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    • 2. 发明申请
    • Vessel for enabling a uniform gravity driven flow of particulate bulk material therethrough, and direct reduction reactor incorporating same
    • 允许颗粒体材料通过其的均匀重力驱动流动的容器,以及包含其的直接还原反应器
    • US20020179640A1
    • 2002-12-05
    • US10161427
    • 2002-05-30
    • HYLSA, S.A. DE C.V.
    • Raul Gerardo Quintero-FloresJorge Octavio Becerra-NovoaJuan Celada-GonzalezMaria Teresa Guerra-ReyesRonald Victor Manuel Lopez-Gomez
    • B67D005/60
    • B65D88/28
    • So as to provide a container that is inexpensive to manufacture and that promotes a uniform flow of particulate bulk materials therethrough, a vessel (10) is suggested comprising at least two wall segments (12, 14) having a generally downwardly converging wall defining a vertical axis for said vessel, a first upper segment (12) being vertically arranged above a second lower segment (14), each one of said wall segments having an upper edge and a lower edge, the perimeter of the upper edge of said second lower wall segment (14) being larger than the perimeter of the lower edge of said first upper wall segment (12); said lower edge of said first upper wall segment (12) and said upper edge of said second lower wall segment (14) being positioned proximate to each other and cooperating to provide an enlargement (34) of the cross-sectional area of the volume occupied by said particulate solid material; and the lower edge of said first upper segment (12) defining a plane forming an angle with respect to the vertical axis of the vessel.
    • 为了提供便宜的制造容器并且促进颗粒体材料通过其的均匀流​​动,建议容器(10)包括至少两个壁段(12,14),该壁段具有大致向下会聚的壁,其限定垂直 所述容器的轴线,垂直地布置在第二下部段(14)上方的第一上部段(12),每个所述壁段具有上边缘和下边缘,所述第二下部壁的上边缘的周边 段(14)大于所述第一上壁段(12)的下边缘的周边; 所述第一上壁段(12)的所述下边缘和所述第二下壁段(14)的所述上边缘彼此靠近定位并配合以提供所占体积的横截面面积的扩大(34) 通过所述颗粒状固体材料; 并且所述第一上部段(12)的下边缘限定相对于容器的垂直轴线形成一个角度的平面。
    • 10. 发明申请
    • METHOD AND APPARATUS FOR GASIFICATION OF ORGANIC MATERIALS
    • 有机材料气化方法与装置
    • WO1996040843A1
    • 1996-12-19
    • PCT/US1996009628
    • 1996-06-07
    • HYLSA S.A. DE C.V.PROLER ENVIRONMENTAL SERVICES, INC.
    • HYLSA S.A. DE C.V.PROLER ENVIRONMENTAL SERVICES, INC.BISHOP, Norman, G.VIRAMONTES-BROWN, Ricardo
    • C10J03/06
    • C10J3/002C10J3/06C10J3/14C10J3/66C10J2200/152C10J2200/158C10J2300/0959C10J2300/1223C10J2300/1621C10J2300/165C10J2300/1687C10J2300/1693C10K1/003C10K1/026C10K1/101
    • 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 & H2) 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 to about 800 DEG 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 CO2 and H2O derived from burner combustion of a fuel and oxygen-containing gas at a high flame temperature, typically 2500 to 3000 DEG C, (2) with excess oxygen, and/or (3) partially with H2O or CO2 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(具有主要含量的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)并控制为保持在这种回火状态 (通过调节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,并使复杂烃和通常与CO 2和H 2(H 2)逸出的气体反应 来自燃烧器和含氧气体的燃烧器燃烧,其在高火焰温度(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加入或存在于 , 费用。