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    • 1. 发明授权
    • Process for melting a ferrous burden
    • 熔化亚铁负担的过程
    • US4556418A
    • 1985-12-03
    • US657121
    • 1984-10-03
    • Andrew J. Syska
    • Andrew J. Syska
    • C21B11/02C21B13/14
    • C21B11/02C21B13/14Y02P10/136Y10S266/90
    • A process for melting a ferrous burden comprising scrap iron, scrap steel, pig iron, direct reduced iron or mixtures thereof without the use of coke is provided. Air or enriched air as a primary oxidant is preheated and together with fuel is combusted to form a reducing atmosphere in a shaft furnace or forehearth which melts the ferrous burden in the melting zone of the shaft furnace. The reducing atmosphere leaving the melting zone of the shaft furnace is further combusted with a secondary oxidant in the preheating zone of the shaft furnace. The top gas from the preheating zone of the shaft furnace is combusted with a tertiary oxidant to provide a heated flue gas to preheat the primary oxidant. Optionally, the heat remaining in the flue gas after preheating the primary oxidant may be recovered in a waste heat recovery device.
    • 提供了一种用于熔炼含铁废料的方法,包括废铁,废钢,生铁,直接还原铁或其混合物,而不使用焦炭。 作为主要氧化剂的空气或富集空气被预热,并与燃料一起燃烧,以便在竖炉或炉床中形成还原气氛,其熔化竖炉熔化区中的铁质负荷。 离开炉膛熔化区的还原气氛在竖炉的预热区中与次级氧化剂进一步燃烧。 来自竖炉的预热区域的顶部气体与第三氧化剂一起燃烧以提供加热的烟道气以预热主氧化剂。 任选地,在预热初级氧化剂之后残留在烟道气中的热量可以在废热回收装置中回收。
    • 2. 发明授权
    • Pneumatic transport and heat exchange systems
    • 气动运输和热交换系统
    • US4575948A
    • 1986-03-18
    • US467392
    • 1983-02-17
    • Lester G. MasseyLawrence G. ClawsonAndrew J. Syska
    • Lester G. MasseyLawrence G. ClawsonAndrew J. Syska
    • B01J8/18F23L15/04F28C3/12F28D19/02F26B3/10
    • B01J8/1836F23L15/04F28C3/12F28D19/02B01J2208/00053B01J2208/0007B01J2208/00088B01J2208/00371Y02E20/348
    • Gas-solids transport and heat exchange techniques are disclosed wherein solid particulate material is circulated in a "figure 8" or a circular flow path for selective contact and/or direct heat exchange with gaseous media. The particulate material is introduced into streams of gaseous media at spaced locations in the flow path and subsequently separated from the gaseous streams following contact and/or heat exchange therewith. The gaseous streams are maintained separate from one another by loose packed bed columns of particulate material formed in the flow path and used to introduce the particulate material into the gaseous streams. The flow rate of the particulate material is regulated by the controlled biasing of particulate material from each of the columns thereof directly into the gaseous streams, and the particulate material is circulated solely through the use of the gaseous media and the force of gravity. The particulate material is circulated in cocurrent relationship with each of the gaseous streams in figure 8 flow path systems and, in circular flow path systems, the particulate material is circulated in cocurrent relationship with one of the gaseous streams and in countercurrent relationship with the other of the gaseous streams. In heat exchange applications, heat transfer between the streams of gaseous media is provided as a function of the flow rate of the particulate material and the relative flow rates of the streams of gaseous media.
    • 公开了气固体输送和热交换技术,其中固体颗粒材料在“图8”或圆形流动路径中循环,用于与气体介质的选择性接触和/或直接热交换。 颗粒材料在流动路径中的间隔位置处被引入气态介质流中,随后在与其接触和/或热交换之后与气流分离。 通过在流动路径中形成的颗粒材料的松散填充床柱将气流彼此分离,并将颗粒材料引入气流中。 颗粒材料的流速通过将颗粒材料从其每个柱的受控偏压直接进入气流来调节,并且颗粒材料仅通过使用气体介质和重力循环。 颗粒材料与图8流路系统中的每种气流以并流关系循环,并且在圆形流动路径系统中,颗粒材料与气流中的一种以并流关系循环并与另一种气流形成逆流关系 气流。 在热交换应用中,提供气体介质流之间的热传递作为颗粒材料的流速和气体介质流的相对流速的函数。
    • 4. 发明授权
    • Process for the production of intermediate hot metal
    • 中间热金属生产工艺
    • US4111687A
    • 1978-09-05
    • US737699
    • 1976-11-01
    • Andrew J. Syska
    • Andrew J. Syska
    • C21B13/02C21B13/14C21C5/32C21C5/52
    • C21B13/14C21B13/02C21B13/023C21C5/32Y02P10/122Y02P10/136Y02P10/216Y02P10/265Y02P10/283
    • A process and apparatus for the production of intermediate hot metal suitable for further refining into steel is disclosed.The basic process includes the steps of heating a charge of ore in a reducing furnace having a reducing atmosphere therein comprising a mixture of reconditioned and recycled top gas from the reducing furnace and off-gas rich in hydrogen and carbon monoxide produced by a cupola melting unit to reduce the ore to iron, partially carburizing the reduced iron in the reducing furnace with carbon-containing off-gas produced by the cupola melting unit, and melting the reduced and carburized iron together with scrap, slag forming additives and fluxes in a cupola melting unit having a reducing atmosphere therein produced by the combustion of a rich fuel/oxidant mixture to form a molten slag and molten iron suitable for the further refining to produce steel. The process contemplates the further refining of the molten iron from the cupola in an electric steelmaking furnace or an oxygen steelmaking converter. In an alternative form of the process, the reduced and carburized iron is cooled within or outside the reducing furnace to form prereduced metal pellets suitable for use as a part of the burden in a melting unit.The apparatus comprises a refractory lined cupola melting unit portion equipped with burners capable of burning a rich fuel/oxidant mixture to produce a reducing atmosphere within the melting unit and off-gas rich in gaseuos reductants, a direct reducing unit portion communicating with the upper end of the melting unit to receive the melting unit off-gas recirculating and conditioning means to recycle at least a portion of the top gas from the upper region of the reducing unit portion to the lower region of the reducing unit portion, means for introducing ore into the direct reduction unit portion of the apparatus, and means for introducing additives and fluxes into the melting unit portion of the apparatus.
    • 5. 发明授权
    • Recirculating burner
    • 循环燃烧器
    • US3990831A
    • 1976-11-09
    • US610250
    • 1975-09-04
    • Andrew J. Syska
    • Andrew J. Syska
    • F23C9/00F23D11/00F23M3/00
    • F23C9/00F23D11/005F23C2202/10F23C2900/06041F23C2900/09002
    • A burner for burning a vaporizable liquid fuel, comprising a suction chamber, a combustion chamber, an air inlet to the suction chamber, a vaporizing chamber, a first passage interconnecting the combustion chamber with the vaporizing chamber, a second passage interconnecting the vaporizing chamber with the suction chamber, a liquid fuel inlet atomizer connected to the vaporizing chamber, and a vortex generator at the interface of the fuel inlet atomizer, first passage, and vaporizing chamber, the generator swirling hot combustion gases from the first passage into a vortex, into which vortex the fuel inlet atomizer directs atomized liquid fuel, the first passage, vortex generator, vaporizing chamber, and second passage together defining a recirculation path, the path having sufficient width to maintain blue-flame combustion, whereby the fuel will be vaporized by hot combustion gases as it passes through the vortex generator and the vaporizing chamber, the air inlet creating a suction which draws hot combustion gases and vaporized fuel from the vaporizing chamber through the second passage and suction chamber, thereby producing a mixture for burning in the combustion chamber.
    • 一种用于燃烧可汽化液体燃料的燃烧器,包括吸入室,燃烧室,到吸入室的空气入口,蒸发室,将燃烧室与蒸发室相互连接的第一通道,将蒸发室与 吸入室,连接到蒸发室的液体燃料入口雾化器和在燃料入口雾化器,第一通道和蒸发室的界面处的涡流发生器,发电机将热燃烧气体从第一通道旋转成涡流,形成 燃料入口雾化器的涡流引导雾化的液体燃料,第一通道,涡流发生器,蒸发室和第二通道共同限定再循环路径,该路径具有足够的宽度以保持蓝焰燃烧,由此燃料将被热蒸发 燃烧气体在通过涡流发生器和蒸发室时,空气入口产生吸入口wh 通过第二通道和吸入室从蒸发室吸入热的燃烧气体和蒸发的燃料,从而产生在燃烧室中燃烧的混合物。