Patent Number: 044902883
Section: summary

BACKGROUND OF THE INVENTION 1. Field to which the invention relates: The present invention relates to methods and systems for removing tritium from a gas, as air. 2. The prior art: In many nuclear- and plasma-physical experiments and work, gaseous tritium (T.sub.2) is produced. Since this is known to be radioactive and, thus, a health hazard, generally it must be removed from the atmosphere in the relevant work-area or the like. It is known to withdraw tritium-containing air out of work areas, glove-boxes, or the like by means of a blower, and to convert the tritium, with oxygen, into tritium-containing water in a catalytic furnace which may contain CuO, Pd or Pt as a catalyst. The resulting water is then absorbed in a molecular sieve. Conventional modern tritium-separating systems contain, in addition to the catalytic furnace and the molecular-sieve, which are the main components, also heating devices, cooling devices, heat-exchangers and the like. It is possible in this way to achieve a final concentration of some 10.sup.-5 Ci per cubic metre of air. In practice, however, one must often be content with some 10.sup.-4 Ci/m.sup.3. The factors governing the minimal obtainable tritium concentration in the purified air are still largely uncertain. The partial water-vapour pressure in the molecular sieve, and the yield from catalytic oxidation, are assumed to be important. Even with a 1% loading of a molecular sieve, the partial water-vapour pressure at 20.degree. C. for optimum performance amounts to about 10.sup.-7 torrs which corresponds in relation to THO to a tritium activity of 2.10.sup.-4 Ci/m.sup.3 of air. This immediately indicates a serious disadvantage of modern purification technology: since the humidity in the ambient air is absorbed from the molecular sieves simultaneously with the tritium-containing water the loading limit of the molecular sieves (about 1%) is soon reached. The molecular-sieve columns must therefore either be made correspondingly large or must be frequently regenerated, and this leads to large quantities of contaminated water. With incomplete catalytic oxidation of the tritium into water, gaseous tritium remains. This passes unimpeded through the molecular sieves and is thus present as an inadmissible output-air activity. Attempts have been made to eliminate the disadvantages of the above-mentioned methods by cooling the molecular sieves with liquid nitrogen and with novel noble-metal catalysts, but the results have not been satisfactory. SHORT SUMMARY OF THE INVENTION An object of the present invention is to provide a method and an apparatus by means of which tritium may be more completely removed from a gas mixture than has hitherto been possible. According to the invention, this purpose is achieved in that the tritium is subjected to a hydrogenation-reaction. According to the invention, therefore, the known oxidizing process, whereby tritium is oxidized to water, is replaced or extended by a reducing or hydrogenating process which delivers an easily separable, liquid or solid reaction-product. In this connection, conversion of the tritium with oxygen to water is not included in the terms reducing or hydrogenating process. Hydrogen and therefore also tritium, especially in the atomic form, reacts more or less easily with other atoms or molecules, especially with unsaturated hydrocarbon compounds. Suitable and proven hydrogenation reactions are the hydrogenation of carbon and petroleum, fat hardening (hydrogenating oily fats to solid fats), the addition of hydrogen on double or triple bonds (e.g. the conversion of benzene into cyclohexane, or of naphthaline into decaline and tetraline), the reduction of aldehydes and ketones to alcohols, and of nitriles and nitrocompounds to amines. Heavy petroleum fractions may be converted by so-called "hydrocracking" into products with low boiling ranges. The process is carried out at moderate temperatures and pressures in the presence of noble metal catalysts. The use of 100 parts by weight of heavy vacuum gas oil and 3 parts by weight of hydrogen produces, for example, after one passage: 3.2 parts by weight NH.sub.3 +H.sub.2 S, PA0 2.5 parts by weight C.sub.1 --to C.sub.3 --fractions, PA0 3.6 parts by weight C.sub.4 --fraction, PA0 8.7 parts by weight C.sub.5 --and C.sub.6 --fractions, PA0 14.8 parts by weight C.sub.7 --fraction, and PA0 70.3 parts by weight of a high-boiling fraction (according to: READ, D, C. H. Watkins and J. G. Eckhouse; Oil Gas J. 63, 86 (24.5.1965). It is thus possible, in principle, to control hydrogenation in such a manner that that longer-chain hydrocarbons are converted into shorter-chain hydrocarbons. As will be explained hereinafter in more detail, this is a particular advantage of the method according to the invention. It is highly advantageous to remove tritium from a gas-mixture by hydrogenation of unsaturated organic compounds, more particulary unsaturated carboxylic acids. It is particularly advantageous to use unsaturated monocarboxylic acids, in which case the hydrogenation is preferably carried out catalytically. It is preferable to use unsaturated fatty acids, especially those containing between 5 and 20 C atoms. For example, linolenic acid (C.sub.17 H.sub.29 --COOH) has three double bonds: EQU CH.sub.3 --CH.sub.2 --CH.dbd.CH--CH.sub.2 --CH.dbd.CH--CH.sub.2 --CH.dbd.CH--(CH.sub.2).sub.7. COOH and linoleic acid C.sub.17 H.sub.31 --COOH has two: EQU CH.sub.3 --(CH.sub.2).sub.4 --CH.dbd.CH--CH.sub.2 --CH.dbd.CH--(CH.sub.2).sub.7 --COOH Upon hydrogenation, both are converted to stearic acid (CH.sub.3 --(CH.sub.2).sub.16 --COOH, If the unsaturated monocarboxylic acids are hydrogenated with tritium, the tritium is firmly bonded in the stearic acid, i.e. one or more of the CH.sub.2 groups contains T instead of H. The hydrogenation process may be controlled in such a manner that the tritiated stearic acid is split up, by incorporation of the tritium, into fractions having shorter chain-lengths, and physical propertics other than the long-chain C.sub.17 fatty acids. This has the major advantage that the tritium-containing reaction-product, because of differences in solubility, density, melting point and boiling point, can be separated continuously or intermittently from the compounds not reacted with tritium and may be removed from the hydrogenation product. A fresh reaction partner is therefore always available for hydrogenation and only relatively small amounts of tritium-containing, radioactive reaction-products are produced. The hydrogenating device, or column, may be in the form of a fixed bed, a fluidized bed, a liquid column, or an emulsion column. The method and apparatus according to the invention are well suitable for cleaning the exhaust air from workshops and for circulatory cleaning of closed systems such as inert-gas glove-boxes. In the case of inertgas glove-boxes there is the advantage that autoxidation of the preferably used unsaturated fatty acids cannot take place because of the absence of any atmospheric oxygen, and the efficiency cannot therefore be reduced (no high "idle consumption" of unsaturated fatty-acids, no resinification, etc.). If an apparatus, operating according to the method of the invention, is used as an emergency or safety-system, all conceivable disadvantages (autoxidation, decomposition of compounds) will be minimized, since the comparatively low costs of the chemicals used are immaterial. The invention provides the following advantages: Conventional systems will always depend upon the efficiency of the oxidizing reaction and unconverted T.sub.2 gas leaves known installations unimpeded. Particularly in areas of high atmospheric humidity, the maximal permissible loading of the molecular sieves will rapidly be exceeded. Residual-gas activity then increases rapidly. These disadvantages are essentially avoided by the method according to the invention. Especially if the conventional oxidizing process is combined with the reducing or hydrogenating process according to the invention, both tritium-containing water and T.sub.2 are very largely eliminated from purified gas-mixtures. In case of an emergency system, the method according to the invention provides the particular advantage that "breakthrough concentrations" (&gt;1% concentration of water-vapour) at the molecular sieve, and therefore activities above 10.sup.-5 Ci/m.sup.3, cannot arise. With the method acording to the invention, continuous replacement of the consumed reaction-partners (hydrogenated fatty acids), and thus continuous operation, is possible, no regeneration pauses are necessary, and the activity cannot therefore rise. In inert-gas containments also very low concentrations of the T can be eliminates continuously.