NOx SENSOR ASSEMBLY
    3.
    发明申请
    NOx SENSOR ASSEMBLY 审中-公开
    NOx传感器总成

    公开(公告)号:WO1991019975A1

    公开(公告)日:1991-12-26

    申请号:PCT/US1991004177

    申请日:1991-06-12

    CPC classification number: G01N33/0037 F02B1/04 G01N25/30 Y02A50/245

    Abstract: This invention is a self-contained NOx sensor assembly. It may be used to detect NOx levels in a flowing gas stream such as might be found in an exhaust gas from a combustion process and to produce a measurable electrical output related to the content of NOx measured. The NOx sensor assembly is of a configuration that may be detached from a mounting and replaced. The sensor assembly comprises two sensor elements one of which is made up of a catalyst on a temperature measuring device. The other is a gas stream ambient temperature measuring device. The catalyst is selected and configured so that it selectively reduces NOx and the resulting heat of the reaction raises the temperature of the allied temperature measuring device. The sensor assembly also contains a NOx reductant source. The sensor assembly may be placed in a moving vehicle for measuring NOx levels in its exhaust gas.

    Abstract translation: 本发明是一种独立的NOx传感器组件。 它可以用于检测流动气流中的NOx水平,例如可能在来自燃烧过程的废气中发现,并且产生与所测量的NOx含量相关的可测量的电输出。 NOx传感器组件具有可以从安装和拆卸的构造。 传感器组件包括两个传感器元件,其中一个传感器元件由温度测量装置上的催化剂构成。 另一种是气流环境温度测量装置。 催化剂的选择和配置使得其选择性地还原NOx,并且所产生的反应热量升高了相关温度测量装置的温度。 传感器组件还含有NO x还原剂源。 传感器组件可以放置在移动的车辆中,用于测量其废气中的NOx水平。

    PALLADIUM PARTIAL COMBUSTION CATALYSTS AND A PROCESS FOR USING THEM
    4.
    发明申请
    PALLADIUM PARTIAL COMBUSTION CATALYSTS AND A PROCESS FOR USING THEM 审中-公开
    气体部分燃烧催化剂及其使用方法

    公开(公告)号:WO1992009848A1

    公开(公告)日:1992-06-11

    申请号:PCT/US1991008918

    申请日:1991-11-26

    Abstract: This invention is a catalyst comprising palladium on a support (102) and a partial combustion process in which the fuel is partially combusted using that catalyst. The palladium catalyst (106) may also comprise palladium mixed with metals selected from Group VIII or IB, may be graded (Fig. 1b) such as to have higher activity in the forward edge (112) of the catalyst, or may be placed on a support comprising zirconia. The choice of catalysts (106) and supports (102, 110) specified each solves a variety of problems dealing with the long term stability of the palladium as a partial combustion catalyst. The catalyst structure is stable in operation, has a comparatively low operating temperature, has a low temperature at which oxidation begins, and yet is not susceptible to temperature "runaway". The combustion gas produced by the catalytic process typically is at a temperature below the autocombustive temperature and may be used at that temperature or it may be fed to other combustion stages for further use in a gas turbine, furnace, boiler, or the like.

    Abstract translation: 本发明是一种催化剂,其包含在载体(102)上的钯和部分燃烧方法,其中燃料使用该催化剂部分燃烧。 钯催化剂(106)还可以包含与选自VIII或IB族的金属混合的钯,其可以分级(图1b),例如在催化剂的前沿(112)中具有较高的活性,或者可以放置在 包含氧化锆的载体。 催化剂(106)和载体(102,110)的选择各自解决了作为部分燃烧催化剂的钯的长期稳定性的各种问题。 催化剂结构在运行中稳定,工作温度较低,氧化开始时温度低,但不易受温度“溢流”影响。 通过催化过程产生的燃烧气体通常处于低于自燃温度的温度,并且可以在该温度下使用,或者可以将其供给到其他燃烧级,以进一步用于燃气轮机,炉,锅炉等。

    PROCESS FOR PRODUCING BROMINE FROM SEAWATER
    8.
    发明申请
    PROCESS FOR PRODUCING BROMINE FROM SEAWATER 审中-公开
    从海水生产溴的方法

    公开(公告)号:WO1993006038A1

    公开(公告)日:1993-04-01

    申请号:PCT/US1992007822

    申请日:1992-09-16

    CPC classification number: B01J27/122 C01B7/096

    Abstract: This invention is a combination process for producing elemental bromine using a seawater feed. The process involves a series of steps in which seawater is acidified, chlorinated, and air stripped to remove the bromine. The stripping effluent is reacted with an SO2 stream to convert the bromine to hydrogen bromine and H2SO4 in the air stream. The process continues by absorbing hydrogen bromide and H2SO4 from the resulting acidic fog to produce an aqueous H2SO4 stream containing HBr. The HBr is stripped from the liquid stream and passed to an oxidation reactor where it is catalytically oxidized with an oxygen-containing gas to produce a stream of Br2 and H2O. The hot reactor effluent is quenched and the product Br2 is separated from the H2O and inert gases such as air. In the figure 2 seawater enters pipeline (202) and is mixed with an H2SO4 stream (200). The resulting stream (214) is sent to a stripping column (218) where air stream (216) strips the bromine from the liquid. The vapor B22 stream (222) is mixed with SO2 (224) which is contacted with a water stream. The resulting aqueous H2SO4/HBr stream (236) is heated and mixed with a chlorine stream (240). A portion of the chlorine is introduced through line (241) to the bottom of stripping column (242) and separates with stream (244) into stream (246) containing H2O4 and HCl separates with stream (244) into stream (246) containing H2SO4 and HCl and stream (248) containing Br2. The Br2 product (260) is discharged from decanter (254) into the purification unit (255).

    Abstract translation: 本发明是使用海水进料生产元素溴的组合方法。 该方法涉及一系列步骤,其中将海水酸化,氯化和空气汽提以除去溴。 汽提流出物与SO 2流反应,将溴转化为氢气中的溴和H2SO4。 该过程通过从所得酸雾吸收溴化氢和H 2 SO 4继续以产生含有HBr的H 2 SO 4水流。 将HBr从液体物流中汽提出并通入氧化反应器,在其中用含氧气体催化氧化,产生Br 2和H 2流。 将热反应器流出物淬灭并将产物Br 2从H 2 O和惰性气体如空气中分离出来。 在图2中,海水进入管道(202)并与H 2 SO 4流(200)混合。 将所得流(214)送至汽提塔(218),其中空气流(216)从液体中分离出溴。 蒸汽B22流(222)与与水流接触的SO 2(224)混合。 将所得H 2 SO 4 / HBr水溶液(236)加热并与氯气流(240)混合。 一部分氯通过管线(241)引入汽提塔(242)的底部,并用料流(244)分离成包含H 2 O 4的HCl(245)和用流(244)分离的HCl(包含H 2 SO 4)的料流(246) 和HCl和含有Br 2的物流(248)。 Br2产物(260)从滗析器(254)排出到净化单元(255)中。

    CATALYTIC PROCESS FOR CONVERTING HYDROCARBONACEOUS FEEDS, PARTICULARLY LOWER ALKANES TO ESTERS, ALCOHOLS, AND OPTIONALLY TO HYDROCARBONS
    9.
    发明申请
    CATALYTIC PROCESS FOR CONVERTING HYDROCARBONACEOUS FEEDS, PARTICULARLY LOWER ALKANES TO ESTERS, ALCOHOLS, AND OPTIONALLY TO HYDROCARBONS 审中-公开
    用于转化碳氢化合物的催化过程,特别是下降到酯,醇和有选择性的烃类

    公开(公告)号:WO1992014738A1

    公开(公告)日:1992-09-03

    申请号:PCT/US1992001272

    申请日:1992-02-14

    Inventor: CATALYTICA, INC.

    Abstract: This invention is a process for converting hydrocarbonaceous feeds, particularly lower alkanes, into their corresponding esters and optionally into various intermediates (such as alcohols) and optionally into liquid hydrocarbons. The hydrocarbonaceous feeds are oxidatively converted to oxy-esters at high selectivity and conversion and at practical reaction rates using at least catalytic amounts of certain class "B" metals and/or metal ions defined by the Pearson definition as "soft" or "borderline". Desirable catalysts comprise such metals as Pd, Tl, Pt, Hg, and Au. Mercury is most desired. If so desired, the oxy-esters may be converted to alcohols or other intermediates such as halides. The oxy-esters, alcohols, and other intermediates may optionally be converted to liquid hydrocarbons such as gasoline.

    Abstract translation: 本发明是将烃类进料,特别是低级烷烃转化成其相应的酯,任选地转化为各种中间体(如醇)和任选地转化成液体烃的方法。 烃类进料以高选择性和转化率,以实际的反应速率,以至少催化量的由“Pearson”定义的“B”族金属和/或金属离子为“软”或“边界” 。 理想的催化剂包括诸如Pd,Tl,Pt,Hg和Au的金属。 汞是最需要的。 如果需要,可将氧酯转化为醇或其它中间体如卤化物。 氧酯,醇和其它中间体可以任选地转化成液体烃如汽油。

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