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 浮选机构 CN88102289 1988-04-16 CN1011490B 1991-02-06 普兰姆·基里斯那斯旺米; 马克·尤金·霍雅克
用三相体系浮选法,从矿石回收矿物的改进浮选槽,通过改进转子定子及浮选室设计在浮选室中形成良好分区,降低泡液中湍流,在室中提供均匀充气,在遇湍流前供给较高的充气量,以提高冶金回收率。描述了转子/定子组合件,形成定子部分的偏导叶片,和泵组合件与室的构形等的参数。
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 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。
3 改良的浮选机构 CN88102289 1988-04-16 CN88102289A 1988-11-23 普兰姆·基里斯那斯旺米; 马克·尤金·霍雅克
用三相体系浮选法,从矿石回收矿物的改良浮选室,通过改良转子定子浮选室设计在浮选室中形成良好分区,降低泡液中湍流,在室中提供均匀充气,在遇湍流前供给较高的充气量,以提高冶金回收。揭示了转子/定子组合件,形成定子部分的偏导叶片,和泵组合件与室的构形等的参数。
4 浮选机转子 CN201380034617.9 2013-05-08 CN104470638B 2017-09-26 R-H.尹; G.勒特雷尔; S.拉加布; D.特利奥尼斯; A-H.赛德; S.米斯科维克; A.诺布尔; 杨义红
一种用于浮选机或者浮选机的浮选单元的转子,包括叶片,该叶片被配置成提供改进的气泡流和气泡产生性能,同时还减少旋转转子以在浮选单元的箱中产生用于生成泡沫的气泡流所需要的动。转子的实施方式还可被配置成比常规的转子设计更小,其可有助于降低转子或者使用该转子的实施方式的浮选机的制造成本。
5 浮选金精矿生物化预处理中的泡沫处理装置及方法 CN201610936297.1 2016-11-01 CN106378266A 2017-02-08 徐祥彬; 郝福来; 李健; 张世镖
发明涉及一种浮选金精矿生物化预处理中的泡沫处理装置及方法,属于浮选金精矿预处理的泡沫处理装置及方法。矿浆表面下部的矿浆才能流到下一级微生物氧化反应器中,在距离矿浆表面上方开一溢流口,用于泡沫自氧化反应器中导出,大部分低于溢流口的泡沫在氧化反应器中降解后进入下一级反应器,来不及降解的少量泡沫产品经溢流口导出,沉积后固液分离,自然降解后返回流程。有益效果是:在微生物氧化反应器中,通过设置深入到矿浆面下的矿浆导管阻挡泡沫,泡沫从溢流口流向预设位置,再通过喷洒清降低泡沫层高度,加速泡沫向溢流口流出,避免泡沫影响,实现分开处理,提高了金回收率。
6 浮选机和浮选方法 CN201180052681.0 2011-10-28 CN103313796B 2015-12-16 利拉·格罗斯曼; 沃尔夫冈·克里格尔施泰因
发明涉及一种浮选机,其具有:包括侧壁和底部(9)的浮选腔(2),搅拌器(3),配属于搅拌器的充气装置(3),布置在浮选腔的上区域上的、用于在浮选时形成的泡沫产物的第一泡沫收集装置(5),和用于向浮选腔供应矿浆的装料管(6),其中,装料管在位于搅拌器的上方的位置(19)上通入浮选腔中,并且在装料管中存在喷射器(7)。本发明此外还涉及一种浮选方法,该浮选方法以两个阶段在浮选机(1)的浮选腔(2)的内部实施,其中,在第一浮选阶段中应用喷射器(7)并且在第二浮选阶段中应用搅拌器(3)。
7 浮选机转子 CN201380034617.9 2013-05-08 CN104470638A 2015-03-25 R-H.尹; G.勒特雷尔; S.拉加布; D.特利奥尼斯; A-H.赛德; S.米斯科维克; A.诺布尔; 杨义红
一种用于浮选机或者浮选机的浮选单元的转子,包括叶片,该叶片被配置成提供改进的气泡流和气泡产生性能,同时还减少旋转转子以在浮选单元的箱中产生用于生成泡沫的气泡流所需要的动。转子的实施方式还可被配置成比常规的转子设计更小,其可有助于降低转子或者使用该转子的实施方式的浮选机的制造成本。
8 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。
9 用于冶金工艺的浮选机的控制方法 CN201510013358.2 2011-09-26 CN104668103A 2015-06-03 A·林内; K·塞罗海默
发明涉及一种使用用于冶金工艺的浮选机的方法并且涉及一种浮选机。所述浮选机从包含疏粒子的含水浆体起泡疏水粒子。该浮选机包括浮选槽(1)和转子(2),该转子在浮选槽内。该转子(2)以混合功率旋转,该混合功率在浆体中维持悬浮并且将空气与浆体混合以形成泡沫,并且该混合功率通过调节转子的旋转速度被控制。确定积聚在槽(1)的底部上的固体物质S的量,并且基于确定的固体物质的量调节转子(2)的旋转速度。该浮选机包括测量装置(5),该测量装置用来确定积聚在该槽的底部上的固体物质的量。调节装置(4)被布置用来基于测量装置(5)的测量结果调节旋转转子(2)的达(3)的旋转速度,以从该槽的底部移除固体物质。
10 浮选机和浮选方法 CN201180052681.0 2011-10-28 CN103313796A 2013-09-18 利拉·格罗斯曼; 沃尔夫冈·克里格尔施泰因
发明涉及一种浮选机,其具有:包括侧壁和底部(9)的浮选腔(2),搅拌器(3),配属于搅拌器的充气装置(3),布置在浮选腔的上区域上的、用于在浮选时形成的泡沫产物的第一泡沫收集装置(5),和用于向浮选腔供应矿浆的装料管(6),其中,装料管在位于搅拌器的上方的位置(19)上通入浮选腔中,并且在装料管中存在喷射器(7)。本发明还涉及一种浮选方法,该浮选方法以两个阶段在浮选机(1)的浮选腔(2)的内部实施,其中,在第一浮选阶段中应用喷射器(7)并且在第二浮选阶段中应用搅拌器(3)。
11 用于浮选机的设备 CN00817967.0 2000-12-20 CN1199702C 2005-05-04 杰弗里·贝尔克
发明涉及一种用于浮选机的设备,其中混合矿浆和传送空气的驱动轴由一驱动装置所驱动并设有一个轴承组件,该驱动轴在内部至少是部分中空的,以便将空气传送至转子。根据本发明,驱动轴(7)在轴承箱内设有至少一个轴承(11),该轴承与至少一个围绕驱动轴(7)形成空气传送室(13)的元件(12)相分离。另外,该驱动轴(7)具有至少一个开口(16),以便在空气传送室(13)和驱动轴(7)内部(17)之间形成基本连续的连通。
12 用于浮选机的设备 CN00817967.0 2000-12-20 CN1414874A 2003-04-30 杰弗里·贝尔克
发明涉及一种用于浮选机的设备,其中混合矿浆和传送空气的驱动轴由一驱动装置所驱动并设有一个轴承组件,该驱动轴在内部至少是部分中空的,以便将空气传送至转子。根据本发明,驱动轴(7)在轴承箱内设有至少一个轴承(11),该轴承与至少一个围绕驱动轴(7)形成空气传送室(13)的元件(12)相分离。另外,该驱动轴(7)具有至少一个开口(16),以便在空气传送室(13)和驱动轴(7)内部(17)之间形成基本连续的连通。
13 JPH0327267B2 - JP6906483 1983-04-19 JPH0327267B2 1991-04-15 JOOJI EI ROORENSU; MAIKURU JEI PUREBETSUTO; YUUJEIN ERU SUMISU
A flotation separation cell is disclosed having a rotor-stator pump assembly wherein a rotor body comprises integrally formed hub, blade and top plate members. These members form a gas chamber in an upper sector of the rotor. The blades are curvilinear and of parabolic or vortex shape. A gas stream which is conveyed to the gas chamber is discharged from the gas chamber in a transverse direction and flows in gas pockets along surfaces of moving blades for dispersion in a slurry.
14 JPS5925630B2 - JP12214079 1979-09-25 JPS5925630B2 1984-06-19 FUUBERUTO FUTSUKUSU
The invention is an apparatus for purifying polluted liquids, especially water. The apparatus comprises a vessel with a relatively large length to width ratio including a reaction zone for contacting the liquid with a gas, separated from the rest of the vessel by a downflow-upflow wall, having a liquid inlet means for introducing a liquid into the reaction zone, the flotation zone connected with the reaction zone occupying the rest of the vessel and a skimmer disposed at the end of the flotation zone for skimming off the floating materials to a channel arranged transverse to the longitudinal axis of the vessel and means for removing the purifying liquid from the apparatus.
15 Rotary vanes for mixing and aeration JP12181877 1977-10-11 JPS53138580A 1978-12-04 ROBAATO EI UIRUSON
A mixing and aeration impeller is comprised of a hub and a plurality of first flutes interspaced between and joined to a plurality of second flutes. The flutes are adapted to the hub and have troughs which begin proximate the hub and extend radially away from and angularly downward and upward away from a plane normal to a shaft to which the impeller is adapted. The flutes are preferably formed as one unitary structure and shaped in a periodic pattern which may be generally sinusoidal or trapezoidal in cross section normal to the radius of the impeller along the length of the troughs. The impeller includes means to receive compressed air from a source and means to exhaust the compressed air radially outward from the rim. The hub has means to receive the compressed air and to communicate it to a passage or gap formed in the flutes to transmit the air radially outward to the rim. The air is exhausted through a slot along the rim of the impeller. A shroud with radial fins may be positioned about the impeller. The impeller used is the agitation means in a flotation machine for recovering mineral values. A method of agitation and aeration is also disclosed.
16 Flotation mechanism JP9328488 1988-04-15 JPS63283769A 1988-11-21 PUREMU KURISHINASUWAMII; MAAKU YUUJIN HOYATSUKU
A flotation cell for recovery of minerals from ore using a three phase system flotation process provides improved metallurgical recovery through improved pump rotor/stator 24, 26 and cell design by establishing good zonal separation within the cell and minimizing froth turbulence, providing uniform aeration in the cell, and accommodating higher aeration volumes before encountering turbulence. Parameters for the rotor/stator pump assembly 22, a deflector vane 36 forming part of the stator, and for the pump assembly/cell configuration are disclosed.
17 Floating separation method and its device JP6906483 1983-04-19 JPS58189055A 1983-11-04 JIYOOJI EI ROORENSU; MAIKURU JIEI PUREBETSUTO; YUUJIEIN ERU SUMISU
A flotation separation cell is disclosed having a rotor-stator pump assembly wherein a rotor body comprises integrally formed hub, blade and top plate members. These members form a gas chamber in an upper sector of the rotor. The blades are curvilinear and of parabolic or vortex shape. A gas stream which is conveyed to the gas chamber is discharged from the gas chamber in a transverse direction and flows in gas pockets along surfaces of moving blades for dispersion in a slurry.
18 Device that dispose polluted liquid JP12214079 1979-09-25 JPS5544400A 1980-03-28 FUUBERUTO FUTSUKUSU
The invention is an apparatus for purifying polluted liquids, especially water. The apparatus comprises a vessel with a relatively large length to width ratio including a reaction zone for contacting the liquid with a gas, separated from the rest of the vessel by a downflow-upflow wall, having a liquid inlet means for introducing a liquid into the reaction zone, the flotation zone connected with the reaction zone occupying the rest of the vessel and a skimmer disposed at the end of the flotation zone for skimming off the floating materials to a channel arranged transverse to the longitudinal axis of the vessel and means for removing the purifying liquid from the apparatus.
19 JPS5310522B1 - JP7349271 1971-09-22 JPS5310522B1 1978-04-14
1369053 Froth flotation; aerating and circulating liquids L H LOGUE 1 Sept 1971 [24 Sept 1970] 40791/71 Headings B1C and B2H In a froth flotation apparatus comprising a cell 10, Fig. 1, through which pulp to be separated is circulated and having an overflow 11a, 11b for the froth containing the desired separated pulp. constituent, a venturi tube aerator 24 is mounted in a submerged upright position in the cell and gas under pressure and pulp are delivered to a lower intake portion 27a of the venturi tube where they are mixed together, the mixture ascends through an upper discharge portion 27b of the tube in which precipitation of dissolved gas in the mixture on to the desired pulp constituent occurs, and the aerated pulp is discharged from the upper edge 28 to the pulp or froth in the cell, the discharge portion 27b of the venturi tube being longer than the intake portion 27a and its angle of divergence being smaller than the angle of convergence of the latter portion. Aerating gas is admitted to the portion 27a from a header 14 via valves 15, 20, a belt-driven hollow rotary shaft 16 and a hollow hub member 21 carried by the shaft and provided with outlet openings 25. The hub member carries a bladed impeller 22 which draws the gas, and pulp entering via baffles 23, upwardly through turbulent-preventing vanes 26 into the interior of the venturi portion 27a whereby the gas is mixed with the liquid portion of the pulp. After passing the constriction 30, a pressure drop in the flow results in gas precipitation in fine bubbles which attach themselves to the desired pulp constituent. At the upper edge 28 of the venturi tube, a deflector 29 directs the aerated pulp to the pulp or froth in the cell. The desired constituent with attached air bubbles is carried in the froth across the overflow 11a, 11b. Unfloated desired constituents are directed in a downward circulation to the intake of the venturi tube for retreatment. In a first modification, Fig. 3 (not shown), there is no deflector and the aerated pulp is discharged directly into the pulp body in the cell. In a second modification, Fig. 4 (not shown), the aerating gas is fed to the bottom of the venturi tube through a nozzle and there are no vanes 26. In a third modification, Fig. 5, an intake tube 41 projecting into the upper portion of the cell is connected to a gas supply tube 43 at a constricted portion 42 and to a pump 40 which discharges pulp and gas dissolved therein via a nozzle 44 and an openended flaring baffle 45 to the base of the venturi tube. In a further modification, Fig. 6, gas is drawn via a rotary hollow shaft 16a and an intake 52 into an impeller 50 which also draws in recirculating pulp through an intake 53 and delivers the gas-pulp mixture to the bottom of the venturi tube at the entrance of which blades 56 are disposed.
20 음식물쓰레기의 폐비닐 선별장치 KR1020040034772 2004-05-17 KR1020050109759A 2005-11-22 심호섭
본 발명은 음식물쓰레기의 폐비닐 선별장치에 관한 것으로, 더욱 상세하게는 음식물처리시스템의 선별공정을 통하여 음식물쓰레기로부터 선별된 폐비닐과 잔여음식찌꺼기를 용이하게 선별할 수 있는 장치로서, 특히 선별을 위한 공간에서 공기의 흐름에 의해 폐비닐이 분리 선별될 수 있는 부유(浮游)분위기를 형성하여 더욱 향상된 선별 효율성을 얻을 수 있는 음식물쓰레기의 폐비닐 선별장치에 관한 것이다. 이러한 음식물쓰레기의 폐비닐 선별장치는, 음식물처리시스템에서 순수음식쓰레기로부터 선별된 음식이물질에서 폐비닐과 잔여음식찌꺼기를 선별하는 장치로서, 음식이물질을 선별하기 위한 공간을 제공하는 하우징과, 이 하우징의 내부에 위치하며 회전 타격 동작에 의해 음식이물질을 타격하여 잔여음식찌꺼기를 분쇄함과 동시에 공기의 흐름에 의해 폐비닐의 선별을 유도하기 위한 분위기를 형성하는 타격구 어셈블리와, 이 타격구 어셈블리의 타격 동작을 위한 동력을 전달하는 구동부와, 상기 타격구 어셈블리에 의해 선별된 폐비닐을 상기 케이스 외부로 배출하기 위한 배출부를 포함하며, 상기 타격구 어셈블리는, 상기 구동부와 동력 전달이 가능하게 연결되는 회전축과, 이 회전축의 원주방향으로 다수개가 설치되며 음식이물질을 타격하기 위한 타격플레이트와, 상기 하우징의 내부 공간에서 폐비닐의 선별을 위한 부유분위기를 형성하는 부유수단을 포함하고, 상기 부유수단은, 폐비닐의 부유를 위한 구간에 대응하여 일방향 흐름의 공기 유도가 가능한 블레이드들을 갖는 팬 형태로 이루어지고, 상기 회전축 상에 설치되어 이 축의 회전시 상기 하우징 외부의 공기를 강제 흡인하여 흡인된 공기로 상기 배출부측에 대응하여 폐비닐의 부유를 위한 분위기를 형성하는 것을 특징으로 한다.
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