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    • 7. 发明申请
    • OZONE CLEANING SYSTEM
    • 臭氧清洁系统
    • WO2008112947A1
    • 2008-09-18
    • PCT/US2008/056936
    • 2008-03-14
    • FOOD SAFETY TECHNOLOGY, LLCLYNN, Daniel W.
    • LYNN, Daniel W.
    • C01B13/10
    • C11D3/3947B01F3/04475B01F3/04503B01F3/04985B01F5/0068B01F5/0415B01F13/065B01F2003/04886B01F2215/0468B08B2203/005C01B13/10C02F1/78C11D11/0041
    • An industrial cleaning system 10 that produces and distributes an aqueous ozone solution is described. The system 10 includes an ozone generator 240 for generating ozone gas, which is injected by an injector 310 into a supply of water to form the aqueous ozone solution. A reaction vessel 350 receives the aqueous ozone solution from the injector 310 as the reaction vessel 350 reduces the bubbles of ozone gas in the aqueous ozone solution to increase the oxidation reduction potential of the aqueous ozone solution. The reaction vessel 350 includes a conical-shaped surface 385 having two or more edges 380 or ridges 382. The conical-shaped surface 385 defines a generally hollow interior 388. An inlet port 355 is in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface 380. Nozzles 360 direct water under pressure at the conical-shaped surface 380, and the water mixes with the aqueous ozone solution from the inlet port 355. An outlet 390 is in fluidic communication with the industrial cleaning system 10. A method of making an aqueous ozone solution is described. The reaction vessel 350 is in fluidic communication with a supply of a first aqueous ozone solution. The first aqueous ozone solution is directed to the reaction vessel 350. Water is directed to the reaction vessel 350, and the water and the first aqueous ozone solution are mixed to form a second aqueous ozone solution. Compositions for aqueous ozone solutions are also described. The aqueous ozone solution contains approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous ozone solution that has an oxidation reaction potential of up to approximately 2.6 and having an ozone concentration of up to approximately 20 ppm.
    • 描述了产生和分布臭氧水溶液的工业清洁系统10。 系统10包括用于产生臭氧气体的臭氧发生器240,臭氧发生器240由注射器310注入水源以形成臭氧水溶液。 当反应容器350减少臭氧水溶液中的臭氧气泡时,反应容器350接收来自注射器310的臭氧水溶液,以提高臭氧水溶液的氧化还原电位。 反应容器350包括具有两个或多个边缘380或脊382的圆锥形表面385.圆锥形表面385限定大致中空的内部388.入口端口355与臭氧溶液水溶液流体连通 将臭氧水溶液供应到锥形表面380.喷嘴360在锥形表面380处引导压力下的水,并且水与来自入口355的臭氧溶液混合。出口390处于流体连通 与工业清洁系统10一起描述制备臭氧水溶液的方法。 反应容器350与第一含水臭氧溶液的流体连通。 将第一臭氧水溶液引导至反应容器350.将水引导至反应容器350,并将水和第一臭氧水溶液混合以形成第二臭氧水溶液。 还描述了臭氧水溶液的组合物。 臭氧水溶液含有约1体积份的水,其混合约4体积份至约9体积份的第一臭氧水溶液,以形成氧化反应电位高达约2.6的第二臭氧水溶液,并具有 臭氧浓度高达约20ppm。