| 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 | Process for treating waste water | US37990773 | 1973-07-16 | US3883426A | 1975-05-13 | LEWANDOWSKI SYLVETTE ODETTE RO; LEWANDOWSKI RAYMOND |
| Waste water is purified by means of the flotation process by using aluminum having on at least one surface thereof an amalgam of aluminum and mercury. The hydrogen gas and aluminum produced during the reaction between the waste water and the aluminum amalgam is used to float the impurities to the surface of the waste water being treated, the impurities then being removed and the purified water recovered. Flotation apparatus for carrying out the process is also described.
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| 22 | Electroflotation apparatus | US34419573 | 1973-03-23 | US3853736A | 1974-12-10 | HARNDEN W; MORRILL E |
| A tank, having a height several times its effective diameter, has a plurality of horizontal electrodes disposed throughout its entire height. Conduits and controls are provided for downflow of liquid to be purified in a non-turbulent manner. Electrolysis of the liquid causes gas bubbles to flow upwardly. This apparatus creates a non-turbulent flow of liquid directly counter to the flow of gas bubbles for a substantial vertical distance. In one embodiment the tank is a cylinder, while in another it has downwardly converging sides. A third embodiment shows two compartments arranged for sequential flow of liquid therethrough.
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| 23 | electrode | JP2010533587 | 2008-11-14 | JP2011503359A | 2011-01-27 | エドヴィンソン−アルバース，ロルフ; ヘデンステッド，クリストファー; ロスバル，マグナス |
| 本発明は、ａ）Ｍ
（ｎ＋１） ＡＸ
ｎを含む電極基材（ここで、Ｍは、元素周期表のＩＩＩＢ、ＩＶＢ、ＶＢ、ＶＩＢもしくはＶＩＩＩ族の金属またはこれらの組合せであり、Ａは、元素周期表のＩＩＩＡ、ＩＶＡ、ＶＡもしくはＶＩＡ族の元素またはこれらの組合せであり、Ｘは、炭素、窒素またはこれらの組合せであり、ｎは、１、２、または３である）；およびｂ）該電極基材に析出した電極触媒コーティングを備える電極に関し、該コーティングは、ｂ． １）Ｂ
ｙ Ｃ
（１−ｙ） Ｏ
ｚ１ Ｓ
ｚ２を含む金属酸化物および／または金属硫化物（式中、Ｂは、ルテニウム、白金、ロジウム、パラジウム、イリジウム、およびコバルトの少なくとも１種であり、Ｃは、少なくとも１種のバルブ金属であり、ｙは、０．４〜０．９であり、０≦ｚ１、ｚ２≦２、およびｚ１＋ｚ２＝２である）；ｂ． ２）Ｂ
ｆ Ｃ
ｇ Ｄ
ｈ Ｅ
ｉを含む金属酸化物（式中、Ｂは、ルテニウム、白金、ロジウム、パラジウム、およびコバルトの少なくとも１種であり、Ｃは、少なくとも１種のバルブ金属であり、Ｄはイリジウムであり、ＥはＭｏおよび／またはＷであり、ｆは０〜０．２５または０．３５〜１であり、ｇは０〜１であり、ｈは０〜１であり、ｉは０〜１であり、ｆ＋ｇ＋ｈ＋ｉ＝１である）；ｂ． ３）少なくとも１種の貴金属；ｂ． ４）鉄−モリブデン、鉄−タングステン、鉄−ニッケル、ルテニウム−モリブデン、ルテニウム−タングステンまたはこれらの混合物を含む任意の合金または混合物；ｂ． ５）少なくとも１種のナノ結晶材料の少なくとも１つから選択される。 本発明はまた、前記電極の製造方法、およびその使用にも関する。 本発明はまた、アルカリ金属塩素酸塩の製造方法、およびその製造のための電解槽にも関する。
【選択図】なし |
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| 24 | JPS5850559B2 - | JP17864380 | 1980-12-17 | JPS5850559B2 | 1983-11-11 | AREKUSANDORU ARUKUSANDOROITSUCHI AKUSENKO; MIRON MIGURANOITSUCHI NAZARIAN; URADEIMIIRU AREKUSANDOROITSUCHI KORUYADA; ARUKADEI ROMANOITSUCHI MATAEFU; RYUUDOMIRA FUEDOROFUNA SHAMUSHA |
| The apparatus according to the invention consists of a settling chamber (1) with outflow ports (6 and 7) for clear water and sludge, respectively, and of an electrocoagulation chamber (2) arranged in the settling chamber (1) and connected thereto. The electrocoagulation chamber (2) contains an inflow port (4) for effluent, an inflow port (5) for electrolyte and a number of soluble electrodes (3). These are situated below the inflow port (4) for effluent. Arranged in the wall of the electrocoagulation chamber (2), distributed over the circumference and below the water level of the settling chamber (1) there are orifices (10) into which nozzles (12) of injectors (11) debouch which feed part of the foam from the electrocoagulation chamber (2) to the settling chamber (1). The invention is used for the electrochemical cleaning of industrial effluents. <IMAGE> | ||||||
| 25 | Electrochemical purifier for polluted liquid | JP17864380 | 1980-12-17 | JPS57102283A | 1982-06-25 | AREKUSANDORU ARUKUSANDOROBUITS; MIRON MIGURANOBUITSUCHI NAZARI; URADEIMIIRU AREKUSANDOROBUITSU; ARUKADEI ROMANOBUITSUCHI MATAE; RIYUUDOMIRA FUEDOROFUNA SHIYAM |
| The apparatus according to the invention consists of a settling chamber (1) with outflow ports (6 and 7) for clear water and sludge, respectively, and of an electrocoagulation chamber (2) arranged in the settling chamber (1) and connected thereto. The electrocoagulation chamber (2) contains an inflow port (4) for effluent, an inflow port (5) for electrolyte and a number of soluble electrodes (3). These are situated below the inflow port (4) for effluent. Arranged in the wall of the electrocoagulation chamber (2), distributed over the circumference and below the water level of the settling chamber (1) there are orifices (10) into which nozzles (12) of injectors (11) debouch which feed part of the foam from the electrocoagulation chamber (2) to the settling chamber (1). The invention is used for the electrochemical cleaning of industrial effluents. <IMAGE> | ||||||
| 26 | Floating method which purify waste water for industry or of selffgoverning community | JP11851780 | 1980-08-29 | JPS5633080A | 1981-04-03 | ERIASU YURUKE |
| In a flotation method for purification of industrial or municipal waste water, in which the waste water comes in contact with electrodes having an electrical potential capable of electrolytically decomposing a portion of the waste water, thereby creating an ascending stream of gas bubbles, the waste water is mixed before or during the electrolytic decomposition with wettable particles of polymer material which are practically insoluble in water and have an absolute density of 1.3 g/cm3 at the most. Polymeric materials, especially polyalkane fibrids, are suitable for use as particles. This process makes it possible to purify oil-containing waste water by electroflotation without forming an oil film on the electrodes. | ||||||
| 27 | JPS5112281B2 - | JP12238772 | 1972-12-06 | JPS5112281B2 | 1976-04-17 | |
| 1408878 Electrolytic flotation apparatus SIMON HARTLEY Ltd 22 Nov 1972 [10 Dec 1971] 57402/71 Heading C1C [Also in Divisions C6-C7] Flotation apparatus used in the treatment of aqueous suspension such as activated sludge comprises a tank in which is located an electrcde assembly comprising a generally plane cathode and a superimposed generally planar and parallel anode structure, means for introducing liquid to be treated evenly along or adjacent to one boundary edge of the electrode assembly to flow across the assembly to an opposed boundary edge, the dimension across the electrode assembly between the boundary edges in the direction of flow of the liquid to be treated being from 0À5-1À5 metres. As shown the cell comprises side walls 11, 12; electrolyte inlet chambers 23, 24 extending the length of the walls such that electrolyte flows over the serated top edge of the walls to flow down between each wall and a respective baffle 25; a V-shaped cell base each side of which has a cathode 18 adjacent thereto and a grid anode 20 parallel to and spaced apart from the cathode; electrolyte flowing from beneath the baffles 25 between anodes 20 and cathodes 18 to be withdrawn via nozzles 26; sediment which collects being removed via channel 17 in the base of the cell and flocculent material which is raised to the surface by gas bubbles given off by the electrolysis being removed by a system of scraper blades attached to an endless belt (40) (Fig. 1, not shown). | ||||||
| 28 | JPS495703B1 - | JP4850067 | 1967-07-29 | JPS495703B1 | 1974-02-08 | |
| 29 | JPS4866003A - | JP12238772 | 1972-12-06 | JPS4866003A | 1973-09-11 | |
| 1408878 Electrolytic flotation apparatus SIMON HARTLEY Ltd 22 Nov 1972 [10 Dec 1971] 57402/71 Heading C1C [Also in Divisions C6-C7] Flotation apparatus used in the treatment of aqueous suspension such as activated sludge comprises a tank in which is located an electrcde assembly comprising a generally plane cathode and a superimposed generally planar and parallel anode structure, means for introducing liquid to be treated evenly along or adjacent to one boundary edge of the electrode assembly to flow across the assembly to an opposed boundary edge, the dimension across the electrode assembly between the boundary edges in the direction of flow of the liquid to be treated being from 0À5-1À5 metres. As shown the cell comprises side walls 11, 12; electrolyte inlet chambers 23, 24 extending the length of the walls such that electrolyte flows over the serated top edge of the walls to flow down between each wall and a respective baffle 25; a V-shaped cell base each side of which has a cathode 18 adjacent thereto and a grid anode 20 parallel to and spaced apart from the cathode; electrolyte flowing from beneath the baffles 25 between anodes 20 and cathodes 18 to be withdrawn via nozzles 26; sediment which collects being removed via channel 17 in the base of the cell and flocculent material which is raised to the surface by gas bubbles given off by the electrolysis being removed by a system of scraper blades attached to an endless belt (40) (Fig. 1, not shown). | ||||||
| 30 | ELECTROFLOTATION APPARATUS HAVING AN OUTLET PIPE WITH A LOW TURBULENCE ORIFICE | EP16778054.3 | 2016-10-07 | EP3359493A1 | 2018-08-15 | GIAEVER, Stig; HOLM, Daniel |
| An electroflotation apparatus for removing impurities from waste water is disclosed. The apparatus comprises an electrolytic cell for treating the waste water and generating a flock containing the impurities as well as an outlet pipe having a linear central axis located co-axially with the electrolytic cell for passing the water and flock from the electrolytic cell to a separation area. The outlet pipe comprises a first end connected to the electrolytic cell and having a first diameter, as well as a second end through which the treated water and flock exit the outlet pipe, the second end having a second diameter. A length extends between the first diameter and the second diameter. The ratio of the second diameter to the first diameter is between 1.5:1 and 6:1. The ratio of the length to the first diameter is between 7:1 and 45:1. The outlet pipe reduces the turbulence of the treated water from the electrolytic cell before the treated water is passed to the separation area such that aggregation of the flock in the separation area is increased. | ||||||
| 31 | METHOD AND APPARATUS FOR THE PURIFICATION OF HYDROGEN SULFIDE -CONTAINING AQUEOUS SOLUTIONS | EP10808020.1 | 2010-08-13 | EP2531451B1 | 2015-07-15 | Suominen, Hannu |
| 32 | METHOD AND APPARATUS FOR THE PURIFICATION OF WASTE WATER | EP10811325.9 | 2010-08-17 | EP2470478A1 | 2012-07-04 | Suominen, Hannu |
| A method and apparatus for the purification of wastewater. The hydrostatic pressure of wastewater present in a tank (14) is used for passing wastewater across an electrolytic cell submerged in the tank. The cell element equipped with an iron and/or aluminum electrode is used for generating iron and/or aluminum hydroxide working as a molecular sieve. The hydrogen released in electrolysis is used for raising the molecular sieve and impurities trapped therein up into a water and flock separation tower (7), in which the same, upon rising, accumulate for a flock (13) in an upper end of the separation tower. Purified water is removed from the separation tower (7) from below the evolving flock (13) and from above the level of water in the tank (14). | ||||||
| 33 | ELECTRODE | EP08850172.1 | 2008-11-14 | EP2217744A2 | 2010-08-18 | ROSVALL, Magnus; EDVINSSON-ALBERS, Rolf; HEDENSTEDT, Kristoffer |
| An electrode substrate comprising M(n+1)AXn, where M is a metal of group IIIB, IVB,VB,VIB or VIII of the periodic table of elements or a combination thereof, A is an element of group IIIA, IVA, VA or VIA of the periodic table of elements or a combination thereof, X is carbon, nitrogen or a combination thereof, where n is 1, 2, or 3; and b) an electrocatalytic coating deposited on said electrode substrate, said coating being selected from at least one of b.1 ) a metal oxide and/or metal sulfide comprising ByC(1-y)Oz1Sz2, wherein B is at least one of ruthenium, platinum, rhodium, palladium, iridium, and cobalt, C is at least one valve metal, y is 0.4-0.9, 0 <= z1, z2 <= 2 and z1+z2=2; b.2) a metal oxide comprising BfCgDhEi, wherein B is at least one of ruthenium, platinum, rhodium, palladium, and cobalt, C is at least one valve metal, D is iridium, E is Mo and/or W, wherein f is 0-0.25 or 0.35-1, g is 0-1, h is 0-1, i is 0-1, wherein f+g+h+i=1; b.3) at least one noble metal; b.4) any alloy or mixture comprising iron-molybdenum, iron-tungsten, iron-nickel, ruthenium-molybdenum, ruthenium-tungsten or mixtures thereof; b.5) at least one nanocrystalline material. The electrode is used in an electrolytic cell for the production of alkali metal chlorate. | ||||||
| 34 | VERFAHREN ZUR ENTGIFTUNG VON HAFENSCHLICK | EP99953604.8 | 1999-08-26 | EP1216205A1 | 2002-06-26 | JÜSSEN, Armin; JÜSSEN, Marc |
| The invention relates to a method for detoxicating harbour silt, especially harbour silt that is charged with organotin compounds. The basic procedure step is an electroflotation. | ||||||
| 35 | FLOCK SEPARATING APPARATUS | EP95900780.8 | 1994-11-18 | EP0794926B1 | 2000-03-15 | SUOMINEN, Hannu, L. |
| 36 | Water treatment by means of electroflotation and electrocoagulation | EP96301505.2 | 1996-03-05 | EP0794157A1 | 1997-09-10 | Lee, Ming Shing |
A method for continuously treating a water body, comprising a step of using a substantially sealed processing tank, at a top and a bottom portion of which a water outlet and a water inlet are arranged respectively, and in an interior space of which three or more conductive plates substantially in parallel relation with the tank bottom and substantially in parallel relation with one another for upwardly forming a substantially closed S-shaped one-way flow path in said processing tank, wherein said conductive plates are made of a conductive material having a resistivity ranged from 1.59 µΩ·cm to 1300 µΩ·cm and at least two of said conductive plates are respectively electrically connected to a positive and a negative power source to serve as an anode and a cathode, wherein said water to be treated is introduced into said processing tank from said water inlet, flows upwardly through said S-shaped one-way flow path, and then is discharged out of said processing tank form said water outlet, and wherein a voltage is applied to said cathode and said anode to generate an electric field having an intensity ranged from 0.5 mV/cm to 1000 V/cm during the flow of said water body in said flow path, thereby polarizing and coagulating impurities in said water body to removing said coagulating impurities. |
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| 37 | Umpolbare Elektrode | EP84112538.8 | 1984-10-17 | EP0140287A2 | 1985-05-08 | Fabian, Peter; Kotowski, Stephan, Dr.; Busse, Bernd, Dr. |
Umpolbare Elektrode für elektrochemische Verfahren, insbesondere wenn der Elektrolyt auch kalzium- und magnesiumhaltig ist. Durch Mehrschichtaufbau aus einem Träger (1) aus Ventilmetall, einer darauf aufgebrachten leitfähigen keramischen Schicht (2) mit einer elektrokatalytisch aktiven Schicht (3) als Deckschicht wird erreicht, daß einerseits der Träger (1) geschützt ist, andererseits die elektrokatalytisch aktive Schicht (3) auch im kathodischen Betrieb stabil ist, wobei der neuen Elektrode der dauernde Ladungswechsel nicht schadet. Dabei können sich gleich große Anoden- und Kathodenflächen parallel oder nahezu parallel gegenüberliegen. |
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| 38 | Method and Apparatus for Separating Impurities from a Liquid Stream by Electrically Generated Gas Bubbles | US12113443 | 2008-05-01 | US20080272056A1 | 2008-11-06 | Bijan Kazem |
| A method and apparatus for separating impurities from a liquid stream includes a feed tank for containing an untreated liquid, a mixer for generating and mixing bubbles throughout the wastewater, and a settling tank for allowing the wastewater to settle for removal of impurities through dissolved gas floatation. The mixer includes a housing and a rotor rotatably mounted within the housing. The rotor is electrically isolated and the peripheral wall of the housing is electrically isolated and the rotor preferably has bores formed in its peripheral surface to produce cavitation to aid in mixing of fluid within the mixer. A power supply is coupled to establish a relatively positive electrical charge on the rotor and a relatively negative electrical charge on the wall of the housing. The charge causes electrolysis to occur within the fluid, which forms small low surface tension gas bubbles on the rotor and housing wall. These bubbles detach and are mixed with the fluid, where they can attach to and separate impurities through dissolved gas floatation. | ||||||
| 39 | System and method for removing deep sub-micron particles from water | US10962616 | 2004-10-13 | US20050045534A1 | 2005-03-03 | KonTsu Kin; Hong-Shiang Tang |
| The present invention discloses a process and an apparatus for removing deep sub-micron particles from water. The invented process includes adjusting pH value and conductivity, adding an oxidation agent, performing an electro coagulation reaction/an electro-oxidation reaction, and performing a flocculation sedimentation, etc. The invented apparatus includes a front adjustment tank for adjusting the properties of waste water, wherein the adjustment includes a pH adjustment, an electrolyte adjustment, or an oxidant addition, etc.; an electrocoagulation reaction tank receiving water from the front adjustment tank and having pairs of separated electrodes, one of the electrodes being made of iron; a rear adjustment tank for adjusting pH value of the effluent of the electrocoagulation reaction tank; and a sedimentation reservoir for providing the resulting pH-adjusted, sedimentary floccule-containing water from the rear adjustment tank with a sufficient residence time in said sedimentation reservoir, so that floccules and sedimentation are formed therein. | ||||||
| 40 | System and method for removing deep sub-micron particles from water | US10310875 | 2002-12-06 | US20030121864A1 | 2003-07-03 | Kon-Tsu Kin; Hong-Shiang Tang |
| The present invention discloses a process and an apparatus for removing deep sub-micron particles from water. The invented process includes adjusting pH value and conductivity, adding an oxidation agent, performing an electro coagulation reaction/an electro-oxidation reaction, and performing a flocculation sedimentation, etc. The invented apparatus includes a front adjustment tank for adjusting the properties of waste water, wherein the adjustment includes a pH adjustment, an electrolyte adjustment, or an oxidant addition, etc.; an electrocoagulation reaction tank receiving water from the front adjustment tank and having pairs of separated electrodes, one of the electrodes being made of iron; a rear adjustment tank for adjusting pH value of the effluent of the electrocoagulation reaction tank; and a sedimentation reservoir for providing the resulting pH-adjusted, sedimentary floccule-containing water from the rear adjustment tank with a sufficient residence time in said sedimentation reservoir, so that floccules and sedimentation are formed therein. | ||||||
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