METHOD FOR PURIFICATION OF AMMONIA, MIXTURES OF NITROGEN AND HYDROGEN, OR NITROGEN, HYDROGEN AND AMMONIA
    2.
    发明申请
    METHOD FOR PURIFICATION OF AMMONIA, MIXTURES OF NITROGEN AND HYDROGEN, OR NITROGEN, HYDROGEN AND AMMONIA 审中-公开
    硝酸铵,硝酸,氢,氮,氢和氨的混合物的纯化方法

    公开(公告)号:WO2013184012A1

    公开(公告)日:2013-12-12

    申请号:PCT/PL2013000075

    申请日:2013-06-07

    Abstract: Method for purification of ammonia or mixtures of nitrogen and hydrogen, or nitrogen, hydrogen and ammonia, according to which: a) ammonia or a mixture of gases under pressure of from 0.1 to 25 MPa is passed through a column packed with aluminium oxide with a large specific surface area; b) the ammonia or mixture of gases is then passed through a column packed with CaO, NaOH, KOH or an NaOH/KOH melt, separately or in a mixture, at 20 to 70°C and under pressure of from 0.1 to 25 MPa; c) next, the ammonia or mixture of gases is passed through a column packed with activated carbon having a specific area of 100÷3000 m2 /g with sodium, potassium, caesium, magnesium, calcium, strontium, barium or cerium nitrates(V) or nitrates(III) deposited on its surface, separately or in a mixture; the aforementioned steps being realised in a serial process at a gas stream flow rate in the range of 100 dm3/h to 1000 m3/h.

    Abstract translation: 纯化氨或氮气和氢气或氮气,氢气和氨的混合物的方法,其中:a)将氨或气体在0.1-25MPa压力下的混合物通过填充有氧化铝的柱, 大比表面积; b)然后在20至70℃和0.1至25MPa的压力下,氨或气体混合物分别或混合物中通过填充有CaO,NaOH,KOH或NaOH / KOH熔体的柱; c)接下来,将氨或气体混合物通过用钠,钾,铯,镁,钙,锶,钡或铈的硝酸盐(V)填充特定面积为100÷3000m 2 / g的活性炭的柱子, 或硝酸盐(III),分别或混合物沉积在其表面上; 上述步骤是以100dm 3 / h至1000m 3 / h范围内的气流流速在串联方法中实现的。

    BOILER HAVING AN INTEGRATED OXYGEN PRODUCING DEVICE
    3.
    发明申请
    BOILER HAVING AN INTEGRATED OXYGEN PRODUCING DEVICE 审中-公开
    具有一体化氧气生产装置的锅炉

    公开(公告)号:WO2009064539A2

    公开(公告)日:2009-05-22

    申请号:PCT/US2008/077593

    申请日:2008-09-25

    Abstract: A system provides a boiler (10) integrated with an oxygen producing device (12). Combustion heat generated in the boiler (10 is used to generate steam in the boiler and applied to at least one of a sweep gas stream (13) and a feed gas stream (15) to ensure sweep gas and feed gas streams (12, 15) are provided at the appropriate temperature to the oxygen producing device (12). Flue gas generated by fuel combustion within the combustion chamber (14) may be used as the sweep gas stream (13), in which case, the flue gas exiting the oxygen producing device (12) includes the oxygen removed from the feed gas stream. The flue gas/oxygen mixture may be used for fuel combustion within the combustion chamber, and may be provided to an oxygen separator (28) for removing oxygen from the flue gas. Sensible heat contained in the oxygen depleted feed gas from the oxygen producing device (12) may be recovered by the feed gas stream (15).

    Abstract translation: 系统提供与氧气产生装置(12)集成的锅炉(10)。 在锅炉中产生的燃烧热(10)用于在锅炉中产生蒸汽并施加到吹扫气流(13)和进料气流(15)中的至少一个,以确保吹扫气体和进料气体流(12,15 )在适当的温度下被提供给氧气产生装置(12),在燃烧室(14)内由燃料燃烧产生的烟气可用作吹扫气流(13),在这种情况下, 氧气生成装置(12)包括从进料气流中除去的氧气,烟道气/氧气混合物可用于燃烧室内的燃料燃烧,并且可以提供给用于从烟道中除去氧气的氧气分离器(28) 来自氧产生装置(12)的贫氧进料气中含有的显热可以通过原料气流(15)回收。

    PSA WITH ADSORBENTS SENSITIVE TO CONTAMINANTS
    8.
    发明申请
    PSA WITH ADSORBENTS SENSITIVE TO CONTAMINANTS 审中-公开
    PSA吸附剂对污染物敏感

    公开(公告)号:WO02047797A1

    公开(公告)日:2002-06-20

    申请号:PCT/US2001/048569

    申请日:2001-12-11

    Abstract: Disclosed embodiments address contaminant management challenges that arise during production of desirably contaminant free product fluid in the operation of PSA equipment, and further address the more serious challenges that arise under intermittent operation of PSA equipment. One embodiment includes a breather fluidly coupled to a feed end of an adsorber with a contaminant-sensitive adsorbent. The breather can be coupled to the feed end through a shutoff valve closed during production and open during shutdown. Other embodiments use particular sealing strategies for additional sealing of the apparatus, or at least components thereof, from contaminant ingress. For example, a buffer seal for receiving a buffer gas having a contaminant vapor content substantially the same as or less than a product gas produced by a pressure swing adsorption process over the adsorbers. As a second example, a parking seal can be used that typically is engaged when the apparatus is parked.

    Abstract translation: 公开的实施例解决了在PSA设备的操作中生产期望的无污染物质流体期间产生的污染物管理挑战,并且进一步解决了在PSA设备的间歇操作下出现的更严重的挑战。 一个实施例包括与污染物敏感的吸附剂流体耦合到吸附器的进料端的通气孔。 呼吸器可以通过在生产期间关闭的截止阀与关闭时关闭时打开相连接。 其他实施例使用特定的密封策略来附加地密封设备,或至少其组件,以免污染物进入。 例如,用于接收缓冲气体的缓冲密封件,该缓冲气体的污染物蒸汽含量基本上等于或小于通过吸附器上的变压吸附过程产生的产物气体。 作为第二示例,可以使用通常在设备停放时接合的停车密封件。

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