Patent Number: 052778460
Section: description

The installation comprises a cryogenic grinding unit made up of a crusher-shredder 1 and a granulator 2 which operate at -120.degree. C. The ground waste is passed through a duct 3 to a first metering device 4. A second metering device 5 is fed by a duct 6 coming from a source of additive. The two metering devices 4, 5 open into a duct 7 which is supplied at one end from an air source and which leads to a mixing cyclone 8. From here runs a rod 9 which passes through the side wall of a furnace and opens out close to the bottom 10 of said furnace. The furnace, made of refractory material, comprises two distinct parts. A crucible 11, made of refractory steel at the bottom, containing a molten siliceous bath and equipped with heating means 12, and an upper part 13 made of refractory material. A pouring rod 14 passes through the base 10 and opens into the crucible at a height of 400 mm. The top part 13 has a refractory vault 15 provided with zig-zag passages 16 which sub-divide this top part into a combustion chamber 17 formed above the siliceous bath and below the vault 15 and an evacuation chamber 18 above the vault 15. The top part 13 is equipped with heating means 19. An air ramp 20 opens into the chamber 17. From the chamber 18, a duct 21 leads to an air cooler 22 supplied with air through a duct 23 and communicating via a duct 24 with a chemical neutraliser 25 which converts chlorine into soluble chloride and operates as a closed circuit, with a pump 26 circulating a solution of alkali metal carbonate or sodium carbonate into the neutralizer 25 through a duct 27. A duct 28 leads from there to a very high efficiency filter 29. The efficiency of the filter is 99.98%. This filter is intended to eliminate radioactive aerosols. From the filter 29, a duct 30 leads to a fan 31 and a chimney 32. The following examples illustrate the invention. EXAMPLE 1 The installation shown in the drawing is used to treat waste from the maintenance and repair of hospitals, laboratories and nuclear plants, consisting of plastics, rubber, paper, cotton and cloth. This waste is contaminated by radionuclides with a short half-life and low radioactivity. This waste, ground in the crusher 1 and granulator 2, which operate at -120.degree. C., has a particle size of less than 1 mm in the duct 3. The metering device 4 delivers 667 g of waste per minute to the duct 7. The metering device 5 delivers 19 g of sodium carbonate per minute to the duct 7. The flow rate of air in the duct 7 is 3 normal cubic meters per hour under pressure. The refractory steel crucible 11 has a diameter of 500 mm and a height of 1000 mm, corresponding to a capacity of 196 liters. It contains a molten siliceous bath consisting of 61% by weight of SiO.sub.2 and 39% by weight of a mixture of B.sub.2 O.sub.3 and Na.sub.2 O. The melting point is 900.degree..+-.20.degree. C. The operating temperature is 1000.degree..+-.50.degree. C. The height of the bath at the start of treatment is 400 mm (78 liters corresponding substantially to 195 kg). This mass constitutes the permanent liquid residue in the crucible which is at a temperature of 1000.degree. C. The opening of the injection rod 9 for the waste is 100 mm above the bottom 10. 350 normal cubic meters per hour of air are passed into the combustion chamber 17 via the ramp 20. 2300 normal cubic meters of air per hour are passed through the duct 22 at 20.degree. C., thus enabling the temperature of the gases leaving the duct 21 to be brought down to a temperature of below 100.degree. C. The temperature at the exit from the cooler is about 80.degree. C. The binders and mineral additives to the waste are held in the siliceous bath. The variation in the volume of the bath, for an intake flow rate of 40 kg of waste per hour is 0.7 liters per hour and this bath is poured through the rod 14 every 96 hours for a unit treating 40 kgh.sup.-1. The glass solidifies in the receiving vessel. Its chemical composition hardly varies as a function of time. Analyses of the poured glass after 8 hours treatment shows SiO.sub.2 equals 61%+.epsilon., whereas Na.sub.2 O+B.sub.2 O.sub.3 equals 39%-.epsilon.. The effluent leaving the chimney 32 comprises 49,000 normal cubic meters of CO.sub.2 per hour, 52 cubic meters of H.sub.2 O per hour and 2600 cubic meters of air per hour. The environmental pollution is negligible because the process only emits 97% air at 20.degree. C. Any contaminants are imprisoned in the poured glass or trapped on the specific filter and the HCl content remains less than 100 mg per normal cubic meter. When it is known that this type of waste is currently collected, then compacted and coated with concrete in specific containers and that a 200 liter capacity vessel contains only 30 kg of waste, it will be realised that the process according to the invention makes it possible to reduce the volumes definitively by a co-efficient of about 350, whilst achieving a compact packaging which has good mechanical resistance and is not subject to leaching. EXAMPLE 2 Polyethylene and glass flasks are treated which contain scintillators and nuclear medicine tracers. The installation is the one described in example 1. The metering device 4 supplies 670 g of waste per minute to the duct 7. A metering device 5 supplies 25 g of sodium carbonate per minute to the duct 7. Through the ramp 20, 5 normal cubic meters per hour of air are passed into the chamber 17. 910 cubic meters per hour pass through the duct 23 at a temperature of 20.degree. C. The temperature at the exit from the cooler is about 80.degree. C. In this case, the neutralizer 25 is omitted from the installation. The chemical composition of the bath is 60% by weight of SiO.sub.2 and 40% by weight of a mixture of B.sub.2 O.sub.3 and Na.sub.2 O. The melting point thereof is 900.+-.20.degree. C. Its operating temperature is 1000.+-.50.degree. C. The variation in the volume of the bath essentially caused by the glass flasks for an intake flow rate of 40 kg of waste per hour is 12.5 liters per hour and pouring through the rod 14 is carried out every 8 hours (100 liters. A composition of the glass obtained hardly changes as a function of time, the composition remaining substantially identical to the initial composition. The waste gases leaving through the chimney consist of 16 normal cubic meters of CO.sub.2 per hour, 16 cubic meters of H.sub.2 O per hour and 1000 normal cubic meters of air per hour. The process produces only an effluent which consists of 97% air at 20.degree. C. Any contaminants are imprisoned in the poured glass or trapped on the filter. Currently, these flasks are coarsely ground in order to recover the scintillation residues, then compacted and coated in concrete in specific containers. A 200 liter container of this mixed waste contains only 30 kg of glass. The process makes it possible to reduce volumes by a coefficient of 16 and provides a compact, non-leachable packaging with good mechanical strength. EXAMPLE 3 Waste from the chemical industry consisting essentially of phenyl mercury is treated. The installation used is essentially the same as that used in FIG. 1. The metering device 4 delivers 167 g of waste per minute to the duct 7. The metering device 5 delivers 22 g of a mixture of alkali metal carbonate and silica per minute to the duct 7. 3 cubic meters of air per hour are fed under pressure into the duct 7. 60 normal cubic meters per hour of air are passed to the chamber 17 via the ramp 20. Through the duct 23, 700 normal cubic meters of air are passed each hour at 20.degree. C. The temperature at the exit from the cooler 22 is about 80.degree. C. The chemical neutralizer converts HgO into soluble salts. The bath contains 60% by weight of SiO.sub.2 and 40% by weight of Na.sub.2 O. Its melting point is 900.+-.20.degree. C. Its operating temperature is 1000.+-.50.degree. C. Analysis of the poured bath, after 8 hours treatment, shows SiO.sub.2 equals 60%.+-..epsilon. and Na.sub.2 O equals 40% .+-..epsilon.. The variation in the volume of the bath, for an intake flow rate of 10 kg of waste per hour, is 3.2 liters per hour. The waste gases comprise 11 normal cubic meters of CO.sub.2 per hour, 4 normal cubic meters of H.sub.2 O per hour and 700 cubic meters of air per hour. The process produces a waste product of 98.5% by weight of air at 20.degree. C. (the Hg content is less than 0.3 mg. per normal cubic meter) .