http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-3628236-A1

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filingDate 1986-08-20-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3fb4181966e4668f97477642e126df51
publicationDate 1988-02-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber DE-3628236-A1
titleOfInvention METHOD FOR PRODUCING AN OZONE-CARRIER GAS MIXTURE
abstract For diverse applications in the chemical and pharmaceutical industries, pure ozone in a carrier gas which can be, for example, N2, CO2 or else a noble gas is required. However, the gas mixture flowing out of an ozone generator contains proportions of O2, N2 and possibly even NOx and is not suitable for such applications. A downstream O3/O2 separation stage such as, for example, ozone adsorption on silica gel can in principle achieve this object, but requires great technical effort if a complete O2/O3 separation is desired. It is therefore proposed that the separation be carried out via a liquefaction of the ozone proportion at the exit of the ozone generator (4). Ozone can be liquefied at temperatures as high as -112 DEG C, far above the liquefaction point of oxygen or of nitrogen. Since liquid ozone has a very high energy content and its handling is associated with certain hazards, the plant is operated in such a way that there is always only a small amount of liquid ozone present in the apparatus and this is continuously transferred into an inert carrier gas (for example N2, CO2, noble gas). <IMAGE>
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priorityDate 1986-07-17-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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Total number of triples: 31.