Patent Number: 062185926
Section: description

DETAILED DESCRIPTION OF THE INVENTION The evaporator concentrate used in the method of the invention should be essentially free of undissolved substances, since the latter impair or prevent a homogeneous crystallization of the sodium sulfate without inclusions of radioactive components. The separation of the unsoluble substances can, e.g., be effected by filtration, decantation, separating or other mechanical separation processes, decantation being preferred. The evaporator concentrate which is essentially free of suspended matter is introduced at normal temperature into the container of a crystallization apparatus which is schematically shown in FIG. 1. The apparatus consists of a container 1 for receiving the evaporator concentrate, an immersion cooler 2 which has one or more inlets 3 and outlets 4 for a cooling or heating medium and is connected to a cooling or heating aggregate 5 which provides the cooling or heating medium. The immersion cooler 2 is immersed into the evaporator concentrate which has been introduced into container 1 from the top by means of a lifting apparatus (not shown) after the cooler has been cooled down to about 0.degree. C. by introducing a cooling medium, e.g. ethylene glycol/water or saline, from the cooling or heating aggregate 5. Temperatures below -2.degree. C., i.e. the freezing point of the mother liquor, are undesirable, since in this case ice crystals will deposit on the heat exchange surface of the immersion cooler 2. The evaporator concentrate in container 1 is not agitated or stirred during crystallization. Under the above-mentioned conditions, the sodium sulfate will crystallize as Glauber's salt (Na.sub.2 SO.sub.4.10H.sub.2 O) from the oversaturated solution and will form uniform crystal layers on the cooling surface which, depending on the crystal habit, may still contain up to about 10% of mother liquor. The formation of excessively thick crystal layers should be prevented. Usually the crystallization is stopped after a period of about 8 hours or after a maximum thickness of the crystal layer of about 5 cm has been reached. The immersion cooler 2 having the crystal layer deposited thereon is then lifted out of the evaporator concentrate and left further for about 30 minutes above container 1 in order to let the adhering radioactive mother liquor drop off. Usually decontamination factors of about 10-20 are obtained on crystallization; i.e. the specific activity of the crystals is 10-20 times lower than that of the mother liquor. Depending on the starting activity, this is not sufficient to obtain inactive sodium sulfate, so that a subsequent recrystallization is required. Said recrystallization can be carried out in the form of a cooling crystallization or as a conventional evaporation crystallization. Preferably, a cooling crystallization is employed. For this purpose, the immersion cooler 2 having the Glauber's salt crystals deposited thereon is placed over a bath of deionized (e.g. destilled) water and heated by introducing a heating medium (e.g. warm water) to about 33-40.degree. C. (e.g. 35.degree. C.). This makes the Glauber's salt crystals melt in their own crystal water, slide into the water bath and dissolve therein. The amount of water is preferably selected in such a way that the sodium sulfate concentration is close to the saturation range, i.e. at about 20 to 30% by weight. Subsequently, the cooling crystallization step is repeated in the manner described above, i.e. the immersion cooler 2 is brought to about 0.degree. C. by introducing a cooling medium and immersed into the sodium sulfate solution obtained. In this case, too, a solid crystal layer of now purified Glauber's salt is obtained after about 8 hours. The remaining sodium sulfate solution can be reused several times and is exchanged as required. The recovery of the purified Glauber's salt can be effected by heating the immersion cooler 2 again to &gt;33.degree. C., the salt melting in its own crystal water and falling into a collecting tank. Alternatively, the recrystallization of the Glauber's salt can be effected by conventional methods, whereby, as a rule, crystalline forms of sodium sulfate which contain less crystal water are produced. The described recrystallization by cooling or evaporation crystallization can be repeated once or several times. In practice, it has become evident that normally two recrystallizations are enough to achieve a sufficient decontamination factor of 1000 to 4000. Generally, the recrystallization is repeated until the desired residual activity is reached. The thus obtained white inactive sodium sulfate can be processed in the conventional way and does not have to be disposed of in an expensive manner as radioactive industrial waste. The depleted evaporator concentrate of step a) still contains about 4-6% by weight of sodium sulfate, i.e. 60-75% of the sodium sulfate have been separated off as inactive matter. The depleted evaporator concentrate is introduced into the evaporation system of the nuclear plant and can be concentrated therein to about 20-25% by volume, i.e., according to the invention the amount of liquid, radioactive industrial waste is reduced by more than 70%. This reduction in volume achieved by the method according to the invention represents an enormous economical advantage. The concentrated evaporator concentrate can either be recycled to separate sodium sulfate as Glauber's salt or it can be finally deposited after having been evaporated and, optionally, stored for decaying. The crystallization apparatus suited to carry out the method according to the invention comprises a container 1, e.g. made of metal or plastics, having a load capacity of e.g. 500 liters. By means of a lifting apparatus, e.g. a pulley block, an immersion cooler 2 consisting of one or more heat exchange elements can be lowered or immersed into container 1. The heat exchange elements are, e.g., plate- or rod-shaped and preferably have a smooth surface. They can, e.g., consist of stainless steel or another corrosion-resistant material. In a preferred embodiment, the immersion cooler 2 is a plate cooler comprising e.g. 5-10 heat exchange plates. The immersion cooler 2 is preferably designed in such a way that one square meter of heat exchange surface is provided for about 70 liters of evaporator concentrate.