| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 161 | METHOD FOR PROCESSING PEROXYGEN SOLUTIONS | US13038171 | 2011-03-01 | US20110217761A1 | 2011-09-08 | John D. Hilgren; Jelte Lanting; Roger John Arthur Tippett |
| The present disclosure relates to a multi-step method for processing peroxygen solutions for reuse or disposal. The method uses an enzyme and a reducing agent. | ||||||
| 162 | Method for oxidizing substance and oxidation apparatus therefor | US11597250 | 2005-05-18 | US07892404B2 | 2011-02-22 | Ryuji Sotoaka; Yoshiya Kimura |
| The present invention provides a method of oxidizing a substance in a liquid containing nitrous oxide (N2O) and an oxidation apparatus therefor. In this method, oxidation of a substance is conducted by allowing a substance to be present in a solution containing nitrous oxide (N2O) and irradiating the solution with light including a wavelength of at least 240 nm or less. | ||||||
| 163 | Composition for the Alkylation and a Method For Detoxifying a Harmful Compound by Using The Composition | US12309494 | 2007-07-26 | US20090326313A1 | 2009-12-31 | Koichiro Nakamura; Akihiro Hishinuma; Shinji Kamiya |
| It is an object of the present invention to provide a beneficial composition in order to detoxify the harmful compound containing arsenic etc. effectively and systematically and a method for detoxifying a harmful compound by using the composition. The composition for the alkylation according to the present invention is characterized in that the composition contains a cobalt complex. The method of detoxifying the harmful compound according to the present invention is characterized in that a harmful compound containing at least one element selected from the groups comprising arsenic, antimony and selenium is detoxified by the alkylation of the harmful compound, in the presence of the composition according to the present invention. | ||||||
| 164 | METHOD FOR VITRIFICATION OF FISSION PRODUCTS | US12443834 | 2007-10-04 | US20090326312A1 | 2009-12-31 | Roger Boen; Agnes Grandjean; Olivier Pinet; Bruno Penelon |
| The mass to be vitrified undergoes a reduction operation in order to have the ruthenium pass from an oxidized state to a metal state in order to reduce the viscosity, the electric conductivity and to obtain good chemical kinetics. | ||||||
| 165 | In-container mineralization | US10972068 | 2004-10-22 | US07476194B2 | 2009-01-13 | John Bradley Mason; Thomas W. Oliver |
| A method of waste stabilization by mineralization of waste material in situ in a treatment container suitable or treatment, transit, storage and disposal. The waste material may be mixed with mineralizing additives and, optionally, reducing additives, in the treatment container or in a separate mixing vessel. The mixture is then subjected to heat in the treatment container to heat-activate mineralization of the mixture and form a stable, mineralized, monolithic solid. This stabilized mass may then be transported in the same treatment container for storage and disposal. | ||||||
| 166 | Method for synthesis of reversion resistant chromium bearing wastes and materials | US11811832 | 2007-06-12 | US20070287877A1 | 2007-12-13 | Keith Edward Forrester |
| This invention provides a method for stabilization of hexavalent chromium and trivalent chromium bearing wastes, materials, and contaminated soils subject to acid and water leaching tests or leach conditions by addition of water solution, hexavalent chromium reducing agent, precipitating and pH increase agent, and chromium reversion control and stabilizing agents such that leaching of chromium is inhibited to desired levels and resists reversion to hexavalent chromium form over time. The resultant material, contaminated soil and/or waste after stabilization and reversion control is deemed suitable for on-site reuse, off-site reuse or disposal as RCRA non-hazardous waste. | ||||||
| 167 | Method for Oxidizing Substance and Oxidation Apparatus Therefor | US11597250 | 2005-05-18 | US20070215454A1 | 2007-09-20 | Ryuji Sotoaka; Yoshiya Kimura |
| The present invention provides a method of oxidizing a substance in a liquid containing nitrous oxide (N2O) and an oxidation apparatus therefor. In this method, oxidation of a substance is conducted by allowing a substance to be present in a solution containing nitrous oxide (N2O) and irradiating the solution with light including a wavelength of at least 240 nm or less. | ||||||
| 168 | Binding and in situ destruction of chemical agents and other contaminants | US11007612 | 2004-12-07 | US20060122451A1 | 2006-06-08 | Viktor Petrik |
| A graphene-containing composition is employed to bind a contaminant, which is then destroyed in situ using microwave irradiation. In preferred aspects of the inventive subject matter, the microwave irradiation has a frequency and energy sufficient to cause electron emission from the graphene. | ||||||
| 169 | Process for the treatment of waste materials | US10891878 | 2004-07-15 | US06926837B2 | 2005-08-09 | Wolfgang Schwetlick |
| The invention relates to a mixture and a process for the treatment of waste materials and the use of the mixture for the treatment of waste materials and waste material treated therewith. The mixture comprises (A) at least one zinc salt of a saturated or unsaturated aliphatic or aromatic carboxylic acid, (B) at least one calcium salt of a saturated or unsaturated aliphatic or aromatic carboxylic acid, (C) at least one hydrophobing agent, (D) at least one amino alcohol and (E) NH3. | ||||||
| 170 | Process and apparatus for treating dioxins | US10310144 | 2002-12-05 | US20030136659A1 | 2003-07-24 | Sataro Yamaguchi; Yasuhiro Hasegawa |
| A process and apparatus assuring low costs and high efficiency in practicing refuse incineration. A applying electromagnetic wave of a frequency band resonant with rotation or vibration of a specific substance e.g., dioxins molecule, thereby to heat the dioxins molecule selectively up to high temperature to remove the dioxins molecule by decomposition. | ||||||
| 171 | Stabilization of arsenic-contaminated materials | US09752225 | 2000-12-29 | US06543964B2 | 2003-04-08 | Ajit K Chowdhury; Lane D Tickanen |
| A method for stabilizing arsenic in a waste matrix includes the steps of combining with the waste matrix an agent for controlling the oxidation-reduction potential of the matrix, an agent for controlling the pH of the matrix and an agent for adsorbing or coprecipitating the arsenic in the matrix. | ||||||
| 172 | Process and apparatus for treating dioxins | US09753713 | 2001-01-04 | US06503463B2 | 2003-01-07 | Sataro Yamaguchi; Yasuhiro Hasegawa |
| A process and apparatus assuring low costs and high efficiency in practicing refuse incineration. A applying electromagnetic wave of a frequency band resonant with rotation or vibration of a specific substance e.g., dioxins molecule, thereby to heat the dioxins molecule selectively up to high temperature to remove the dioxins molecule by decomposition. | ||||||
| 173 | Process and apparatus for treating dioxins | US09753713 | 2001-01-04 | US20010025782A1 | 2001-10-04 | Sataro Yamaguchi; Yasuhiro Hasegawa |
| A process and apparatus assuring low costs and high efficiency in practicing refuse incineration. A applying electromagnetic wave of a frequency band resonant with rotation or vibration of a specific substance e.g., dioxins molecule, thereby to heat the dioxins molecule selectively up to high temperature to remove the dioxins molecule by decomposition. | ||||||
| 174 | Method for treatment of halogen-containing waste material | US09591411 | 2000-06-12 | US06274050B1 | 2001-08-14 | Erik Rasmussen |
| A method for treatment of halogen-containing waste material, in particular PVC-containing waste material, is disclosed. The waste material is heated in a decomposition step in a reaction zone in a substantially closed system essentially without addition of water to a temperature between 150 and 750° C., preferably 250-350° C., in the presence of a halogen-reactive compound selected from alkali and alkaline earth metal hydroxides, alkali and alkaline earth metal carbonates and mixtures thereof, so as to establish a controllable autogenous pressure substantially above atmospheric pressure, in a sufficient reaction time to convert essentially all halogen present in the waste material to alkali or alkaline earth metal halides. The closed system preferably also has a condensation zone, where water vapor and volatile compounds liberated from the waste material are condensed. Remanence obtained in the decomposition step is washed with an aqueous solvent, preferably pure water, and the soluble and insoluble parts of the remanence are separated. By this method the halogen is removed from the waste without uncontrolled emission of halogen-containing acids to the environment. | ||||||
| 175 | Solid waste treatment agent and treatment method of solid waste | US247548 | 1999-02-10 | US6137027A | 2000-10-24 | Masatake Kawashima; Takashi Ogawa; Kazuhiro Terada; Hiroyuki Okayama; Katsushi Sugiyama; Kazuo Hosoda; Masafumi Moriya |
| Disclosed herein are a solid waste treatment agent comprising phosphorous acid or a derivative thereof and/or hypophosphorous acid or a derivative thereof, or phosphorous acid or a derivative thereof and/or hypophosphorous acid or a derivative thereof, and an aluminum compound and/or a titanium compound, and a method of treating solid waste, which comprises adding the solid waste treatment agent to solid waste containing harmful metals and/or organic chlorinated compounds such as dioxins and PCB to make the solid waste harmless. When the solid waste treatment agent comprising phosphorous acid or a derivative thereof and/or hypophosphorous acid or a derivative thereof, and titanium oxide, or comprising phosphorous acid or a derivative thereof and/or hypophosphorous acid or a derivative thereof, titanium oxide and an aluminum compound is used as a solid waste treatment agent to treat solid waste under irradiation of rays, the solid waste can be effectively made harmless even when the treatment is conducted at a relatively low temperature. | ||||||
| 176 | Methods for neutralizing/detoxifying and stably fixing/solidifying hazardous compounds | US138952 | 1998-08-24 | US5986161A | 1999-11-16 | Yukoh Akae; Kazuo Kote |
| Hazardous compounds are chemically treated to remove various pollutants by subjecting the compounds (samples) to various process steps, including selecting specific solvents and using them, treating the sample at room temperature or below (30.degree. C. or lower); separating fatty acids mixed with heavy metal and semi-metal compounds as well as the separation of organic substances (including halogenated compounds) added to heavy metals and semi-metals; and using sodium nitrite and sodium 1-naphthylamine-4-sulfonate in combination from specific solvents, thereby in the sample, adsorbing and fixating halogen substances related to air pollution, coagulation resulting from the decomposition of fatty acids and the fixation of such compounds by quicklime and graphite and the stable fixation of heavy-metal oxide and semi-metal compounds using solvents having redox action and the formation of their complex salts and compounds, the above being accomplished by a continuous processing method. | ||||||
| 177 | Method for destroying organohalogen compounds | US658646 | 1996-06-05 | US5977427A | 1999-11-02 | Shin Tamata; Satoru Ohashi; Toshihide Takano; Hisao Yokoyama; Toshihiro Mori |
| A process is provided for the destruction of organohalogen compounds, such as methyl chloride, chloroform, carbon tetrachloride, etc., by mixing the organohalogen compounds with a heated carrier gas, such as nitrogen, argon or air, and either steam or water to form a mixture; supplying the mixture to a catalyst, such as titanium oxide/tungsten oxide, to decompose the organohalogen compounds into halogens and hydrogen halides, such as chlorine, hydrochloric acid, fluorine and hydrofluoric acid; conducting the halogen and hydrogen halide contaminated gas through a bent path, created by a baffle that prevents the entry of mist or droplets into the catalyst chamber, into a cooling section where the halogen and hydrogen halide contaminated gas is sprayed with water to cool the gas to a temperature low enough to prevent the formation of dioxines. An alkaline agent, such as sodium hydroxide, can be added to the cooling water to neutralize the halides and hydrogen halides. | ||||||
| 178 | Method of decomposing CMPO | US35064 | 1998-03-05 | US5965003A | 1999-10-12 | Masaki Ozawa; Yasumasa Tanaka; Yoshihiro Hoshino; Hiroyuki Tanuma; Chisako Kawakami; Takamichi Kishi |
| CMPO is safely, reliably and rapidly decomposed under mild conditions. A CMPO-containing substance is emulsified in an electrolyte comprising an oxidation promoter (silver ion) by an emulsifier in an emulsifying tank, this electrolyte comprising the CMPO-containing substance is supplied to an anode chamber, and an electrolytic oxidation reaction is performed by passing an electric current. By emulsifying the CMPO-containing substance, the surface area of CMPO in contact with electrolyte is increased, and electrolytic decomposition is thereby promoted. As sufficient CMPO decomposition is not obtained by passing the emulsion only once through an electrolysis tank 1, a batch oxidation method is employed wherein an anolyte is recirculated by a recirculating pump 3a through the anode chamber, a constant temperature bath 7a and an emulsifying tank 6, so that electrolysis is performed with the CMPO-containing substance permanently emulsified in the electrolyte. To maintain a catholyte in a cathode chamber at the same temperature as the anolyte, the catholyte is recirculated by a recirculating pump 3b between the cathode chamber and a constant temperature bath 7b. The current supplied to an anode 4 and cathode 5 in the electrolysis tank 1 is controlled by a rectifier 8. | ||||||
| 179 | Vitrification of waste | US866780 | 1992-04-01 | US5891011A | 1999-04-06 | George G. Wicks |
| A method for encapsulating and immobilizing waste for disposal. Waste, preferably, biologically, chemically and radioactively hazardous, and especially electronic wastes, such as circuit boards, are placed in a crucible and heated by microwaves to a temperature in the range of approximately 300.degree. C. to 800.degree. C. to incinerate organic materials, then heated further to a temperature in the range of approximately 1100.degree. C. to 1400.degree. C. at which temperature glass formers present in the waste will cause it to vitrify. Glass formers, such as borosilicate glass, quartz or fiberglass can be added at the start of the process to increase the silicate concentration sufficiently for vitrification. | ||||||
| 180 | Method for the disposal of explosive material | US834833 | 1997-04-10 | US5763736A | 1998-06-09 | Eduard Daume |
| A method for the decomposition of explosive materials into water-soluble products is offered, which can be disposed of in a thermal or biochemical way, which requires only very short reaction times because of the addition of polar, aliphatic, non-saponifiable compounds to a strongly basic, preferably aqueous reaction medium and under temperature control by means of the metered addition of the explosive materials. | ||||||
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