序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
1 一种全截面充气式浮选机 CN201110155809.8 2011-06-10 CN102211061A 2011-10-12 张云龙
发明涉及一种全截面充气式浮选机,其包括浮选槽和安装在浮选槽顶部的泡沫溢出机构,浮选槽槽体上设置有矿浆进口和矿浆出口,在浮选槽槽体底部安装有单向安装板,且单向阀安装板形状与浮选槽槽体底部截面形状相匹配,从而将浮选槽槽体分割形成承浆室和位于承浆室下方的气室,承浆室底部一侧设置有放矿口,气室一侧设置有进气口,单向阀安装板上均匀分布有多个单向阀。本发明全截面充气式浮选机结构简单,维护方便,提高选矿回收率,降低能耗,充分利用气体,减少药剂用量,易损件寿命延长,缩短浮选工艺阶段并降低设备和基建投资。
2 从含无机固体的颗粒中分离质组分的方法及装置 CN86103632 1986-05-30 CN86103632A 1986-12-17 C·爱得华·卡比斯; 理查德·D·科莱曼; 瑟格·科罗蒂奥; 威廉姆·L·萨耶尔
、附聚油与加以搅拌和充气,使煤中质组分与油和捕集在附聚物中的空气形成附聚物的方法来从含无机固体的颗粒煤中分离碳质组分。捕集在附聚物中的空气使附聚物有浮,因此附聚物聚集在水面而容易分离,无机残留固体却聚集在水底。含煤无机固体可以与水成浆的形式存在,也可包含预先形成的附聚物。借助搅拌使之分解而形成水浆。后一方法是为了分离那些初始附聚时难以分离的无机固体。搅拌作用可借助搅拌器、搅拌叶轮来完成。
3 用于从进料浆料中分离出低密度颗粒的方法及装置 CN201180034985.4 2011-06-02 CN103002987B 2015-04-22 凯文·帕特里克·高尔文
在用于从进料浆料中分离低密度颗粒的方法及装置中,泡状混合物在下导管(14)内形成并流至腔室(1)中的中间区域(12)。在该中间区域下方由多个平行倾斜板(6)形成了一个倒置的回流分级器,用于低密度颗粒与更高密度颗粒的有效分离,这些低密度颗粒上升而在该腔室的顶部形成密集泡沫(16),并且更高密度颗粒下落至出口(29)。
4 从含无机固体的颗粒中分离质组分的方法及装置 CN86103632 1986-05-30 CN1006900B 1990-02-21 C·爱得华·卡比斯; 理查德·D·科莱曼; 瑟格·科罗蒂奥; 威廉姆·L·萨耶尔
、附聚油与加以搅拌和充气,使煤中质组分与油和捕集在附聚物中的空气形成附聚物的方法来从含无机固体的颗粒煤中分离碳质组分。捕集在附聚物中的空气使附聚物有浮,因此附聚物聚集在水面而容易分离,无机残留固体却聚集在水底。含煤无机固体可以与水成浆的形式存在,也可包含预先形成的附聚物,借助搅拌使之分解而形成水浆。后一方法是为了分离那些初始附聚时难以分离的无机固体。搅拌作用可借助搅拌器、搅拌叶轮来完成。
5 处理流中去除有机溶剂的方法 CN89100239.1 1989-01-11 CN1035274A 1989-09-06 詹姆斯·劳·索伦森; 马克·代·亚伯路; 查尔斯·亚·格洛克
结合溶剂提取/电解法公开了一个从处理流分离有机溶剂的改进方法。将含有携带有机溶剂液滴的水溶液送入立式反应器的上方部位,把空气泡从该反应器的底部附近的空气进口送入,水溶液连续地从低于送气泡位置的反应器的底部排出,由此形成气泡和溶剂的对流。气泡结合有机溶剂流滴并可控制地在反应器内的溶液上表面形成泡沫,可容易地收集泡沫并在其中形成有机溶剂的浓缩液。
6 用于从进料浆料中分离出低密度颗粒的方法及装置 CN201180034985.4 2011-06-02 CN103002987A 2013-03-27 凯文·帕特里克·高尔文
在用于从进料浆料中分离低密度颗粒的方法及装置中,泡状混合物在下导管(14)内形成并流至腔室(1)中的中间区域(12)。在该中间区域下方由多个平行倾斜板(6)形成了一个倒置的回流分级器,用于低密度颗粒与更高密度颗粒的有效分离,这些低密度颗粒上升而在该腔室的顶部形成密集泡沫(16),并且更高密度颗粒下落至出口(29)。
7 处理流中去除有机溶剂的方法和设备 CN89100239.1 1989-01-11 CN1027500C 1995-01-25 詹姆斯·劳·索伦森; 马克·代·亚伯路; 查尔斯·亚·格洛克
发明涉及从来自溶剂提取法的提余液和从溶剂中反萃出铜的电解质溶液中除去携带有机溶剂液滴的方法以及在铜电解法从提余液和从溶剂中反萃出铜的电解质溶液回收有机溶剂的设备。
8 에어레이션 및 다른 목적용 거품 생성 KR1020097011171 2007-10-29 KR1020090098963A 2009-09-18 짐머만,윌리엄,바우어,제이; 테사르,바클라브
A method of producing small bubbles (90) of gas in a liquid comprises a source (16) of the gas under pressure, a conduit (64a) opening into a liquid and oscillating the gas passing along the conduit at a frequency between 1 and 100 Hz. The oscillation is effected by fluidic oscillator (10) comprising a diverter that divides the supply into respect outputs (A, B), each output being controlled by a control port, wherein the control ports are interconnected by a closed loop (22). There may be at least two of said conduits (62a, 64a), each output port being connected to one or the other of said conduits, in which one phase of the oscillating gas is employed to drive liquid across the conduit (64a) after formation of a bubble in the other phase of oscillation, whereby the bubble is detached by the force of said driven liquid.
9 분산된 공기 부유선광 거품 및 상기 거품에 의한 토양의 방사성 오염 제거 방법 KR1020147034738 2013-05-10 KR1020150018563A 2015-02-23 포르,실바인; 메살리에,마크
본 발명은 세슘 137 Cs과 같은 적어도 하나의 방사성 핵종으로 오염된 토양을 처리하기 위한, 상기 토양 및 적어도 하나의 콜렉터를 포함하는 현탁액에 기포를 불어 넣음으로써 생성되는 분산된 공기 부유선광 거품에 의하여 상기 방사성 핵종을 분리하는 적어도 하나의 단계를 포함하는 방법에 관한 것이다. 또한, 본 발명은 이러한 방법을 수행하여 얻어진 부유선광 거품에 관한 것이다.
10 폐지펄프의 잉크제거장치와 방법 KR1019940700725 1992-09-04 KR100239630B1 2000-02-01 마일로스크로프타
An apparatus and method for de-inking waste paper pulp using a foam flotation process to recycle printed waste paper for the manufacture of new paper. Pulped printed paper is fed as a slurry to an inlet of a shallow tank. Internal guide walls in the tank establish a flow path from the inlet to an outlet. The walls are sized and positioned to create a generally uniform cross-sectional flow area. A plurality of modules are disposed along the flow path. Each module includes at least one injector that aerates the flow and an extractor that removes floated ink foam. A portion of the flow from each module is recycled to an upstream module, preferably by a conduit and associated pump. In a preferred form, an injector (or injectors) alone located at the inlet is fed by the next downstream module and an extractor alone is located near the outlet. The invention also includes a main recycling loop from the downstream end of the flow path to the upstream end. This main recycling loop has a large flow rate compared to the recycled flow between the modules.
11 에어레이션 및 다른 목적용 거품 생성 KR1020097011171 2007-10-29 KR101378672B1 2014-03-26 짐머만,윌리엄,바우어,제이; 테사르,바클라브
액체 내에 작은 기체 거품(90)을 생성하는 방법은, 압력을 받는 기체 소스(16); 액체로 개방되고 1 내지 100 헤르쯔 사이의 주파수에서 도관을 따라 통과하는 기체를 진동시키는 상기 도관(64a)을 포함한다. 상기 진동은 상기 공급을 각 출력(A, B)으로 나누는 전환기를 포함하는 유체 진동기(10)에 의해 수행되며, 각 출력은 제어 포트에 의해 제어되며, 상기 제어 포트들은 폐루프(22)에 의해 서로 연결된다. 적어도 두 개의 상기 도관들(62a, 64a)이 있을 수 있으며, 각 출력 포트는 상기 도관들의 하나 또는 다른 하나에 연결되며, 상기 진동하는 기체의 한 단계는 다른 단계의 진동에서의 거품 형성 이후에 상기 도관(64a)을 통해 액체를 유도하도록 채용된다. 상기 거품은 상기 유도된 액체의 힘에 의해 떨어진다.
12 폐지로부터의 잉크 제거방법 및 장치 KR1019850006570 1985-09-09 KR1019890001973B1 1989-06-05 시오이리아끼라; 이소베요오지; 하야노히로야스
A process for removing ink from wastepaper comprises (a) introducing an aq. slurry of wastepaper pulp into a treating vessel, (b) blowing air bubbles into the pulp slurry in the vessel to cause the air bubbles to absorb ink particles from the pulp slurry while rising to the surface of the pulp slurry, and (c) removing the resultant ink- absorbed froth from the pulp slurry.
13 Paper recycling processing equipment JP2009186187 2009-08-11 JP5489583B2 2014-05-14 章 川口; 佳久 東本
14 Soil radioactive decontamination process by dispersed air flotation foam and foam thereof JP2012158124 2012-07-13 JP2013238577A 2013-11-28 SYLVAIN FAURE; MARC MESSALIER
PROBLEM TO BE SOLVED: To provide a method for treating soil contaminated by at least one radioactive nuclide, such as cesiumCs.SOLUTION: A process includes at least one step for separating a radioactive nuclide by dispersed air flotation foam. The process includes the following steps. (a) Air foam is injected into a suspension liquid containing soil and at least one collector, and foam is formed by the suspension liquid. (b) At least a portion of the foam is separated from a remaining part of the suspension liquid. The collector is selected among, for example, fatty acid, fatty acid salt and cationic surfactant.
15 Foam generation for aeration and other objects JP2009535112 2007-10-29 JP2010508143A 2010-03-18 バウアー ジェイ ジマーマン ウィリアム; テーザー バツラフ
気体の小さな泡(90)を液体中に作り出す方法は、加圧気体の供給源(16)と、液体中に開口する管路(64a)であって、この管路内を伝わる気体を1と100Hzとの間の周波数にて振動させる管路とを具えている。 この振動は、供給物を個々の出(A,B)に割り振る分流器を具えた流体発振器(10)によってもたらされ、個々の出力は制御ポートによって制御され、制御ポートは閉ループ(22)によって相互に接続されている。 少なくとも2つの前記管路(62a,64a)があってよく、個々の出力ポートが前記管路の一方または他方に接続され、振動する気体の一方の相が振動の他方の相での泡の形成後に液体を管路(64a)中で駆動するために用いられ、それにより泡が前記駆動される液体の力によって分離される。
16 How to separate the SiO2 particles and SiC particles and equipment as well as the separation and recovery SiC JP2003011036 2003-01-20 JP4335541B2 2009-09-30 秀樹 山本; 隼次 芝田
17 Centrifugal flotation device and method JP50523190 1990-03-06 JP3042875B2 2000-05-22 キャンベル,トーマス・ピー
The apparatus includes a powered bowl assembly having a tubular shaft journalled within a base of the apparatus. A pressurized air flow is discharged into slurry in the bowl assembly via a circular array of bubble generators. An impellor discharges the slurry outwardly against an upwardly inclined annular surface of the bowl assembly to cause the slurry to merge upwardly with the streams to promote flotation. Slurry within the bowl assembly forms a vortex with particle flotation forming a froth layer inwardly of a slurry vortex. The froth exits the bowl assembly upwardly past a barrier partially closing the bowl assembly. Heavier gangue particles exit via an outlet about the bowl assembly periphery. A collector shroud is partitioned to receive the froth and the heavier waste material. A modified form of the apparatus includes an independently powered bowl assembly and impellor.
18 JPH07500881A - JP50545093 1992-09-04 JPH07500881A 1995-01-26
An apparatus and method for de-inking waste paper pulp using a foam flotation process to recycle printed waste paper for the manufacture of new paper. Pulped printed paper is fed as a slurry to an inlet of a shallow tank. Internal guide walls in the tank establish a flow path from the inlet to an outlet. The walls are sized and positioned to create a generally uniform cross-sectional flow area. A plurality of modules are disposed along the flow path. Each module includes at least one injector that aerates the flow and an extractor that removes floated ink foam. A portion of the flow from each module is recycled to an upstream module, preferably by a conduit and associated pump. In a preferred form, an injector (or injectors) alone located at the inlet is fed by the next downstream module and an extractor alone is located near the outlet. The invention also includes a main recycling loop from the downstream end of the flow path to the upstream end. This main recycling loop has a large flow rate compared to the recycled flow between the modules.
19 JPH04507213A - JP50523190 1990-03-06 JPH04507213A 1992-12-17
The apparatus includes a powered bowl assembly having a tubular shaft journalled within a base of the apparatus. A pressurized air flow is discharged into slurry in the bowl assembly via a circular array of bubble generators. An impellor discharges the slurry outwardly against an upwardly inclined annular surface of the bowl assembly to cause the slurry to merge upwardly with the streams to promote flotation. Slurry within the bowl assembly forms a vortex with particle flotation forming a froth layer inwardly of a slurry vortex. The froth exits the bowl assembly upwardly past a barrier partially closing the bowl assembly. Heavier gangue particles exit via an outlet about the bowl assembly periphery. A collector shroud is partitioned to receive the froth and the heavier waste material. A modified form of the apparatus includes an independently powered bowl assembly and impellor.
20 Method and apparatus for deinking old paper JP8342585 1985-04-18 JPS61245390A 1986-10-31 SHIOIRI AKIRA; ISOBE YOJI; HAYANO HIROYASU
Wastepaper is treated by a ink-removing process in which an aqueous wastepaper pulp slurry is introduced into a treating vessel, air is blown into the wastepaper pulp slurry preferably through a number of air-blowing orifices formed on a peripheral surface of at least one horizontal cylinder located in the bottom portion of the vessel to absorb ink particles floating in the wastepaper pulp slurry by air bubbles ejected from the orifices and rising toward the wastepaper pulp slurry surface. The resultant ink-absorbed froth is then removed. In this process, air is blown in an amount satisfying the relationship (I) G/L>/=5.0 (I) wherein L is the volume (m3) of the wastepaper pulp slurry in the treating vessel and G is the total volume (Nm3) of the air bubbles blown into the vessel, to promote the contact of the air bubbles with the ink particles in the wastepaper pulp slurry.
QQ群二维码
意见反馈