Patent GB-487066-A (GB)
Title: Improvements in or relating to the production of heavy water
IPC: C01B5/02
Filed: 1936-12-22
Abstract: In obtaining heavy water in the course of the generation of hydrogen or gaseous mixtures containing hydrogen by reduction of water with a chemical reducing agent, the reduction of water to hydrogen or hydrogen containing gases and an enrichment of water with deuterium compounds by the contact of the hydrogen with water are effected in two stages constituting in combination a sequence, the first stage comprising the reduction of water and the second stage comprising contacting water with hydrogen or hydrogen containing gases so as to effect an exchange of deuterium between hydrogen and water until equilibrium is established without any further substantial reduction of water to hydrogen, and the sequence is then repeated, the water so enriched with deuterium compounds being wholly or in part reduced with a chemical reducing agent to hydrogen or hydrogen-containing gaseous mixtures and the deuterium being withdrawn again by means of water or water already enriched with deuterium compounds from the hydrogen obtained by the reduction process and enriched with deuterium.  The second stage may be carried out in the presence of catalysts such as nickel or platinum group metals (e.g. platinum black), iron oxide activated with chromium, or a mixture of magnesium oxide and carbon with or without potassium carbonate. Chromium oxide or zinc oxide also may be used.  The temperature of the second stage may be about, or even below, 100 DEG  C.  According to one example, the first stage consists in reacting one mol of carbon monoxide (in the form of water gas) with three mols of water vapour, the reaction being conducted under pressure as described in Specification 417,829. In the second stage the gaseous mixture comprising 2 mols of hydrogen and 2 mols of water vapour is contacted with platinum black at slightly above 100 DEG  C., the gaseous mixture being subsequently cooled to condense the water.  Two mols of enriched water having a ratio of DHO : H2O of 1 : 1950 are thus obtained and, after evaporation and dilution with one mol of fresh steam are returned to the conversion, stages 1 and 2 being repeated.  Two mols of water having a ratio of DHO : H2O of 1 : 1650 are thus obtained. A third repetition results in 2 mols of water the ratio being 1 : 1550. After having obtained 32 mols having this last ratio, 12 mols are decomposed by contact with carbon to produce a gaseous mixture consisting of 12 mols of carbon monoxide and 12 mols of hydrogen which is used with the remaining 24 mols of water to repeat stages 1 and 2 as above described until used up, 8 mols of water having a ratio DHO : H2O of 1 : 1000 being obtained. Further concentration is effected by proceeding in like manner. According to a second example, the first stage consists of decomposing 1 mol of water in contact with carbon at a temperature above 1000 DEG  C. to produce a gas mixture consisting of one mol of carbon monoxide and 1 mol of hydrogen which in the second stage is conducted together with one mol of water vapour into a vessel charged with platinum black maintained at just above 100 DEG  C.  The gases are then cooled to condense water having a ratio DHO : H2O of 1 : 1950.  Half this water is then similarly decomposed in the first stage and contacted with the remaining water in the second stage, and so on until any desired degree of enrichment has been attained.  Hydrogen enriched in deuterium from any stage can be successively contacted with water having a progressively lower deuterium content, the deuterium content of the hydrogen thus being withdrawn.  Water impoverished with heavy water can also be obtained by operating in the reverse manner, i.e. by oxidizing hydrogen or hydrogen containing gases to water combined with impoverishing hydrogen of deuterium by contact with water, the hydrogen so impoverished being introduced in part into the oxidation process, and the deuterium being withdrawn again by means of water obtained in this manner.  Specification 462,191 also is referred to.