| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | 用于处理废料的混合物 | CN00811201.0 | 2000-08-02 | CN1373680A | 2002-10-09 | 沃尔夫冈·施韦特利克 |
| 本发明涉及一种用于处理废料的混合物和方法以及所述的混合物用于处理废料和用它处理过的废料应用。所述的混合物含有:(A)至少一种饱和的或不饱和的脂族的或芳族的羧酸锌盐;(B)至少一种饱和的或不饱和的脂族的或芳族的羧酸钙盐;(C)至少一种疏水剂;(D)至少一种氨基醇;以及(E)NH3。 | ||||||
| 22 | 处理含PVC废料的方法 | CN96193323.2 | 1996-03-22 | CN1083730C | 2002-05-01 | E·拉斯穆森 |
| 公开了一种处理含卤素特别是含PVC废料的方法，其包括一个分解步骤，其中在大体上密封的体系中的反应区域中在基本上不加水的条件下在与卤素反应的选自碱金属和碱土金属氢氧化物、碱金属和碱土金属的碳酸盐和它们的混合物的化合物的存在下加热废料至150～750℃，优选250-350℃，以便产生实质上高于大气压的可控制的自生压力，经过足够的反应时间在废料中存在的所有卤素基本上转化为碱金属或碱土金属的卤化物，所述的密封体系优选包括一个冷凝区域，在该冷凝区域中冷凝从废料中释放的水蒸汽和易挥发化合物。使用含水溶剂优选纯水冲洗在分解步骤中得到的剩余物，并分离剩余物的可溶和不溶部分。通过该方法从废料中除去卤素，而不致于无控制地向环境中排放含卤素的酸。 | ||||||
| 23 | 处理含卤素废料的方法 | CN96193323.2 | 1996-03-22 | CN1181711A | 1998-05-13 | E·拉斯穆森 |
| 公开了一种处理含卤素特别是含PVC废料的方法,其包括一个分解步骤,其中在大体上密封的体系中的反应区域中在基本上不加水的条件下在与卤素反应的选自碱金属和碱土金属氢氧化物、碱金属和碱土金属的碳酸盐和它们的混合物的化合物的存在下加热废料至150～750℃,优选250—350℃,以便产生实质上高于大气压的可控制的自生压力,经过足够的反应时间在废料中存在的所有卤素基本上转化为碱金属或碱土金属的卤化物,所述的密封体系优选包括一个冷凝区域,在该冷凝区域中冷凝从废料中释放的水蒸汽和易挥发化合物。使用含水溶剂优选纯水冲洗在分解步骤中得到的剩余物,并分离剩余物的可溶和不溶部分。通过该方法从废料中除去卤素,而不致于无控制地向环境中排放含卤素的酸。 | ||||||
| 24 | 含卤素、磷、硫和/或金属元素的有机化合物的处理方法 | CN96103916.7 | 1996-03-07 | CN1136971A | 1996-12-04 | E·布泽兹基 |
| 为处理在原子键上除了碳、氢和氧元素外，还包括卤素、磷、硫和/或金属元素的危险或有毒有机化合物，提出了使该有机化合物电离，紧接着进行电渗析的方法，此离子态的最终反应产物可容易操作，并且可毫无问题地进一步使用或以填埋或焚烧方式处理。在电离辐射作用下发生电离。本发明方法特别适合处理含卤素的芳族化合物如各种农药。 | ||||||
| 25 | 物料的处理 | CN93103682.8 | 1993-03-04 | CN1081923A | 1994-02-16 | R·T·迪牧; T·N·卡尼; I·M·奥格尔维; A·E·茫迪; P·D·泽曼切夫; A·I·维特 |
| 一种物料处理方法，尤其是降解废料的方法。该方法包括对等离子体喷管和热区内的废料进行热解，物料从喷管流入热区内，废物料以细小的雾状物和/或气体的形式输送到喷管中，输入方向通常横向于等离子体穿过喷管的运动方向。输入装置所在的位置应使得废料能直接输送到等离子体的中心区域，热区是一长的管子，以使得物料能够彻底被热解，热区后面紧接着是冷却区，在冷却区物料被迅速急冷，进入冷却区的物料的温度应高于物料中CO还原成CO2的温度。物料流体上含有颗粒碳，当物料进入冷却区和/或随后的洗涤区的碱性溶液中时，颗粒碳用于吸附残留的有毒化合物。 | ||||||
| 26 | 핵분열 생성물의 유리화 방법 | KR1020097006834 | 2007-10-04 | KR1020090060325A | 2009-06-11 | 보엥로제르; 그랑장아그네; 삐네올리비에; 뻬네롱브뤼노 |
| The mass to be vitrified undergoes a reduction operation in order to make ruthenium pass from an oxidized state to a metallic state in order to reduce the viscosity, the electrical conductivity and to obtain good chemical kinetics. | ||||||
| 27 | 유독성금속을함유한폐기물의열처리방법 | KR1019960016469 | 1996-05-16 | KR100460688B1 | 2005-01-27 | 까르띠에르레네; 본로거; 빈센장-쟈끄; 라우랑올리비에 |
| A process for the thermal treatment of wastes contg. one or more toxic metals is claimed. This is effected in the presence of a phosphorus-based reactant in a quantity sufficient to convert the toxic metal(s) to the corresp. phosphate(s). Also claimed, is the application of the process to chlorinated, brominated, or radioactive wastes. | ||||||
| 28 | 황산염환원균을 이용한 소각재 처리방법 | KR1019990034333 | 1999-08-19 | KR1019990083846A | 1999-12-06 | 정권 |
| 본발명은소각재황산염환원균을이용하기위하여, 기존의매립시설구조에매립물의상호보완적특성을고려하여합리적이며계획적으로매립하여소각재의중금속을불용화시키고유기물의안정화를유도하는소각재처리방법에관한것으로, 소각재에황산염환원균을포함하는유기성폐기물을함께매립하여상기황산염황원균이상기소각재내의황산염을환원시켜그 결과로생성된황화물을상기소각재내의중금속과결합시켜불용성금속황화물로침전시키도록구성되는소각재처리방법과소각재내의중금속을황산염환원균이불용성금속황화물로침전시키도록소각재및 황산염환원균을포함하는유기성폐기물을함께매립하고복토를덮어매립물을형성하는소각재처리방법을제공하며, 황산염환원균에의하여소각재의중금속을안전한금속황화물로침전시켜고형화시킬수 있으며, 그결과로소각재를처리함에있어서중금속의용출로인한주변의토양및 수질오염의가능성을획기적으로줄일수 있다. | ||||||
| 29 | ペルオキシゲン溶液の処理方法 | JP2012555528 | 2011-03-02 | JP6001458B2 | 2016-10-05 | ジョン ディー.ヒルグレン; イェルテ ランティング; ロジャー ジェイ.エー.ティペット |
| 30 | フッ素系有機化合物の分解方法、及びフッ素系有機化合物の分解装置 | JP2014083193 | 2014-04-14 | JP2015202454A | 2015-11-16 | 堀 久男; 加藤 昌明 |
| 【課題】新しく、効率の良いフッ素系有機化合物の分解方法、及びそのような方法を実施するのに有用なフッ素系有機化合物の分解装置を提供すること。 【解決手段】本発明は、分解対象であるフッ素系有機化合物に対して、電解硫酸の存在下で光照射することを特徴とするフッ素系有機化合物の分解方法である。すなわち、硫酸水溶液を電気分解した際に陽極側にて得られる電解硫酸に、分解対象となるフッ素系有機化合物を加えて光照射を行うことにより、そのフッ素系有機化合物をフッ素イオンや二酸化炭素まで分解させることを特徴とする。これにより、従来のように高温で燃焼してフッ素系有機化合物を分解する必要がなくなり、分解のためのエネルギーコストを削減できる。 【選択図】図3 |
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| 31 | Asbestos processing agents and asbestos processing method | JP2010233955 | 2010-10-18 | JP5010021B2 | 2012-08-29 | 公明 原野; 吉弘 田口; 輝彦 草野 |
| 32 | Disposal of the refrigerant | JP51835398 | 1997-09-22 | JP3930571B2 | 2007-06-13 | サティアパル，スニタ; エイチ． シエネル，トビアス; ディー フレイハウト，ジェイムス; ハーヴェイ． マイケル，エイチ |
| 33 | Heat treatment method of the toxic metal-containing waste | JP12352696 | 1996-05-17 | JP3891605B2 | 2007-03-14 | オリヴィエ・ローラン; ジャン−ジャック・ヴァンサン; ルネ・カルティエ; ロジェ・ブワン |
| 34 | Method and device for making polyvinyl chloride harmless | JP21057299 | 1999-07-26 | JP2001037905A | 2001-02-13 | KATAYAMA HIDEO |
| PROBLEM TO BE SOLVED: To reduce generation of harm substances by emulsifying polyvinyl chloride liquid, aluminum oxide, and silicon dioxide within a supersonic emulsification device, and by treating emulsified substances in an electric resistance furnace at a specific temperature to vitrify them. SOLUTION: Mixture members of polyvinyl chloride liquid, aluminum oxide, and silicon dioxide are inserted into a supersonic emulsification device 2 and are emulsified at a temperature of 1500 to 2000°C. This emulsified mixture member is conveyed through an electromagnetic valve V2, a pump P2, a pipe 21, a monitoring section 8, an electric resistance measuring section 9, and an electromagnetic valve V5 to an electric resistance furnace 5, is melted vitrified at a melting temperature of 1500 to 2000°C, is discharged from a discharging section 11, and is cooled and hardened to form a glass member. Emulsified and mixed conditions are monitored through a glass window provided at the monitoring section 8, and the electromagnetic valves V1, V4, V5, the pumps P1, P2, and the like are controlled according to a measured electric resistance valve of the electric resistance measuring section 9. In this way, generation of harm substances can be reduced and treated. COPYRIGHT: (C)2001,JPO | ||||||
| 35 | Cmpo decomposing method | JP6432597 | 1997-03-18 | JPH10249350A | 1998-09-22 | OZAWA MASAKI; TANAKA YASUMASA; HOSHINO YOSHIHIRO; TANUMA HIROYUKI; KAWAKAMI CHISAKO; KISHI TAKEMICHI |
| PROBLEM TO BE SOLVED: To rapidly decompose CMPO (octyl(phenyl)-N,N- diisocutylcarbamoilmethylphsophine oxide) safely, surely and by a mild condition. SOLUTION: The CMPO-containing matter is emulsified in an electrolyte containing an oxidation accelerating agent (silver ion) by an emulsifying machine of an emulsifying tank 6, and the electrolyte is fed to an anode chamber, and an electrolytic oxidation reaction is executed by energizing. An electrolysis is accelerated since a surface area of the CMPO containing with the electrolyte is enlarged by emulsifying the CMPO-containing matter. Since a sufficient CMPO decomposition is not attained by passing only once the electrolyte through an electrolytic cell, a batch type oxidizing method is adopted, and the anode liq. is circulated between the anode chamber, a thermostatic bath 7a and the emulsifying tank 6 by using a circulating pump 3a, and the electrolysis is continued in a state in which the CMPO-containing matter is always emulsified in the electrolyte. The cathode liq. is circuilaed between a cathode chamber and the thermostatic bath 7b by using the circulating pump 3b. And in the anode 4 and the cathode 5 is the electrical cell 1, a supplied current is controlled by a rectifier 8. COPYRIGHT: (C)1998,JPO | ||||||
| 36 | A method of reducing the chlorine content in the chlorinated hydrocarbon | JP51208694 | 1994-10-14 | JPH09503789A | 1997-04-15 | シュワルツ、ジェフレイ; リウ、ユミン |
| (57)【要約】 空気や水分の存在を許容できる環境において塩素化炭化水素またはハロゲン化芳香族炭化水素中の塩素または塩化物は、塩素化炭化水素またはハロゲン化芳香族炭化水素を試薬であって、（ｉ）少なくとも２つの酸化状態を有する実質的に非毒性錯体と（ｉｉ）錯体を第２酸化状態から最初の酸化状態に錯体を還元的に戻すことができる還元剤からなるものと接触させることにより減少することができる。 代表的な実施態様には、ビス−（η 5 −シクロペンタジエニル）チタンジクロリドとナトリウムテトラヒドリドボレートが含まれる。 任意に、反応は脂肪族または芳香族のアミンの存在下、または必要により不活性有機溶媒の存在下に行うことができる。 | ||||||
| 37 | Treatment of organic compound and apparatus therefor | JP5208896 | 1996-03-08 | JPH0975709A | 1997-03-25 | EEDOARUTO BUZETSUKII |
| PROBLEM TO BE SOLVED: To make it possible to neutralize dangerous compds. by subjecting the compds. to be treated to ionization, dividing the resulted product ionized by electrodialysis and subjecting the final resulted ionic products and residual org. materials to known use or filling up of land or to a treatment by incineration. SOLUTION: A raw material mixture in an equipment section I is supplied from a tank 20 to an ionization section II via a line 21 having a pump and valve. The materials to be treated by the influence of an ionization device 22 in this ionization section II are divided and separated in a dialysis device 23. The org. materials which are rare materials in the dialysis section II are discharged form the dialysis device 23 by a line 24. On the other hand, the inorg. reaction product/condensate and a caustic or salt soln. are supplied via lines 29, 30 to circulation paths 25, 26 and are discharged from discharge lines 27, 28. The discharged materials are used for filling up of land or are treated by incineration. As a result, the dangerous compds. as harmful biotic pesticides, e.g. insecticides and herbicides, are neutralized and treated. | ||||||
| 38 | Method and apparatus for reduction and control of organic substances | JP51281693 | 1993-01-26 | JPH08501016A | 1996-02-06 | エマリー，チャールズ，レスリー |
| (57)【要約】 有機物質を還元性雰囲気中でマイクロ波放射に暴露することからなる、有機物質をコントロールして非熱分解的に還元する方法および装置が提供される。 この方法を実施する装置は、マイクロ波のチャンバー（４０）またはチャンバーのモジュール、少なくとも１つのマイクロ波発生器（３２）、各前記発生器に接続されたアンテナ（３４）および反射表面（３６）からなる。 有機物質をチャンバー（４０）の中に供給する手段（４８）、チャンバーから気体の生成物を取り出す手段（１８）およびチャンバーから固体の残留物を取り出す手段（２２）が提供される。 | ||||||
| 39 | JPH05508666A - | JP50512591 | 1991-02-25 | JPH05508666A | 1993-12-02 | |
| 40 | Method for treating highly environmentally polluting residue | JP20902692 | 1992-08-05 | JPH05192698A | 1993-08-03 | MISHIERU SHIYUNAIDAA; JIERAARU MATSUSON; ERIKU BESHIEERU |
| PURPOSE: To provide a method for treating the residue which brings about a high degree of environmental pollution via water, for example, the residue generated from dry process filtration or wet process filtration. CONSTITUTION: This method consists of a stage for mixing the residue with the product contg. iron oxide, a stage for placing the mixture into a crucible 5, a stage for protecting the crucible 5 with insulative fibers, a stage for placing the crucible 5 protected with the insulative fibers 6 in a microwave oven 1 and a stage for forming the dry fused matter of the mixture and exposing the mixture to microwaves at 1,000 to 1,300°C for 2 to 15 minutes in order to obtain a solid material. COPYRIGHT: (C)1993,JPO | ||||||
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