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In the artificial manufacture of mineral water, carbon-dioxide is similarly intro- duced under greater or lesser pressure, which in any event, however, is greater than 1 atmosphere, wherein a sufficient quantity of certain salts is admixed as the taste of the mineral water demands. A fur- ther well-known method of producing effervescent drinks consists in dissolving any easily soluble carbonate (sodium bicarbonate for example) and adding weak acids (such as tartaric or citric acid), through which free carbonic acid is similarly evolved, which is the cause of the prickly taste of the drink thus created. The present case, however, concerns the production of water of a kind in which car- bon-dioxide is not merely concentrated in unbound form, but is -contained in bound form, and in every respect is similar to good, high-grade springwater, wherein the manufacturing process emu- lates the processes in Nature as far as possible. Sterilised water flows down pipe m under a cold, mercury-vapour lamp and mixes with the salt solution coming from duct l. In vessel C the salts are actually dis- solved and well stirred by mixer g. The quantity and type of salt is naturally dependent on the composition of the par- ent water, which in most cases will be any variety of surface water exhibiting certain permanent degrees of hardness. On the other hand, through the addition of salts, the hardness of the water to be produced should not be caused to exceed 12 degrees, otherwise the product would be difficult for industry to use. For every 10 litres of any average quality parent water, 1 litre of salt solution is prepared in which about 0.02g sodium-chloride, 0.02g magnesium- sulphate, 0.02g sodium-biphosphate, 0.008g potassium-nitrate and 0.2g calcium- oxide are dissolved. The type and quantity of these salts are the result of several hun- dred experiments. Since in the beginning the calcium-oxide is only partially dis- solved in the water, and on the other hand, the evolving calcium hydrate is sensitive to atmospheric carbon-dioxide, the vessel is sealed against light and air. In order to maintain a constant rate of discharge from vessel C, it is placed under a constant pres- sure of 0.1 atmospheres = 1 water-column metre. The concentrated salt solution is continuously added to the water in pipe m drop by drop and the mixture of both flu- ids flows into the atomising unit D, where it is sprayed into the interior of the vessel through the small holes n in the pipe, whereas the already previously prepared carbonated water is sprayed outwards from atomising pipe k. The droplets of both types of water then precipitate, mixing together drop by drop en route in the same way that in Nature every drop on its way down into the Earth first dissolves salts and absorbs gases. This quantity of water now flows into unit E containing tulip-like glass bulbs and always rises up in the outer glass tulip, subsequently to be made to descend in the inner glass tulip, in order to rise further through the innermost riser pipe into the next higher outer tulip. During this process the water therefore follows a meander-like path en route to the process- es described later. The gas, that is to say, predominantly the carbon-dioxide, always accumulates in the upper part of the tulip and once the pressure has risen sufficient- ly, will then be continuously injected into the path of the rising water in the inner- most riser pipe via the tube r, in which the very finest jets have been incorporated, so that any carbon-dioxide not previously bound, will be forced to bind itself with the water. On the axis of this component of the apparatus, an alternating series of gold and silver laminates are attached, but which are insulated from each other. A cer- tain potential is created between both met- als, giving rise to the weak ionisation of the water. Further along its path, the water enters the main mixer F. This consists of an exter- nally thermally-insulated cylindrical metal vessel, silver-plated on the inside, incorpo-PDF Image | The Water Wizard
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