序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
61 用于对悬浮液进行充气的方法和装置 CN01112368.0 2001-02-02 CN1222658C 2005-10-12 B·舒尔青格; H·加布尔
发明涉及一种用于对悬浮液进行充气的方法,尤其是用于在脱墨工艺中对纸浆悬浮液进行浮选的方法,所述包含有杂质颗粒的纸浆悬浮液与气体尤其是空气一起被喷射进一个容器中。该方法的主要特征在于气体尤其是空气在至少两个连续的地方(2,4,12)在喷射机的作用下被吸入并与悬浮液混合。本发明还涉及一种用于实施该方法的装置。
62 控制一种浮选槽的工作的方法 CN200410008080.1 2004-03-10 CN1535762A 2004-10-13 H·加布尔; A·戈尔顿一许格尔斯; E·赫尔特尔
发明涉及一种控制浮选槽工作的方法,其中测量和控制该浮选槽中液体的高度位置泡沫的高度位置。本发明的方法的特征在于,测量离开该浮选槽的接受物的至少一个品质特性,根据这个品质特性确定该液体高度位置和/或者泡沫高度位置的设定值。特别是在脱墨浮选中,本发明的方法特别适于纸浆悬浮液。
63 用于充气悬浮液的过程和装置 CN200410003553.9 2004-01-29 CN1517488A 2004-08-04 H·加布尔
发明涉及用于充气悬浮液的过程,特别是通过一个或者多个阶段和/或单元(P1、P2、P3、P4、S1、S2)来将它们在例如浆料悬浮液的脱墨中浮选,其中,每个阶段/单元(P1、P2、P3、P4、S1、S2)具有其自己独立的液体回路(6)。为了改进脱灰,本发明规定引入洗涤过程(12、12’、16、18)。此外,本发明涉及用于实现该过程的装置。
64 一种浮选分离罐 CN96191495.5 1996-01-18 CN1108277C 2003-05-14 汉斯·埃里克松; 肯特·伊萨克松
发明涉及一种用于分配和散化高压充满空气的的装置,它最好用于水净化设备的浮选分离罐(1)之中,它位于通入要在浮选分离罐(1)受处理的水的入口(2)附近。该分配和散化装置包括一个设置在分配管(22)或其供给管道(24)之中的预散化装置(27,28),它包括一个同轴地安装在所述管道中的多孔管。饱含空气的水通过这些孔或节流孔(26)来获得第一次压下降及由此产生的散化。水流入分配管(22),再由此流过分配管(22)的壁上的一个或多个开口(23),由此处压入浮选分离罐(1),而形成进一步的压力下降和水的散化。
65 通过浮选法从悬浮液中分离杂质的方法和装置 CN02143166.3 2002-09-16 CN1408480A 2003-04-09 B·舍尔青格; H·加布尔
用浮选法使杂质与悬浮液分开的方法包括向液体充气直到饱和,随后将气体饱和的液体膨胀并形成气泡。为了在悬浮液中为创造最佳的气泡大小和数量提供良好条件并使本方法更有效,气体饱和的液体单独地并在含气泡的液体加到有杂质的悬浮液中之前进行膨胀。用浮选法使杂质与悬浮液分开的装置至少包括向液体充气直到饱和的设备,气体饱和的液体进行膨胀并产生气泡的设备,和将有气泡的液体加到悬浮液中并送到浮选槽的设备,其特征在于:液体膨胀设备(4)与将有气泡液体加到悬浮液的设备分开布置,且与浮选槽(6)分开布置。
66 向液体充气的方法和装置 CN02143165.5 2002-09-16 CN1408479A 2003-04-09 B·舍尔青格; H·加布尔
向液体充气的方法,特别是应用浮选法使杂质与悬浮液分离的方法,该方法包括液体通过喷管喷射到气体容积中。为了在质量传递方面有大的改进和更有效地获得最大可能的饱和度,部分气体容积通过喷射液体所产生的真空吸入,与液体一起携带并与此同时与液体混合。实现该方法的装置包括一容器(2),它盛装液体且在液体上方是气体容积,在压力容器上部有气体的压力管接头并有喷管(11),液体通过喷管喷出。为了达到上述效果,喷管(11)与安装在压力容器(2)内的喷射器(10)的头部连接,喷射器伸到压力容器(2)盛装液体的下部,喷射器头部伸到压力容器(2)盛装气体容积的顶部。
67 从液体中分离不溶性颗粒的方法和设备 CN96192773.9 1996-03-20 CN1089017C 2002-08-14 R·杜福尔
一种用于处理含有不溶性悬浮颗粒的液体以从液体中分离这些颗粒的净化器。它包括一澄清槽、一开口于澄清槽底部的进料管道以及一将压空气喷射到加入进料管道的至少部分液体中将液体用所说的气体饱和从而当饱和液体在澄清槽中降压时产生气泡的喷射器。
68 从液体中分离不溶性颗粒的方法和设备 CN96192773.9 1996-03-20 CN1179113A 1998-04-15 R·杜福尔
一种用于处理含有不溶性悬浮颗粒的液体以从液体中分离这些颗粒的净化器。它包括一澄清槽、一开口于澄清槽底部的进料管道以及一将压空气喷射到加入进料管道的至少部分液体中将液体用所说的气体饱和从而当饱和液体在澄清槽中降压时产生气泡的喷射器。由此产生的气泡粘附在液体中的悬浮颗粒上并使颗粒上升,在澄清槽顶部形成一层飘浮污泥。在澄清槽顶部设有刮除器将所形成的污泥层刮除。在进料管道上方,多板在澄清槽中伸展一定度。这些板形成一组向上倾斜通道,各通道具有开口顶端,加入澄清槽中的液体可通过开口顶端进入各通道。在各通道下端安装有液体出口,在澄清槽中经处理后的液体在此收集并排出澄清槽。由于其形状和结构,本净化器的占地面积仅为具有同样生产能力的任何已知净化器的50%或更少。本净化器的结构也使得对同样数量的注入空气能够维持多得多的所要求尺寸的微小气泡以增加颗粒与空气泡之间接触的可能性。
69 가스 부유 탱크 KR1020167007546 2014-08-08 KR1020160050044A 2016-05-10 커크,토드윌리엄; 휘트니,다니엘클리포드; 이,더글라스워커
인접하는챔버들내에서회전흐름이일어나게하는그러한일련의인접하는챔버들을포함하는가스부유탱크가제공된다. 각각의챔버는스키밍위어에의해스킴오일통으로부터분리된다. 각각의챔버는하나걸러인접챔버들사이에유체소통장치를포함하며, 여기서유체소통장치는인접챔버들사이의분할벽에서소통포트의형태로인접챔버들간의유체소통이가능하게하고, 다공성판과결합된챔버유출부가포함되며, 유출부는마지막챔버와유체소통을행하도록위치하고있다.
70 나노버블을 이용한 토양세척 및 화학적 산화에 의한 유류/중금속 복합오염토양의 융복합정화처리방법 KR1020140036148 2014-03-27 KR101443724B1 2014-09-26 최재영; 이홍균; 지은도; 김치경
The present invention relates to a fusion method for treating and purifying soil with complex oil/heavy metal contamination through soil washing by using nano-bubbles and through chemical oxidation, and more particularly, provides a method for simultaneously treating soil with complex contamination of petroleum contaminant, such as BTEX, diesel, gasoline, etc., and heavy metals. The method according to the present invention includes a flotation step using nano-bubbles or micro-bubbles, a chemical oxidation step for oxidating petroleum contaminants, and a heavy metal washing step using organic acid and can treat the soil with complex contamination simultaneously and more effectively.
71 수평 탱크들을 가스 부상 분리기들로 전환시키기 위한 방법 및 장치 KR1020107007034 2007-09-04 KR101217363B1 2012-12-31 이더글라스더블유; 오웬스니콜라스
부유식원유생산저장하역설비선들(FPSO vessels))위의석유저장고용으로사용되는것들같은수평탱크에사용가능한가스부상분리기(gas flotation separator)는상기탱크를연속하여작용하는복수개의챔버들로나누는것을포함한다. 각각의챔버로들어가기전에상기오염된수성상(aqueous phase)은상기비혼화성상오염물의응집과부상을돕기위해가스버블들을포함하는흐름(stream)과혼합된다. 상기가스버블재순환흐름은상기탱크외부에서의공정에서조절된비율의압축가스를깨끗한생산수의흐름으로주입하거나, 상기탱크로의내부적기상의유입에의해생성될수 있다. 상기혼합물은첫번째챔버로흘러들어가서굽어진유입수위어에부딪힌다. 상기비혼화성상과상기기상의일부는상기챔버의상부로올라오고, 한편, 비혼화성혼합물의나머지는수성상으로상기챔버의바닥을향해아래로흘러간다. 상기수성상은상기각 연속된챔버를분할시키는배플의벽 안으로형성된복수개의평행한라이저도관으로들어감으로써 180°위쪽으로돌게된다. 상기비혼화성오염물의응집및 부상을더욱돕기위해두 번째가스버블흐름은각각의평행한덕트안으로주입된다. 상기수성상은그것이두 번째굽은위어에부딪히는두 번째챔버의상부에서재혼합된다. 이러한공정은각각의연속된챔버내에서마지막챔버에이르기까지반복되며, 마지막챔버에서는정수가액체펌프를거쳐상기챔버의밖으로나간다. 거기서의다양한물 제거비율은마지막챔버내의수위를조절한다. 상기응집되어부상한석유오염물은, 1) 상기챔버내에서수위를올림으로써범람(over-flow) 위어안쪽으로주기적으로걷어내는것 또는, 2) 부상하는석유층을상기물 표면으로부터들어올리거나, 멀리옮겨서수집장치(collector system)로그것을전달하는연속적으로회전하는패달혹은브러쉬같은것에의해제거될수 있다.
72 부유 분리 장치 및 방법 및 그 이용 제품의 제조 방법 KR1020127004243 2010-07-15 KR1020120037491A 2012-04-19 마쓰후지야스노리; 다카스고지; 다쓰미기요타카
By storing a liquid to be treated in a treatment tank main body 10 having a bottom portion 10g that narrows downward, with particles of materials to be treated dispersed therein, taking out the liquid to be treated from a position lower than the liquid level of the treatment tank main body 10, and returning the liquid to the bottom portion 10g of the treatment tank main body 10, thereby circulating the liquid to be treated while forming a vortex flow within the treatment tank main body 10, and at the same time supplying air bubbles from the lower part of the treatment main unit 10, a first component contained in froths is separated from a second component, which is less susceptible to floatation, contained in the liquid to be treated.
73 부양식 수처리 장치 및 방법 KR1020097023995 2008-05-16 KR1020100016650A 2010-02-12 두모린,로랑스; 패스토렐리,델리아; 바다드,미쉘
The invention relates to a flotation water treatment plant comprising at least: an inlet zone (31) for the water to be treated, which is coagulated and flocculated beforehand; a mixing zone (32), for mixing pressurized and then depressurized water with said water to be treated; a flotation zone (35) separated from said mixing zone by a wall; a clarified-water take-up zone (36) provided in the lower part of said flotation zone (35). According to the technique shown here, said mixing zone accommodates (32) at least one spray nozzle (40, 91, 92) for spraying said pressurized water, said spray nozzle (40, 91, 92) lying close to a panel (33), at least part of which has perforations (331), said panel separating said inlet zone (31) from said mixing zone (32).
74 액체로부터 비용해 입자를 분리하기 위한 방법 및 장치 KR1019970706033 1996-03-20 KR100404716B1 2004-02-18 듀포르레뉴
Disclosed is a clarifier for use in treating a liquid containing non-soluble particles in suspension in order to separate these particles from the liquid. It comprises a tank, a liquid supply duct opening into the bottom portion of the tank and an injector for injecting a gas under pressure into at least part of liquid supplied to the supply duct in order to saturate this liquid with said gas and thus to generate gas bubbles as the saturated liquid is subject to depressurization within the tank. The gas bubbles that are so-generated adhere to the particles in suspension in the liquid and lift them up to form a floating layer of sludge in the top portion of the tank. A scraper is provided in the top portion of the tank for skimming off the layer of sludge while it is formed. A plurality of plates extend at an angle within the tank above the supply duct. These plates define a set of upwardly inclined channels each having an upper end that is opened and through which the liquid fed into the tank may enter the channel. A liquid outlet mounted within the lower end of each channel to collect and remove from the tank the liquid that has been treated within the same. Thanks to its shape and structure, this clarifier occupies a surface area on the ground that is 50% or less smaller than any known clarifier of the same capacity. Its structure also permits to maintain much more microbubbles of requested size for a same amount of injected air in order to increase the probability of contact between the particles and the air bubbles.
75 又は排水を処理するためのシステム及び方法 JP2016543741 2014-12-24 JP2017503649A 2017-02-02 パトリック アンダーソン,マイケル
本発明は、又は排水を処理するための、処理システム、装置、組立体、設備、サイクル、及び/又は方法、特に、一連の2つ以上の溶解空気浮上チャンバを通して高い流量(約200L/分を超える値を含む)で受取られる水又は排水を処理するための、システム、装置、組立体、設備、サイクル、及び/又は方法に関する。【選択図】図3
76 随伴の処理方法及び処理装置 JP2012043527 2012-02-29 JP5826068B2 2015-12-02 川村 和茂; 粟井 英司; 武田 大
77 系からのカーボンナノチューブの除去 JP2015507053 2013-04-10 JP2015519280A 2015-07-09 ロバート ディー デントン; ジュニア ラッセル ジェイ コヴィール; ダラス ビー ノイエス; テリー エイ リング
本明細書では、ストリームからカーボンナノチューブを除去するための方法およびシステムを提供する。本システムは、水ストリーム内のカーボンナノチューブから炭素酸化物を形成するように構成された精製容器を含む。本方法は、水ストリームを精製容器中へ流すステップと、その精製容器中に化学物質を注入するステップとを含む。このカーボンナノチューブを、精製容器内での前記化学物質とカーボンナノチューブの相互作用によって、水ストリームから分離する。
78 Method and apparatus for treating produced water JP2012043527 2012-02-29 JP2013180213A 2013-09-12 KAWAMURA KAZUSHIGE; AWAI EIJI; TAKEDA MASARU
PROBLEM TO BE SOLVED: To provide a method for simply and easily treating a large amount of taken-out produced water while suppressing the increase of cost by the use of a chemical or the generation of waste accompanying it.SOLUTION: A method for treating produced water taken out according to the production of crude oil or natural gas, and containing at least an oil content as a treatment target subject includes: an oil content separation process 1 performed so as to remove free oil or the like from the produced water as the need arises; a coagulation process 2 of coagulating emulsified oil by introducing micro-nano bubbles consisting of ozone-containing gas into the produced water preferably such that a gas-liquid contact time of 2-60 minutes can be obtained; and a floatation separation process 3 of floating and separating the coagulated emulsified oil as scum to obtain purified water.
79 Water treatment by flotation equipment and water treatment process JP2010507933 2008-05-16 JP5259698B2 2013-08-07 デュムラン,ロランス; パストレリ,デリア; バダール,ミシェル
The invention relates to a flotation water treatment plant comprising at least: an inlet zone (31) for the water to be treated, which is coagulated and flocculated beforehand; a mixing zone (32), for mixing pressurized and then depressurized water with said water to be treated; a flotation zone (35) separated from said mixing zone by a wall; a clarified-water take-up zone (36) provided in the lower part of said flotation zone (35). According to the technique shown here, said mixing zone accommodates (32) at least one spray nozzle (40, 91, 92) for spraying said pressurized water, said spray nozzle (40, 91, 92) lying close to a panel (33), at least part of which has perforations (331), said panel separating said inlet zone (31) from said mixing zone (32).
80 Flotation device comprising a perforated plate JP2010504486 2008-04-02 JP5146939B2 2013-02-20 トルブニス,ゲオルゲ; メンケ,ルーカス
A flotation apparatus (10) for the separation of solid particles from a suspension with formation of a fraction lacking in solid particles and a fraction rich in solid particles comprises a tank with an inlet (14) for the suspension, with an outlet (16) for the fraction lacking in solid particles, with an outlet (18) for the fraction rich in solid particles, and with at least one block of slats (20) composed of multiple overlapping slats (22), wherein the at least one block of slats (20) has a rear side oriented toward the tank wall and a front side arranged on the opposite side of the block of slats (20). On the rear side of the at least one block of slats, a plate (26) is arranged which extends over at least a part of the rear side of the block of slats, wherein the plate has a plurality of openings which facilitate the penetration of liquid through the plate. The sum of the areas of the individual openings (38) in the upper region, relative to the vertical axis, of the plate, per square centimeter of the plate, is greater than the sum of the areas of the individual openings in the lower region of the plate, per square centimeter of the plate.
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