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    • 7. 发明授权
    • System for transporting particulate solids from high temperature to low
temperature zone
    • 将颗粒固体从高温运送到低温区的系统
    • US4301138A
    • 1981-11-17
    • US143172
    • 1980-04-24
    • Kenneth W. RyanElmer H. Rogers, Jr.
    • Kenneth W. RyanElmer H. Rogers, Jr.
    • B01J8/00C01F7/60F27B15/08
    • C01F7/60B01J8/003Y10S423/16
    • Fluidizable particulate solids are removed from a first zone operating at a relatively higher temperature and pressure to a second zone or collector operating or maintained at a lower temperature and pressure by an improved drain or particle removal system. The improved system includes moving the particles from the first zone downwardly within a substantially vertical inlet conduit or leg into the lower regions of a first chamber and upwardly through that chamber under fluidized particle transport conditions energized by a fluidizing media provided in the chamber. The particles move to a second chamber by overflowing a weir separating the first and second chambers and are mixed with cooler particles which extract heat within the second chamber under fluidized particle transport conditions energized by a second fluidizing gas source which further transports the particles to the collector or second zone. Heat is removed from the second chamber by indirect heat exchange. The volume of fluidizing gas for the second chamber is much larger than that for the first chamber and provides for particle flow rate control in combination with a flow restriction. Particle flow is interrupted by stopping the particle flow out of, and the gas flow into, the second chamber while maintaining fluidizing gas flow into the first chamber and the inlet leg. The system is particularly suited to draining unreacted alumina from a chlorination reactor for producing gaseous aluminum chloride from particulate alumina.
    • 可流动的颗粒固体从在相对更高的温度和压力下操作的第一区域移除到通过改进的排水或颗粒去除系统操作或保持在较低温度和压力下的第二区域或集水器。 改进的系统包括将颗粒从第一区域向下移动到基本上垂直的入口导管或腿部内进入第一室的下部区域,并且在由设置在室中的流化介质激励的流化颗粒运输条件下向上通过该室。 颗粒通过溢出分离第一和第二室的堰而移动到第二室,并与在由第二流化气体源激励的流化颗粒运输条件下在第二室内提取热量的冷却器颗粒混合,所述第二流化气体源将颗粒进一步输送到收集器 或第二区。 通过间接热交换将热量从第二室排出。 用于第二室的流化气体的体积比第一室的流化气体的容积大得多,并提供与流量限制相结合的颗粒流速控制。 通过使颗粒流出停止,并且气体流入第二室,同时保持流化气体流入第一室和入口支管而中断颗粒流动。 该系统特别适于从用于从颗粒氧化铝生产气态氯化铝的氯化反应器中排出未反应的氧化铝。
    • 8. 发明授权
    • Process for the production of aluminum chloride
    • 氯化铝生产工艺
    • US4289735A
    • 1981-09-15
    • US117462
    • 1980-02-01
    • Hans P. MuellerHanspeter AlderGerhard Zhuber-Okrog
    • Hans P. MuellerHanspeter AlderGerhard Zhuber-Okrog
    • C01F7/60C22B1/08C22B21/00C01F7/56
    • C01F7/60C22B1/08C22B21/0007C22B21/0046Y10S423/16
    • The efficiency of a given reactor for the conversion of aluminum oxide bearing starting material by means of reducing and chlorinating gases or of carbon coated aluminum oxide bearing starting material by means of chlorinating gases in a solid/gas fluidized bed to yield aluminum chloride is improved by the addition of an inert, solid dilution agent to the bed. Whereas, as a result of the chemical reaction, the average particle size and bulk density of the reagent decreases in a batch process, and in a continuous process an equilibrium value is reached, the average particle size and the bulk density of the inert material remains unchanged. An initial average particle size of 60-80 microns proved successful; quartz, corundum, magnesium oxide of similar particle size and bulk density was added as dilution agent, and a gas flow rate of 2 to 30 cm/sec was attained along with quantitative conversion of the gaseous reagent. The increase in the space-time-yield of a fluidized bed reactor, measured by the conversion achieved before onset of breakthrough in the fluidized bed, amounted to 58 to 65%.
    • 通过在固/气流化床中通过氯化气体还原和氯化气体或含碳涂覆的氧化铝负载起始材料以得到氯化铝,给定的反应器用于转化含氧化铝原料的效率得到改善 向床中加入惰性固体稀释剂。 而作为化学反应的结果,试剂的平均粒度和体积密度在间歇过程中减少,而在连续过程中,达到平衡值,惰性材料的平均粒度和体积密度保持 不变 60-80微米的初始平均粒径证明是成功的; 加入石英,刚玉,粒径相似的体积和体积密度的氧化镁作为稀释剂,气态试剂的定量转化得到2〜30cm / sec的气体流量。 流化床反应器的时空产量的增加通过在流化床中的穿透开始之前实现的转化率来测量,达58%至65%。
    • 10. 发明授权
    • Production of aluminum trichloride and magnesium oxide
    • 生产三氯化铝和氧化镁
    • US3939247A
    • 1976-02-17
    • US391747
    • 1973-08-27
    • Sven Fougner
    • Sven Fougner
    • C01F5/02C01F7/60C01F7/56
    • C01F5/02C01F7/60
    • Alumina is reacted with magnesium chloride in accordance with the chemical reactionAl.sub.2 O.sub.3 + 3MgCl.sub.2 .fwdarw.3MgO + 2AlCl.sub.3In the presence of a mixed mass of inert solid contact material, such as a fluidized mass of magnesium oxide particles. The aluminum trichloride is recovered and is advantageously employed in the treatment of hydrocarbonaceous material, such as retorted shale oil, to improve the physical and/or chemical properties thereof. The substantially carbon and/or hydrocarbon free retorted aluminiferous oil shale is useful as the source of the alumina in the above chemical reaction.
    • 氧化铝根据化学反应Al2O3 + 3MgCl2-> 3MgO + 2AlCl3与氯化镁反应,在混合质量的惰性固体接触材料(如氢氧化镁氧化物颗粒)中存在。 回收三氯化铝,并且有利地用于处理含烃材料,例如蒸馏页岩油,以改善其物理和/或化学性质。 在上述化学反应中,基本上碳和/或无烃蒸馏的含铝油页岩可用作氧化铝的来源。