in the process of the invention the toxic materials are typically placed inside a mechanical mill together with a suitable reagent ( s ), and subjected to milling action . as a consequence of mechanical activation associated with milling , collision events involving the reagents and the grinding media occur which induce the toxic materials to enter into reaction with the reagent materials to form non - toxic end products . additionally , it may be necessary to overcome an activation energy barrier for the reaction to proceed . in the process according to the invention , the activation energy is typically supplied by the action of a ball mill in providing mechanical activation . the processing parameters depend on the nature of the toxic materials treated and the mechanical activation employed . for illustrative purposes , the following parameters for rotary ball milling are preferred : atmosphere : air or inert gas , for example , argon or nitrogen plus any reactant gases . in the process of ball milling the liquid / solid / gaseous reactants , including the toxic materials and suitable reagents , collide with each other and the grinding media . at least one of the reactants should be a solid and the reactivity of the reactants increases due to the increase in reaction area resulting from the decrease in particle size of the solid phase associated with fracture events . a welding , mixing of atoms and / or exchange of molecules occurs at the interfaces of colliding particles to promote reactivity . if necessary , liquid reactants , such as toxic materials in liquid form , may be adsorbed on particles of an activated material , such as , for example , activated clay , activated carbon , activated alumina or activated diatomatious earth . initially such inert materials may be activated by a suitable surfactant or thermally activated . during high intensity ball milling , the temperature in the mill may increase due to the heat generated by some collision processes . the reactants may also be heated , preferably in the range of ambient to 200 ° c ., more preferably ambient to 100 ° c ., to improve the chemical reactivity . however , the process according to the invention is typically a relatively low - temperature process . the process of the invention is applicable to the disposal of a wide range of toxic compounds including organic and inorganic compounds , halogenated organic compounds such as cfcs , pcbs , ddt , dioxins , hexachlorophenol , chlorobenzenes , dichlorophenol , pentachlorophenol , dieldrin , aldrin , and other organochlorinated pesticides ( ocps ) such as chlordane and heptachlor . other toxic materials that may be disposed of by the method of the invention include 2 , 4 - d , 2 , 4 , 5 - t , paraquat , diquat , phorate , bromicide , carbamates , atrazine , other herbicides and insecticides , and chemical weapons such as gb ( sarin ), ga ( tabun ), vx and hd ( mustard ). the only limitation on the reactants is that there should normally be a negative gibb &# 39 ; s free energy change associated with the mechanochemical reaction , however there may be exceptions to this . the invention is further described and illustrated by the following examples . these examples are illustrative of a large number of candidate reactions and are not to be construed as limiting the invention in any way . loading of the hardened steel vial and all subsequent handling of reactants was carried out in a high purity argon filled glove box . ddt ( 1 . 5 grams ) and calcium oxide ( 10 . 9 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 72 grams and the ball to reactant mass ratio was 5 . 9 : 1 . at the conclusion of the milling , the product was analysed using x - ray diffraction ( xrd ), gas chromatography mass spectroscopy ( gcms ) and gas chromatography electron capture ( gcec ) techniques . the asmilled powder was found to contain calcium oxide and calcium hydroxide by xrd . the gcec analysis showed that 99 . 9996 % destruction of organochlorines had occurred during milling . water was added to the as - milled powder to dissolve the water soluble compounds . the resulting solution was dried and the residue was identified as cacl 2 by xrd . a chloride analysis of the residue indicated that all of the organic chloride had been converted to inorganic chloride during milling . the insoluble material was separated by filtering and subsequently analysed as containing calcium hydroxide and carbon . hydrochloric acid was added to the insoluble material to dissolve the calcium hydroxide . the resulting insoluble residue was filtered and dried . pyrolysis gas chromatography showed that no organic compounds remained in the final residue . xrd analysis of the final residue showed only the presence of carbon . the calcium oxide reagent thus produced end products that are substantially inert . calcium oxide is particularly attractive as a reagent due to its ready availability in the form of quicklime and its relatively low cost . significantly , the use of lime as a reagent for the destruction of toxic waste has previously been examined critically by some authorities in the field who have concluded that it has no application to , nor potential for , toxic waste disposal . however , contrary to these findings , when used in the process of the invention , lime and calcium oxide have been found to be highly effective as a reagent in the destruction of toxic materials , as the above and following examples demonstrate . pcb ( aroclor 1254 ) ( 1 . 0 grams ) and calcium oxide ( 8 . 8 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was ; 73 grams and the ball to reactant mass ratio was 7 . 4 : 1 . at the conclusion of the milling the product was analysed using gcms and gcec techniques . the gcec analysis showed that 99 . 9995 % of the pcb starting material was destroyed during milling . ddt ( 1 . 5 grams ) and calcium oxide ( 10 . 9 grams ) were milled together with twelve 12 mm hardened steel balls in a hardened steel vial for 24 hours using a fritsch planetary mill . the total mass of the balls was 96 grams and the ball to reactant mass ratio was 5 . 9 : 1 . at the conclusion of the milling the product was analysed using gcms and gcec techniques . the gcec analysis showed greater than 99 . 999 % destruction of organochlorine . ddt ( 1 . 0 grams ) and calcium oxide ( 7 grams ) were milled together with one hundred and sixty three 6 mm hardened steel balls in an attritor mill for 12 hours . the total mass of the balls was 163 grams and the ball to reactant mass ratio was 20 : 1 . at the conclusion of the milling the product was analysed using gcms and gcec techniques . the gcms analysis detected no chlorinated or organic compounds . dde ( 0 . 5 grams ) and calcium oxide ( 3 . 7 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 17 . 4 : 1 . at various times ; during milling samples were removed from the mill and analysed using gcms and gcec techniques . fig1 shows the fraction of dde remaining as a function of the milling time . the gcec analysis showed that 99 . 9998 % destruction of the organochlorine had occurred . ddt ( 1 . 5 grams ) and quicklime [ 78 % cao ] ( 13 . 5 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 4 . 9 : 1 . at various times during milling samples were removed from the mill and . analysed using gcms and gcec techniques . fig2 shows the fraction of organochlorines remaining as a function of the milling time . it is seen that dde forms as a break - down product of ddt . complete destruction of the ddt was found to occur after 6 hours and dde after 24 hours . ddt ( 1 . 5 grams ) and calcium oxide ( 11 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 800 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 5 . 9 : 1 . at various times during milling samples were removed from the mill and analysed using gcms and gcec techniques . fig3 shows the fraction of organochlorines remaining as a function of the milling time . it is seen that dde forms as a break - down product of ddt . complete destruction of the ddt was found to occur after 10 hours and dde after 24 hours . ddt ( 1 . 5 grams ) and quicklime [ 78 % cao ] ( 13 . 4 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 800 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 4 . 9 : 1 . the milling was carried out with the reactants exposed to an air atmosphere . at various times during milling samples were removed from the mill and analysed using gcms and gcec techniques . fig4 shows the fraction of organochlorines remaining as a function of the milling time . it is seen that dde forms as a break - down product of ddt . the measurements indicate that complete destruction of the ddt occurs after 3 hours and dde after approximately 20 hours . ddt ( 1 . 5 grams ,) and quicklime [ 78 % cao ] ( 13 . 5 grams ) were milled together with seventy 6 mm hardened steel balls in hardened steel vial for 24 hours using a spex model 800 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 4 . 9 : 1 . at various times during milling samples were removed from the mill and analysed using gcms and gcec techniques . fig5 shows the fraction of organochlorines remaining as a function of the milling time . it is seen that dde forms as a break - down product of ddt . complete destruction of the ddt was found to occur after 6 hours and dde after 18 hours . monochlorobenzene ( 1 . 1 grams ) and calcium oxide ( 8 . 0 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 36 hours using a spex model 8000 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 8 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 9993 % destruction of organochlorines . dichlorobenzene ( 1 . 02 grams ) and calcium oxide ( 7 . 0 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 800 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 9 . 1 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 9969 % destruction of organochlorines . hexachlorobenzene ( 1 . 06 grams ) and calcium oxide ( 7 . 98 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 73 grams and the ball to reactant mass ratio was 8 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 9994 % destruction of organochlorines . chlorpyrifos ( c 9 h 11 no 3 cl 3 ps ) ( 1 . 01 grams ) and calcium oxide ( 7 . 08 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed greater than 99 . 9998 % destruction of organic compounds . atrazine ( c 8 h 14 n 5 cl ) ( 1 . 0 grams ) and calcium oxide ( 7 . 02 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 72 grams and the ball to reactant mass ratio was 10 . 1 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed greater than 99 . 99 % destruction - of organics . fenitrothion ( c 9 h 12 no 5 p ) ( 0 . 95 grams ) and calcium oxide ( 6 . 63 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 7 : 1 . at the conclusion of the milling , the product was ; analysed using gcms and gcec techniques . the gcec analysis : showed 99 . 9996 % destruction of organic compounds . benzene ( c 6 h 6 ) ( 0 . 86 grams ) and calcium oxide ( 7 . 0 grams ) were milled together with nine 12 mm hardened steel balls in a hardened steel vial for 48 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the product was analysed using gcms analysis . the gcms analysis did not detect any organic compounds . paraffin oil ( 1 . 01 grams ) and metallurgical grade quicklime [ 78 % cao ] ( 14 . 24 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the product was analysed using gcms analysis . the gcms analysis did not detect any organic compounds . benzophenone ( c 13 h 10 o ) ( 1 . 00 grams ) and cao ( 7 . 03 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 48 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the product was analysed using gcms analysis . the gcms analysis did not detect any organic compounds . anthracene ( c 14 h 10 ) ( 0 . 99 grams ) and cao ( 6 . 98 grams ) were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 48 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the product was analysed using gcms analysis . the gcms analysis did not detect any organic compounds . dicyanobenzene ( c 8 h 4 n 2 ) ( 0 . 98 grams ) and cao ( 6 . 99 grams ) were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 48 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the product was , analysed using gcms analysis . the gcms analysis did not detect any organic compounds . ddt ( 2 . 0 grams ) and magnesium metal ( 2 . 45 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 20 . 2 : 1 . at the conclusion of the milling the product was analysed using gcms and x - ray diffraction ( xrd ). the gcms analysis did not detect any organochlorine , indicating that complete destruction had occurred during milling . chloride analysis of the as - milled powder using volhard &# 39 ; s method showed that all of the organic chlorine had been converted into inorganic chloride . the organic molecules of ddt thus appear to have reacted with the magnesium metal during milling and were converted into simple inorganic compounds . after heating to 600 ° c . in vacuum the powder was found by xrd to contain magnesium carbide and magnesium chloride . magnesium hydride is known to decompose at temperatures below 600 ° c . and was thus not detected by xrd . agricultural ddt in a toluene solvent [ 25 % ddt ] ( 7 . 96 grams ) and magnesium ( 4 . 97 grams ) were milled together with eight 10 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 800 mixer / mill . the total mass of the balls was 65 grams and the ball to reactant mass ratio was 5 : 1 . at the conclusion of the milling , the crumbly paste product was analysed using gcms analysis . except for the toluene from the solvent the gcms analysis detected no trace of the ddt starting material or any other chlorinated or organic compounds . ddt ( 2 . 01 grams ), sodium hydroxide ( 2 . 54 grams ) and graphite ( 0 . 25 grams ) were milled together with eight 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 65 grams and the ball to reactant mass ratio was 13 . 5 : 1 . at the conclusion of the milling , the product was analysed using x - ray diffraction and gcms . the as - milled powder was found to contain sodium hydroxide monohydrate and sodium chloride by x - ray diffraction . the gcms analysis detected that dechlorination had occurred . ddt ( 0 . 99 grams ) and mgo ( 6 . 97 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 2 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 98 % destruction of organochlorine . ddt ( 1 . 01 grams ) and fe 2 o 3 ( 7 . 0 grams ) were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 1 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 89 % destruction of ddt ( including ddd and dde ). ddt ( 1 . 00 grams ) and cuo ( 6 . 95 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 2 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 89 % destruction of ddt . copper metal was found on the balls after milling , indicating that the reduction of cuo to metallic copper occurred during milling . ddt ( 1 . 00 grams ) and al 2 o 3 ( 6 . 99 grams ) were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 1 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 85 % destruction of ddt ( including ddd and dde ). ddt ( 1 . 00 grams ) and a sample of ` red mud ` ( 7 . 03 grams ) from an alumina refinery were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . the total mass of the balls was 81 grams and the ball to reactant mass ratio was 10 . 1 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 84 % destruction of ddt ( including ddd and dde ). ddt ( 1 . 00 grams ) and fe 2 o 3 ( 7 . 3 grams ) and cao ( 9 . 91 grams ) were milled together with eight 12 mm hardened steel balls in a hardened steel vial for 21 hours using a spex model 8000 mixer / mill . the total mass of the balls was 64 . 9 grams and the ball to reactant mass ratio was 3 . 6 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 99 % destruction of ddt ( including ddd and dde ). ddt ( 1 . 01 grams ) and cao ( 0 . 89 grams ) were milled together with nine 12 mm hardened steel balls in a hardened steel vial for 24 hours using a spex model 8000 mixer / mill . in a second experiment ddt ( 1 . 01 grams ) and cao ( 0 . 88 grams ) were milled with al ( 0 . 11 grams ) using the same conditions . at the conclusion of the two millings , the products were analysed using gcms and gcec techniques . the gcec analysis showed 99 . 994 % destruction of organochlorine occurred in the sample which contained the addition of 0 . 11 grams of al , while in the sample not containing the al addition only 28 . 8 % of the organochlorine was destroyed . these results indicate that the ratio of cao to ddt can be greatly reduced ( compare with examples 3 to 9 ) by the addition of a small quantity of metal such as aluminium as one of the reactants . the addition of fe and ni had little effect . pcb ( aroclor 1254 ) ( 3 . 0 grams ) and magnesium metal ( 3 . 0 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 15 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed that 99 . 97 % of the pcb starting material was destroyed during milling . the organic molecules of pcb had thus reacted with the magnesium metal during milling and were converted into simple inorganic compounds . monochlorobenzene ( 1 . 0 grams ) and calcium metal ( 5 . 0 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 15 : 1 . at the conclusion of the milling , the product was analysed using x - ray diffraction ( xrd ), fourier transform infra - red spectroscopy and gcms techniques . the as - milled powder was found to be amorphous . gcms analysis did not detect any trace of the monochlorobenzene starting material . after heating to 700 ° c . in vacuum to crystallise the constituents the powder was found by xrd to consist of calcium hydride , calcium chloride - and calcium carbide . the organic molecules of monochlorobenzene had thus reacted with the calcium metal during milling and were converted into simple inorganic compounds . ddt ( 2 grams ) and calcium metal ( 3 . 2 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 17 . 3 : 1 . at the conclusion of the milling , the product was analysed using gcms techniques ; the as - milled powder was found to be free of all organic : matter to the resolution of the instrument ( nanograms ). the organic molecules of ddt had thus reacted with the calcium metal during milling and were converted into simple inorganic compounds . pcb ( aroclor 1254 ) ( 1 . 9 grams ) and aluminium metal ( 3 . 6 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 16 . 4 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed that 99 . 95 % of the pcb starting material was destroyed during milling . the organic molecules of pcb had thus reacted with the aluminium metal during milling and were converted into simple inorganic compounds . ddt ( 1 . 0 grams ) and iron metal ( 4 . 5 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 16 . 4 : 1 . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed that 96 . 4 % of the ddt starting material was destroyed during milling . the organic molecules of ddt had thus reacted with the iron metal during milling and were converted into simple inorganic compounds . ddt ( 1 . 0 grams ), calcium metal ( 0 . 7 grams ) and iron metal ( 4 . 0 grams ) were milled together with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours using a spex model 8000 mixer / mill . the total mass of the balls was 90 grams and the ball to reactant mass ratio was 15 . 8 : 1 . at the conclusion of the milling , the product was analysed using gcms analysis . the gcms analysis detected no organochlorines , indicating that practically total destruction of ddt occurred during milling . in view of the importance of cao as a preferred reagent several ways of further enhancing the reactivity off the reactants were investigated when using cao as the , or one of the , reagents . in particular , the effect of pre - milling the cao prior to mechanical activation with a toxic material , the effect of incremental addition of the cao and / or the toxic material to the reactants during milling and the effect of raising the temperature of the reactants were all investigated . in several cases , a marked improvement in the reactivity , evidenced by reduced milling times was achieved , the following examples illustrate the effect of pre - milling , incremental addition of reactants and heating . mixtures of pcb ( aroclor 1254 ) (˜ 1 grams ) and calcium oxide (˜ 7 grams ) were milled together with eighty one 6 mm hardened steel balls in a hardened steel vial for 8 - 12 hours using a spex model 8000 mixer / mill . in a second set of tests cao ( 8 . 5 grams ) was pre - milled with nine 10 mm hardened steel balls in a hardened steel vial for 12 hours in a spex model 8000 mixer / mill . the purpose of premilling being to reduce the cao particle size . mixtures of pcb ( aroclor 1254 ) (˜ 1 grams ) and the pre - milled calcium oxide (˜ 7 grams ) were then milled together with nine 10 mm hardened steel balls in a hardened steel vial for 4 - 6 hours using a spex model 8000 mixer / mill . at the conclusion of the milling , the products were analysed using gcms and gcec techniques . the effect of milling time on the fraction of pcb remaining is shown in fig6 . it is seen that pre - milling of the cao decreased the milling time required for a given level of destruction by a factor of approximately one half . pcb ( aroclor 1254 ) and calcium oxide were milled together with nine 10 mm hardened steel balls in a hardened steel vial using a spex model 8000 mixer / mill . the initial charge consisted of 6 . 78 grams of cao and 0 . 75 grams pcb . after 12 hours milling a small sample ( 0 . 1 grams ) was removed for analysis and a further 0 . 73 grams of pcb was added and milling then continued for an additional 12 hours . similarly , samples were removed and additions of pcb of 0 . 72 grams and 0 . 78 grams , respectively , were made after 24 and 36 hours milling . the samples were analysed using gcms and gcec techniques . fig7 shows the fraction of pcb , as measured by gcec , remaining at the end of each of the four milling periods associated with the additions of pcb ( i . e . after 12 , 24 , 36 , 48 hours milling ). table 1 gives values of the per cent destruction of pcb and the effective cao / pcb mass ratio after each 12 hour period . the measurements show that the sequential addition of pcb results in a significant reduction in the weight ratio of cao to pcb required to achieve destruction of pcb . table 1______________________________________milling time cao / pcb destruction ( hours ) mass ratio % ______________________________________1 . 12 9 : 1 99 . 99952 . 24 4 . 6 : 1 99 . 99973 . 36 3 . 1 : 1 99 . 9764 . 48 2 . 3 : 1 99 . 72______________________________________ a similar effect may be achieved by reusing excess ; cao remaining after destruction of the toxic material as part of the reactants for the following batch of toxic material to be treated . thus , for example , with an initial charge having a reagent / toxic material ratio of 12 : 1 , 3 units of the reactants could be removed following milling and replaced with 2 units of reagent and 1 unit of toxic material . milling is recommenced until substantially all of the toxic material is destroyed and then the process is repeated . this allows an increased number of batches or charges to be milled before the reagent / toxic material ratio falls to an unacceptably low level . a much better cumulative reagent consumption ratio can be achieved . in this example , after 9 charges the reagent / toxic material ratio falls below 7 , but the cumulative reagent consumption ratio is only 4 . 62 : 1 . combined with pre - milling or an ultrafine particle size of the reagent , a significant reduction in the reagent consumption during destruction of the toxic materials can be achieved . ddt ( 0 . 92 grams ) and cao ( 7 . 39 grams ) were milled together with ten 12 mm hardened steel balls in a hardened steel vial for 8 hours using a spex model 8000 mixer / mill . during milling the external surface of the vial was kept at 100 ° c . by the use of a heater . at the conclusion of the milling , the product was analysed using gcms and gcec techniques . the gcec analysis showed 99 . 9986 % destruction of organochlorine . this result shows that destruction of the ddt was greatly accelerated by heating , compared to milling at room temperature . the process of the invention can be readily applied on a large scale to facilitate commercially viable toxic material disposal . a suitably sealed mechanical mill of the kind commonly available , for example a rotary type ball mill , can be employed to perform the mechanical activation . such a mill may be permanently located at a prescribed toxic material disposal site , or a smaller transportable version may be mounted on a truck for transport to the locations of toxic materials . the toxic material is introduced into the mill with appropriate grinding media and a reagent , and the mixture is subjected to milling for a predetermined time period or until such time as sample analysis indicates no detectable levels of the toxic material remain in the mill . any quantity of toxic material can be processed in this way using a batch feed technique . closed circuit recycling of the mill contents between the mill and an external vessel may be desirable in some circumstances . post - milling processing may also be performed to extract the non - toxic end products and / or to facilitate recycling of some end products . the mechanically activated process for the disposal of toxic materials described above has a number of significant advantages over conventional disposal methods , including the following : 1 . the process is simple and does not require the simultaneous functioning of a large number of interconnected systems and components to operate . this lowers the overall risk associated with the process . 2 . the process can be carried out in a closed system which is advantageous in controlling the risk of any emissions of toxic materials . 3 . the process can be operated at conditions close to ambient and thus does not present a high risk for catastrophic emission of toxic materials . 4 . the process is intrinsically robust and its safety will not be compromised by events such as power failure or drive failure or weather conditions . it can be stopped or started as desired . it can be operated without reliance on real time electronic process control systems . these factors lower the risk associated with use of the process . 5 . the process is applicable to a wide variety of liquid or solid toxic materials . 6 . the process can be relocatable and therefore can be used to treat toxic materials on site , and the risks associated with the transport of toxic materials are eliminated . 7 . the process does not require extensive disassembly , reassembly or recommissioning when moved . this lowers the risks associated with these operations . 8 . the end products of the process are typically non - toxic inorganic materials which can be easily disposed of or even recycled . 9 . the process can , in some cases , potentially be used to dispose of both the toxic material and its container at the same time , thus eliminating a handling stage and the associated risks . 10 . the process bears no resemblance to incineration , and is therefore not liable to be perceived to be unacceptable by the drawing of comparisons with incineration . now that preferred embodiments of the invention have been described in detail , it will be apparent to persons skilled in the relevant arts that numerous variations and modifications can be made without departing from the basic inventive concepts . all such modifications and variations are considered to be within the scope of the present invention , the nature of which is to be determined from the foregoing description and appended claims . furthermore , the preceding examples are provided to illustrate specific embodiments of the invention and are not intended to limit the scope of the process of the invention .
a process for the treatment of toxic materials , for example , inorganic compounds , halogenated organic compounds such as polychlorinated biphenyls , dioxin and dichlorodiphenyl trichloroethane and chemical weapons such as sarin and mustard . the process is based on the discovery that mechanical activation can induce chemical reactions which break down the molecular structure of toxic materials and form products which are simple , non - toxic compounds . the process involves subjecting a mixture of a toxic material and a suitable reagent to mechanical activation to produce a non - toxic end product or products . mechanical activation is typically performed inside a mechanical mill , for example , a ball mill . ball milling of various toxic materials with appropriate reagents was found to result in virtual total destruction of the toxic starting material .