INDIRECT HEAT EXCHANGER
    1.
    发明申请
    INDIRECT HEAT EXCHANGER 审中-公开
    间接热交换器

    公开(公告)号:US20090298002A1

    公开(公告)日:2009-12-03

    申请号:US11719823

    申请日:2005-11-14

    CPC classification number: F27D17/004 C03B5/235 F28D15/00 F28F1/003

    Abstract: The invention concerns a heat exchanger (4) for a combustion oven, said exchanger comprising a heat exchanging zone (2) provided with means for the passage of hot fumes derived from a burner of the oven, said zone being traversed by at least one means (1a) for transporting a combustion gas to be heated from a combustion gas source, via the heat exchanging zone and to the oven burner, said means (1a) being provided with a wall (1b) designed to enable the combustion gas to be heated by thermal energy transfer, said means (1a) for transporting the combustion gas being arranged in the heat exchanging zone in means (3a) capable of containing an inert gas and provided with a wall (3b) designed to enable the inert gas to be heated by thermal energy transfer of said hot fumes.

    Abstract translation: 本发明涉及一种用于燃烧炉的热交换器(4),所述交换器包括一个热交换区(2),该热交换区设置有用于通过来自烤箱燃烧器的热烟的装置,所述区被至少一个装置 (1a),用于通过所述热交换区和所述烘箱燃烧器将待加热的燃烧气体从燃烧气体源运送到所述炉燃烧器,所述装置(1a)设置有壁(1b),所述壁被设计成使得燃烧气体能够被加热 通过热能传递,所述用于输送燃烧气体的装置(1a)被布置在能够容纳惰性气体并且设置有壁(3b)的装置(3a)中的热交换区中,该壁设计成能够使惰性气体被加热 通过所述热烟的热能传递。

    Method for melting a composition of raw materials with an arched burner
    4.
    发明授权
    Method for melting a composition of raw materials with an arched burner 有权
    用拱形燃烧器熔化原料组合物的方法

    公开(公告)号:US08256245B2

    公开(公告)日:2012-09-04

    申请号:US11721191

    申请日:2005-11-21

    Abstract: The invention concerns a method for melting a composition of raw materials including introducing the composition in an oven to form a layer (2) at the surface of the molten pool (4). An oxycombustion burner (10) is arranged above the pool and directed towards the composition layer (2) to produce a melting front (3). Parameters of the burner are adjusted to produce a large covering flame (12) causing an essentially radiation-based thermal transfer. Additionally, a plane containing a longitudinal section of the flame (Z-Z) and a horizontal direction perpendicular to the axis of the oven (X-X) intersects the melting front (3) at a height (h) included ranging between one third and half of the thickness of the composition (e). Such a method provides for a stable operation of the oven and is particularly adapted to a large-capacity oven.

    Abstract translation: 本发明涉及一种用于熔化原料组合物的方法,包括将组合物引入烘箱中以在熔池(4)的表面形成层(2)。 一个氧化燃烧器(10)设置在池的上方并被引向组合物层(2)以产生熔融前沿(3)。 燃烧器的参数被调节以产生大的覆盖火焰(12),从而导致基本上基于辐射的热传递。 此外,包含火焰(ZZ)的纵向截面和垂直于烤箱(XX)的轴线的水平方向的平面在熔化前沿(3)处相交,高度(h)包括范围在三分之一 组合物(e)的厚度。 这种方法提供了烤箱的稳定操作,并且特别适用于大容量烘箱。

    Burner and method for partly oxidising a gas stream comprising hydrogen sulphide and ammonia
    6.
    发明授权
    Burner and method for partly oxidising a gas stream comprising hydrogen sulphide and ammonia 有权
    用于部分氧化包含硫化氢和氨的气流的燃烧器和方法

    公开(公告)号:US06890498B2

    公开(公告)日:2005-05-10

    申请号:US10415919

    申请日:2001-10-29

    CPC classification number: F23D14/22 C01B17/0417 F23D2900/00006

    Abstract: A gas burner for use with a Claus furnace made up of at least five concentric tubes and the spaces formed between them. The diameters of the tubes increase radially outward so that the first tube has a smaller diameter than the fifth tube. At the end of the burner closest to the furnace, the tube ends of the third, fourth, and fifth tubes lie in the same plane. The first and the second tubes are fastened together and capable of movement along the central longitudinal axis of the burner, but their ends closest the furnace are not capable of moving past the plane formed by the third, fourth, and fifth tubes. An injector is located between the first and second tubes at the end closest the furnace. The injector is oriented towards the periphery of the burner.

    Abstract translation: 一种用于与由至少五个同心管组成的克劳斯特炉和它们之间形成的空间的气体燃烧器。 管的直径径向向外增加,使得第一管具有比第五管小的直径。 在最接近炉子的燃烧器的末端,第三,第四和第五管的管端在同一平面内。 第一和第二管被紧固在一起并且能够沿着燃烧器的中心纵向轴线移动,但是其最靠近炉子的端部不能移动经过由第三,第四和第五管形成的平面。 喷射器位于最靠近炉子的一端处于第一和第二管之间。 喷射器朝向燃烧器的周边。

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