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    • 3. 发明授权
    • Method and apparatus for gasification of organic materials
    • 有机材料气化的方法和装置
    • US5656044A
    • 1997-08-12
    • US486372
    • 1995-06-07
    • Norman G. BishopRicardo Viramontes-Brown
    • Norman G. BishopRicardo Viramontes-Brown
    • C10J3/06C10J3/14C10J3/66C10J3/60
    • C10J3/002C10J3/06C10J3/14C10J3/66C10K1/003C10K1/026C10K1/101C10J2200/152C10J2200/158C10J2300/0959C10J2300/1223C10J2300/1621C10J2300/165C10J2300/1687C10J2300/1693
    • A process and apparatus for gasification of organic materials (typically incorporated in domestic and industrial wastes, including auto shredder residues) to produce useful synthesis gas (with a major content CO and H.sub.2) with effectively non-toxic ash residue by means of at least one continuously operated burner, preferably stoichiometrically balanced (1:2 for natural gas/oxygen) at least at startup and shut down (optionally with some excess of oxygen, usually under steady-state conditions, such as at a ratio of 1:4 or higher, especially if the charge has well over 18% water content), directed into a primary single stage reaction zone (through an opening in common with the effluent product gas discharged therefrom such as to assure intimate contact therebetween), which zone contains a tumbling charge in a rotating barrel-shaped horizontal reactor thus heated to from about 650.degree. to about 800.degree. C. (below the incipient fusion temperature of the charge) and controlled to remain in such temperature range (by adjustment of the burner volume and fuel-to-oxygen ratio for any given charge) resulting in thermally cracking and gasifying the organic materials in the charge and reacting the complex hydrocarbons and gas evolved (1) normally with the CO.sub.2 and H.sub.2 O derived from burner combustion of a fuel and oxygen-containing gas at a high flame temperature, typically 2500.degree. to 3000.degree. C., (2) with excess oxygen, and/or (3) partially with H.sub.2 O or CO.sub.2 otherwise added to or, present in, the charge.
    • 一种用于气化有机材料(通常并入家用和工业废物,包括自动粉碎机残渣)的方法和装置,以通过至少一种有效的无毒灰渣来生产有用的合成气(主要含量为CO和H 2) 至少在启动和关闭时(可选地使用一些过量的氧气,通常在稳态条件下,例如以1:4或更高的比例)连续操作的燃烧器,优选化学计量平衡(天然气/氧气为1:2) ,特别是如果电荷具有超过18%的含水量),引导到初级单级反应区(通过与从其排出的流出物产物气体相同的开口,以确保其间的紧密接触),该区域包含翻滚电荷 在旋转的桶形水平反应器中,由此加热至约650℃至约800℃(低于电荷的初始熔融温度)并控制为保持在 温度范围(通过调整任何给定电荷的燃烧器体积和燃料与氧气的比例),导致电荷中的有机材料的热裂化和气化,并使复杂烃和通常放出的气体(1)与CO 2和H 2 O 来自燃烧器和含氧气体的燃烧器燃烧,所述燃料和含氧气体在高火焰温度(通常为2500°至3000℃),(2)具有过量的氧气,和/或(3)部分地用H 2 O或CO 2加入或, 现在,收费。
    • 8. 发明授权
    • Apparatus for the pneumatic transport of large iron-bearing particles
    • 用于气动输送大型含铁颗粒的装置
    • US5445363A
    • 1995-08-29
    • US71756
    • 1993-06-09
    • Jorge O. Becerra-NovoaRicardo Viramontes-BrownMarco A. Flores-VerdugoJose J. Garza-Ondarza
    • Jorge O. Becerra-NovoaRicardo Viramontes-BrownMarco A. Flores-VerdugoJose J. Garza-Ondarza
    • C21B13/00C21B13/14F27B3/18F27B3/19
    • C21B13/14C21B13/00C21B13/0086Y02P10/122Y02P10/136Y02P10/143
    • In method and apparatus for producing iron and steel from iron cores largely composed of iron oxides, wherein a direct reduction process is used to produce a solid particulate intermediate product, generally known as sponge Iron or Direct Reduced Iron (DRI); pneumatically conveying large iron-bearing particles, such as pelletized iron ore or particularly DRI, in a closed transport pipe, eg. from the reduction reactor of the direct reduction process to the metallurgical furnaces where liquid iron or steel are produced, for example electric arc furnaces, induction furnaces, basic oxygen furnaces, etc. or to a briquetting press to form DRI briquettes, or simply to a silo or storage bin, or in general to a subsequent processing step for said DRI. When the carrier gas is recirculated for reuse, surprisingly air can be a preferred source of such gas, especially for reactive hot DRI. This method has a superior efficiency and productivity and reduces the overall energy consumption relative to currently used DRI steelmaking plants.By using pneumatic conveyors, elements of the plant may be arranged side by side rather than one on top of the other, whereby the overall height of the plant may be reduced.
    • 主要由铁氧化物构成的铁芯生产铁和钢的方法和装置,其中直接还原工艺用于生产通常称为海绵铁或直接还原铁(DRI)的固体颗粒中间产物; 将诸如造粒铁矿石或特别是DRI的大型含铁颗粒气动输送到封闭的输送管中,例如, 从直接还原工艺的还原反应器到生产液态铁或钢的冶金炉,例如电弧炉,感应炉,碱性氧气炉等,或用于压块机以形成DRI压块,或简单地 仓库或存储箱,或通常用于所述DRI的后续处理步骤。 当载气再循环以重新使用时,令人惊讶的是,空气可以是这种气体的优选来源,特别是对于反应性热DRI。 与目前使用的DRI炼钢厂相比,该方法具有优异的效率和生产率,降低了总体能耗。 通过使用气动输送机,植物的元件可以并排设置,而不是一个在另一个之上,由此可以减少植物的整体高度。
    • 10. 发明授权
    • Method of making sponge metal
    • 制造海绵金属的方法
    • US4375983A
    • 1983-03-08
    • US234317
    • 1981-02-13
    • Juan CeladaPatrick W. MacKayJuan F. Price-FalconRicardo Viramontes-Brown
    • Juan CeladaPatrick W. MacKayJuan F. Price-FalconRicardo Viramontes-Brown
    • C21B13/04C21B13/02
    • C21B13/04Y02P10/122Y02P10/128Y02P10/136Y02P10/212
    • A method for the batchwise reduction of iron ore to sponge iron in a multiple unit reactor system is disclosed in which (a) separate fixed beds of iron-bearing material are simultaneously treated in at least one cooling reactor and at least two reduction reactors, (b) a reducing gas composed largely of carbon monoxide and hydrogen is used to cool the iron-bearing material in said cooling reactor and thereafter to reduce the iron-bearing material in said reduction reactors, (c) a stream of said reducing gas is caused to pass through the fixed bed of iron ore in said cooling reactor and then cooled and (d) a portion of the cooled effluent reducing gas from said cooling reactor is recycled thereto, the improvement which comprises causing the remainder of the cooling reactor effluent gas to be fed to said reduction reactors and to flow in parallel through the fixed beds of metal-bearing material in said reduction reactors, and heating the reducing gas fed to said reduction reactors before it enters said reactors in a gas superheater without combustion of said gas to a temperature of at least 900.degree. C.
    • 公开了一种在多单元反应器系统中将铁矿石分批还原成海绵铁的方法,其中(a)在至少一个冷却反应器和至少两个还原反应器中同时处理单独的含铁材料固定床( b)主要由一氧化碳和氢气组成的还原气体用于冷却所述冷却反应器中的含铁材料,之后还原所述还原反应器中的含铁材料,(c)引起所述还原气体流 在所述冷却反应器中通过铁矿石的固定床,然后冷却,并且(d)将来自所述冷却反应器的冷却的排出物还原气体的一部分再循环到其中,所述改进包括使剩余的冷却反应器流出气体 被供给到所述还原反应器并且通过所述还原反应器中的含金属材料的固定床平行流动,并且在所述还原反应器之前加热供给到所述还原反应器的还原气体 它在气体过热器中进入所述反应器,而不将所述气体燃烧至至少900℃的温度。