch mixture during the melting phase . heavy metal oxides , which may be discharged with the exhaust gases , may later be recovered . of course , the first step in the process of producing an environmentally acceptable abrasive product from a stream of hazardous wastes is to provide hazardous wastes . this step is illustrated as box 10 of fig1 . the hazardous waste stream employed in this process typically includes a relatively high aluminum content , heavy metals elements and compounds , and other organic and inorganic wastes and toxins . as embodied herein , the pre - processing step of the present invention includes the extraction of soluble salts from the waste stream . this pre - processing step is illustrated in fig1 as box 12 , and more particularly includes a hot water extraction process for removing soluble salts from the waste stream . the hot water extraction process is done as waste materials arrive for processing . the incoming waste is washed and stirred in a water bath equal to twenty ( 20 ) times the weight of the raw waste being washed . the water bath is a hot water bath in which the bath temperature is maintained at about 50 to about 80 degrees c . the materials will remain in the water bath for a period of time equal to about 2 hours . the resulting solution is passed through a filter press , where the insoluble components of the waste stream are caught and retained as a filter cake . the filter cake is then partially dried and repackaged . a number of different filter cakes can be merged for easier control of assaying . the material is also weighed before the extraction process and again after the filter cake resulting from the hot water extraction . the weight loss is recorded in a computer batching matrix , which organizes the extracted material for batching and melting . after completing the hot water process , the extracted filter cakes of the hazardous wastes ( such as emission control dusts ) are segregated and merged into lots . these lots are then sampled by known assaying methods for organic content , alumina content , and the content of other relevant materials . the step of assaying and analyzing the content of the filter cakes is illustrated as box 14 of fig1 . while any number of known assaying techniques may be employed , it is most important to accurately measure the percentage of alumina and the percentage of inorganic materials . accordingly , the amount of organic material may be easily ascertained by conducting an energy content test , or a loss - on - ignition test . a thermogravimetric analysis may also be employed to identify the amount of organic material present in the lot , as well as the percentage of hydrates . the presence of heavy metals can be easily determined through the use of an atomic absorption spectrophotometer or other similar techniques . a combination of each of these tests , plus historical data relating to specific type of waste generated by specific waste generator can be used to establish the characteristics of the materials . as embodied herein , the data collected from the analysis of each lot is entered into a computer batching matrix for analysis and recording and for development of melting batches incorporating the addition of glass formers and modifiers such as silica and soda ash respectively . the computer batching process is discussed in greater detail hereinbelow . the soluble salts collected from the hot water extraction process are the residual after concentration , crystallization and evaporation . this step in the inventive reclamation process is illustrated in box 16 of fig1 . the collected soluble salts are tested for heavy metals to determine their potential as by - products . for example , the collected soluble salts may be usable for roadway ice melting purposes , for weed control or reused in metal processing . however , in order to be usable for these purposes , the salts must be substantially free from heavy metals . the invention preferably further includes a computer batching system which tracks the characteristics of particular waste streams from particular waste generators , across time affording an understanding of the historical trends in constituent percentages of the total weight . it also creates batch matrices into which the lots of particular waste streams with the other ingredients , mainly glass formers such as sand and modifiers such as soda ash , are fitted to produce particular abrasive specifications . the contents of each batch will , in turn , meet the required product specifications . the step of batching by computer matrix is illustrated in fig1 as box 18 , and includes the further step of inputting the results of the chemical assaying discussed hereinabove with respect to the pre - processing of the wastes stream . many of the particles included in the batch mix are fine particles , measuring between 2 and 20 microns across their broadest dimension . these particles are dusty and , by virtue of their extremely small size , cannot be handled directly in the batch mix . for this reason , they may be coated to coagulate them onto larger particles of the batch mix . in a preferred embodiment of the present invention , to a mixture of water and glycerin , or other suitable materials that will readily evaporate or oxidize and will not impede the heating of the particles and particularity the organics , is used . the fine particles inside the melter will be further managed by baffles within the melter which will keep them from continuing to travel in the gas stream and direct them to settle out in the molten glass . certain types of heating routines may be used in this connection where the feed is periodically reduced or increased as may be sensed to be needed in the exit from the melter atmosphere . the heating routines are a function of the batching matrix , and will depend upon the composition of the starting materials , including , but not limited to , the amount of iron and organic matters present in them . in a preferred embodiment of the present invention , the batched mixture is next delivered to an apparatus adapted to melt the batch mixture into a glass - like material in an oxidizing environment . the melting apparatus is further adapted to oxidize organic materials and vaporize heavy metal oxides in the gas stream . the step of melting the waste stream is illustrated in fig1 as box 20 . the collection of the vaporized organic materials is illustrated as box 22 , and the step of collecting vaporized heavy metal oxides is illustrated in box 24 of fig1 . under certain circumstances , it may be desirable to add collected heavy metal oxides to the batch mixture . melting in an oxidizing environment is required in order to assure that organic materials are oxidized as completely as possible from the batched mixture . an oxidizing environment also serves the function of oxidizing at least some fine elemental or alloyed metal particles in the batched mixture . moreover , failure to melt the batched mixture in an oxidizing environment could lead to reduction of the heavy metals or other metal oxides , particularly if carbon is present in the batched mixture . carbon would reduce metal oxides to the metal and carbon dioxide , thus making it more difficult to reclaim the metal component of the batched mixture . metal components or molten glass are also damage refractories and cause premature failures . an appropriate apparatus for melting the batch mixture is a glass melter as illustrated in fig2 and indicated generally as 30 . as embodied herein , glass melter 30 is also adapted to oxidize organic materials in the batch mixture . thorough oxidation of organic materials is ensured by providing an oxygen injection system 32 which assures an oxidation atmosphere in the melter . as embodied herein , glass melter 30 also vaporizes any heavy metal oxides , such as for example , lead and cadmium oxides , and excepting chromium oxides , in the batch mixture . the vaporized heavy metal oxides are directed from the melter 30 to a scrubber 40 attached to the melter via an exhaust duct 35 . the scrubber 40 is a wet / dry scrubber which condenses the metal oxides from the stream of vaporized materials . vaporized heavy metals are preferably maintained in the vapor state in the melter 30 and in the exhaust path 35 from the melter 30 to the first quench zone 45 of the scrubber 40 . temperatures along the exhaust path should be maintained above about 1100 ° c . to avoid the precipitation of the heavy metals prior to the quench zone 45 . premature precipitation will cause such the heavy metals to accumulate in the exhaust pathway 45 . in a preferred embodiment of the invention , scrubber 40 is a wet / dry scrubber , such as the waterloo scrubber known is the art , modified to recapture the vaporized heavy metal oxides and particles of the glass - making materials from the melter exhaust gases . in a preferred embodiment of the present invention the exhaust gasses are quenched in the quench zone 45 by exposure to a spray of water and by exposure to the water irrigated surfaces of the quench zone 45 . the quench water is recovered and filtered through a filter press to remove the precipitated lead oxide and cadmium oxide . in general , this water will be maintained in a slightly alkaline condition with the use of calcium hydroxide . specifically , the scrubber liquid is maintained at a ph of about 9 and is regularly monitored to assure that it remains in an acceptable range . the air stream is passed through a wet particle scrubbing zone or a &# 34 ; contact &# 34 ; zone where water vapor contacts the particles in the gas stream and removes them by a wetting process . the moisture is then removed from the air with the particles in the zone of an axial fan and in the moisture entrapment zone . the water containing the particles is treated in a treatment process to remove the particles in a filter . the filter cake of particles contains glass making ingredients such as silica , alumina , magnesia , calcia , soda , potash and zinc oxide which can be used in batching materials after being assayed and analyzed . after the collection materials are complete , they are assayed and the resulting data is entered into the computer batching matrix . they are reused in this or other glass processes . after passing through the contact zone , through the axial fan and through the entrapment zone the air is then heated to approximately 150 ° c . the air stream is then passed through a dry baghouse 50 which substantially collects any remaining metal oxides allowing any remaining water to pass through and be collected for reuse or disposal . the precipitated heavy metals are collected in collection chamber 46 . the metal oxides are then dried and collected . the lead oxide and cadmium oxides can be later used as a raw material for other glass manufacturing processes . the temperature of the glass melter 30 is adjusted to heat to the proper melting temperature for a batch mixture of a given composition . for example , furnace temperatures may need to be increased depending on the amount of high melting point material , such as iron , that is present in the batch . additionally , the melting point of the batch mixture may be changed by the addition of various materials . for example , certain sodium compounds such as na 2 co 3 , or nasio 3 may be added to reduce the melting point of the batch mixture . in addition , thermal analysis , i . e ., the weight and energy gain or loss and gas emission as a sample material is heated to , for example , 1000 ° c . in 10 ° c . increments and viscosity measurements are also input into the process base data in order to determine the optimum melter temperature . melting will occur in an oxygenizing atmosphere , though the time / temperature regimen will depend upon the starting materials of the batch mixture and the specific composition of the material . for example , materials with a high content of metal oxides with high melting temperatures will take longer to melt at a given temperature . in a preferred embodiment of the present invention , the process oxidizes substantially all organics which are present , as well as all metals present as fine particles . the minimum temperature required to perform this oxidation is 1250 ° c . for producing the abrasive particles . during the processing of emission control dusts or sludge as a feed stock , organic constituents of the melt will be exposed to a temperature of 1250 ° c . in an oxygen rich atmosphere for a period of greater than three seconds . this will also satisfy requirements for the destruction of pcb &# 39 ; s and other possible toxic organics present in the batch mixture . the required vaporizing temperature is 1100 ° c . for lead and cadmium oxides , though the upper vaporizing temperature is approximately 1750 ° c . in order to assure vaporization of fluoride containing compounds in the batch mixture . as embodied herein , the melter 30 should provide for a long dwell time . the melter 30 should also provide for oxygen injection to insure complete oxidation of the organic compounds . in a preferred embodiment of the present invention , the melter 30 will oxidize up to 500 ppm toxic organics , allowed in the waste stream under current epa regulations . the final product is discharged ( as described below ) directly into a water bath or may be first &# 34 ; frizzled .&# 34 ; in a preferred embodiment of the present invention the resulting glass is fritted to the correct shape . this step is illustrated in box 26 of fig1 . sizing of the materials is accomplished by discharging the material at high temperature ( 1200 ° c .) from the melter 30 to a quenching water bath . this produces blocky or block - like , round or spheroidal and pyramidal shaped particles with high fracture resistance . the resulting intregal particles are between 75 and 125 microns in maximum dimension . the temperature at fritting is critical to produce this result . this temperature of the outflow of glass must be adjusted to impart to the glass a low viscosity just prior to fritting . alternatively , it is possible to spray the glass as it emerges from the furnace with a fine mist of cooling liquid , such as water . this process is called frizzling in which the flow of melted liquor is sprayed with a fixed amount of water to begin the cooling process . frizzling results in larger particles than in fritting . these particles are then dropped onto a refractory belt composed of ceramic materials with high melting temperatures where the individual particles still have enough residual heat to heal cracks in them . this particular process may be employed in the manufacture of coarse abrasives . the resulting materials , whether fritted or frizzled , is then collected as illustrated in box 28 of fig1 . under certain circumstances , it may be desirable to add collected heavy metal oxides to the collected abrasive product . in one variation of the process , emission control dusts from the aluminum industry are formulated directly to the specifications of the abrasive material . this material is known as &# 34 ; alumaglass .&# 34 ; an initial volume of emission control dust , weighing 200 gm , was submerged and stirred in a hot water bath having a weight of approximately 20 times that of the emission control dust , i . e ., approximately two liters of water . the hot water bath was maintained at a temperature of approximately 80 ° c . the emission control dust was allowed to remain in the hot water bath for 2 hours , after which time the entire mass was passed through a filter . the filtered materials were weighed in order to determine the loss in weight . the filtered materials weighed 112 gm . the filtrate was evaporated to crystallize and collect the soluble salts washed out in the water bath . the filtrate consisted mainly of calcium chloride dihydrate and some complex calcium hydrate salts . no evidence of heavy metals was found . there salts will be dehydrated prior to use by calcining . the materials collected on the filter weighed 112 gm and consisted of the following materials in the following percentages in the column below to the left : ______________________________________material percent of total______________________________________sio . sub . 2 3 . 59al . sub . 2 o . sub . 3 28 . 72mgo 7 . 23cao 3 . 74na . sub . 2 o 0 . 44fe . sub . 2 o . sub . 3 1 . 48tio . sub . 2 1 . 48mno 0 . 56p . sub . 2 o . sub . 5 0 . 46zno 0 . 28li . sub . 2 o 0 . 03coo 0 . 01loss on ignition ( organics ) 48 . 70______________________________________ the 112 gm sample of material was placed in a crucible fabricated of zirconia . the batching / mixing matrix indicated that 41 . 3 gm of sand and 19 . 8 gm of soda ash should also disposed into the crucible . the crucible and materials were placed in a melting oven . the oven was heated to a temperature of between 1450 ° c . and 1500 ° c . an oxidizing atmosphere was maintained inside the melting oven . the temperature of the oxidizing atmosphere was maintained at approximately 1480 °- 1500 ° c . the melt temperature was maintained for a period of approximately 4 hours . thereafter , the molten material was discharged directly into a water bath maintained at a temperature of between 90 ° and 95 ° c . the resulting fritted material had a size distribution of between 250 - 75 microns . the resulting high hardness , abrasive material included the following components in the following percentages : ______________________________________mateial percent of total______________________________________sio . sub . 2 49 . 20al . sub . 2 o . sub . 3 25 . 80mgo 6 . 40cao 3 . 40na . sub . 2 o 8 . 40fe . sub . 2 o . sub . 3 1 . 30balance ( various ) all ≦ 0 . 25______________________________________ in another variation of the process an emission control dust from the aluminum industry is mixed with a waste water treatment sludge (&# 34 ; wts &# 34 ;) containing mainly lime , alumina , magnesia and silica and which may be hazardous by characteristic for lead according to the toxic constituent leaching procedure (&# 34 ; tclp &# 34 ;) test 1311 . after completing the hot water extraction process on the emission control dust as described in example 1 , the wastes comprised the following materials in the following percentages : ______________________________________material percent ecd total percent wts total______________________________________sio . sub . 2 0 . 00 2 . 60al . sub . 2 o . sub . 3 74 . 30 4 . 20mgo 6 . 30 1 . 33cao 0 . 00 47 . 60na . sub . 2 o 0 . 00 0 . 28fe . sub . 2 o . sub . 3 1 . 50 1 . 20tio . sub . 2 0 . 40 0 . 76p . sub . 2 o . sub . 3 0 . 00 0 . 13zno 0 . 00 1 . 90caf 11 . 30 0 . 00so . sub . 3 0 . 00 4 . 38pbo 0 . 00 0 . 87sro 0 . 00 0 . 22k . sub . 2 o 0 . 00 0 . 13zn . sub . 2 o . sub . 2 0 . 00 0 . 01f . sub . 2 / cl . sub . 2 1 . 30 15 . 00loss on ignition 0 . 90 14 . 33 ( organics ) c 0 . 00 5 . 06insolubles 4 . 30 0 . 00______________________________________ the batching matrix determined that 144 gm of wts should be mixed with 40 gm of ecd . the batching matrix also indicated that 40 gm of silica sand and 16 gm of soda ash should be added to the mixture . the silica sand and anhydrous sodium silicate was added to the mixture . the mixture was subjected to the same heating regimen described above in example 1 . the resulting high hardness , abrasive material comprised the following components in the following percentages : ______________________________________material percent of total______________________________________sio . sub . 2 52 . 02al . sub . 2 o . sub . 3 27 . 50mgo 2 . 00fe . sub . 2 o . sub . 3 1 . 40cao 9 . 40na . sub . 2 o 7 . 50tio . sub . 2 0 . 22zno 0 . 05so . sub . 3 0 . 01pbo 0 . 09k . sub . 2 o 0 . 11______________________________________ with respect to the high hardness , abrasive product fabricated according to the above examples , the specifications of this material are as follows : ______________________________________physical properties : ______________________________________color : black - opaque ( gray in fine sizes ) structure : amorphoushardness : 575 - 625 knoop - 100 gm . density : 2 . 7 - 2 . 8 gm / ccsoftening point : 1100 - 1125 ° c . working point : 1150 ° c . ______________________________________ exemplary high hardness , abrasive materials will comprise at least the following materials in the following amounts : ______________________________________chemical constituents : ______________________________________ sio . sub . 2 48 - 54 % al . sub . 2 o . sub . 3 22 - 28 % na . sub . 2 o 8 - 10 % ca . sub . 2 o 8 - 12 % mgo fe . sub . 2 o . sub . 3 1 - 3 % pbo 0 . 1 - 1 % others max . 0 . 25 % ______________________________________ this material has superior characteristics as a loose grain abrasive . this indicates that it will also be a superior material for the manufacture of coated abrasives for wood and metal working and conceivably also , on a limited basis , bonded abrasives . because it can be separated into size profiles by water sedimentation , it can also be used as a polishing material . part of the formulation requires a small amount of lead to be included in the glass of extraordinary toughness as well as adequate hardness for abrasive applications . the glass contains small amounts of iron oxide which renders it a black color which is desirable for materials used as loose grain or coated abrasives . dark colors are necessary to show the residual material after clean - up or blow - off and thus assist in quality assurance by identifying that the abrasive has not been cleaned away adequately . it will be apparent to those skilled in the art that various modifications and variations can be made to the present invention and in particular to the specification or the claims without departing from the scope or spirit of the invention . thus , it is intended that the present invention cover the modifications and variations of the invention provided they come within the scope of the claims and their equivalents .