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    • 1. 发明授权
    • Method for separating fine particles by selective hydrophobic coagulation
    • 通过选择性疏水凝结分离细颗粒的方法
    • US5161694A
    • 1992-11-10
    • US513884
    • 1990-04-24
    • Roe-Hoan YoonGerald H. Luttrell
    • Roe-Hoan YoonGerald H. Luttrell
    • B03B1/04B03C1/01B03D3/02
    • B03D3/02B03B1/04B03C1/01
    • A process of selectively agglomerating coal in an aqueous environment while leaving the mineral matter dispersed has been developed. This process is autogenous for hydrophobic particles in that neither an agglomerating agent nor an electrolytic coagulant is needed. It is based on the finding that hydrophobic particles are pushed against each other by the surrounding water structure. This process, which is referred to as selective hydrophobic coagulation, is driven by the so-called hydrophobic interaction energy, which is not included in the classical DLVO theory describing the stability of lyophobic suspensions. The relatively small coagula formed by the selective hydrophobic coagulation process can be readily separated from the dispersed mineral matter by several different techniques such as screening, elutriation, sedimentation and froth flotation.
    • 已经开发出在分离矿物质的同时在含水环境中选择性凝集煤的方法。 该方法对于疏水性颗粒是自生的,因为不需要附聚剂和电解凝结剂。 这是基于以下发现:疏水性颗粒被周围的水结构相互推压。 被称为选择性疏水性凝血的这个过程是由所谓的疏水相互作用能量驱动的,它不包括在描述疏液性悬浮液稳定性的经典DLVO理论中。 通过选择性疏水凝结方法形成的相对较小的凝结剂可以通过几种不同的技术,如筛选,淘析,沉淀和泡沫浮选,容易地从分散的矿物质中分离出来。
    • 2. 发明授权
    • Method for dewatering fine coal
    • 脱水细煤的方法
    • US5458786A
    • 1995-10-17
    • US229012
    • 1994-04-18
    • Roe-Hoan YoonGerald H. Luttrell
    • Roe-Hoan YoonGerald H. Luttrell
    • B03B1/04C02F1/54C02F11/14F26B5/00
    • C02F1/547B03B1/04C02F1/54C02F11/14F26B5/005C02F2101/10C02F2101/105C02F2101/20C02F2101/32F26B2200/18
    • Fine coals are dewatered in an energy efficient process in which a non-polar liquid or a mixture of different hydrophobic liquids are used to displace the water from the coal surface. This process works with higher rank coals that are naturally hydrophobic so that the coal surface from which the water is displaced has a stronger affinity for the hydrophobic liquid than the water. Thermodynamically, this process is spontaneous and, hence, requires no energy. The only energy required for this process is to recover the spent hydrophobic liquid(s) for recycling purposes. The hydrophobic liquids are recovered in gaseous form either by lowering the pressure or by heating, and coverted back to liquid form for re-use. The most economical reagents that can be used for this purpose include propane, butane, pentane, and ethane. Carbon dioxide can also be used for the dewatering process described in the present invention. The process of dewatering by displacement is capable of achieving the same level of moisture reduction as thermal drying but at substantially lower energy costs.
    • 精细煤在能量有效的过程中脱水,其中使用非极性液体或不同疏水性液体的混合物来从煤表面置换水。 该方法与具有天然疏水性的较高级煤一起工作,使得水被排出的煤表面​​与疏水性液体相比具有比水更强的亲和性。 在热力学上,这个过程是自发的,因此不需要能量。 该方法所需的唯一能量是回收用于回收目的的废疏水性液体。 疏水性液体通过降低压力或加热回收成气态,并被覆盖回液体形式以供再利用。 可用于此目的的最经济的试剂包括丙烷,丁烷,戊烷和乙烷。 二氧化碳也可用于本发明所述的脱水方法。 通过置换脱水的过程能够实现与热干燥相同的水分降低水平,但是以显着更低的能量成本。
    • 7. 发明授权
    • Method for dewatering particles
    • 颗粒脱水方法
    • US5587085A
    • 1996-12-24
    • US476513
    • 1995-06-07
    • Roe-Hoan YoonGerald H. Luttrell
    • Roe-Hoan YoonGerald H. Luttrell
    • B03B1/04C02F1/54C02F11/14F26B5/00
    • C02F1/547B03B1/04C02F1/54C02F11/14F26B5/005C02F2101/10C02F2101/105C02F2101/20C02F2101/32F26B2200/18
    • Fine particles are dewatered in an energy efficient process in which a non-polar liquid or a mixture of different hydrophobic liquids are used to displace the water from the particle surface. Thermodynamically, this process is spontaneous. The only energy required for this process is to recover the hydrophobic liquid(s) for recycling purposes. The hydrophobic liquids are recovered in gaseous form either by lowering the pressure or by heating, and converted back to liquid form for re-use. The most economical reagents that can be used for this purpose include propane, butane, pentane, and ethane. Carbon dioxide may also be used for the dewatering process described in the present invention. The process of dewatering by displacement is capable of achieving the same or better level of moisture reduction as thermal drying but at substantially lower energy costs.
    • 精细颗粒在能量有效的过程中脱水,其中使用非极性液体或不同疏水性液体的混合物来从颗粒表面置换水。 在热力学上,这个过程是自发的。 该方法所需的唯一能量是回收用于回收目的的疏水性液体。 通过降低压力或通过加热将疏水性液体回收成气态,并转化回液体形式重新使用。 可用于此目的的最经济的试剂包括丙烷,丁烷,戊烷和乙烷。 二氧化碳也可用于本发明所述的脱水方法。 通过位移脱水的过程能够实现与热干燥相同或更好的水分降低水平,但是以显着更低的能量成本。
    • 10. 发明授权
    • Flotation separation device and method
    • 浮选分离装置及方法
    • US08960443B2
    • 2015-02-24
    • US12101376
    • 2008-04-11
    • Michael J. MankosaJaisen KohmuenchEric S. YanGerald H. Luttrell
    • Michael J. MankosaJaisen KohmuenchEric S. YanGerald H. Luttrell
    • B03D1/02B03D1/14B03D1/24B03D1/22B03D1/08
    • B03D1/16B01F3/04B03D1/028B03D1/082B03D1/1487B03D1/22B03D1/24B03D1/247
    • A flotation separation system is provided for partitioning a slurry that includes a hydrophobic species which can adhere to gas bubbles formed in the slurry. The flotation separation system comprises a flotation separation cell that includes a sparger unit and a separation tank. The sparger unit has a slurry inlet for receiving slurry and a gas inlet to receive gas with at least enough pressure to allow bubbles to form in the slurry within the sparger unit. The sparger unit includes a sparging mechanism constructed to disperse gas bubbles within the slurry. The sparging mechanism sparges the gas bubbles to form a bubble dispersion so as to cause adhesion of the hydrophobic species to the gas bubbles substantially within the sparger unit while causing a pressure drop of about 10 psig or less across the sparging mechanism. The sparger unit includes a slurry outlet to discharge the slurry and the bubble dispersion into the separation tank.
    • 提供浮选分离系统用于分配浆料,其包括能粘附在浆料中形成的气泡的疏水性物质。 浮选分离系统包括浮选分离单元,其包括分布器单元和分离罐。 分布器单元具有用于接收浆料的浆料入口和用于以至少足够的压力接收气体的气体入口,以允许在分布器单元内的浆料中形成气泡。 该分布器单元包括一个构造成将气泡分散在浆料内的喷射机构。 喷射机构喷射气泡以形成气泡分散体,以便引起疏水物质基本上在分布器单元内的气泡粘附,同时在喷射机构上引起约10psig或更小的压降。 喷射器单元包括浆料出口,用于将浆料和气泡分散体排出到分离罐中。