Method and device for converting biomass into gaseous products
    1.
    发明授权
    Method and device for converting biomass into gaseous products 失效
    将生物质转化为气态产品的方法和装置

    公开(公告)号:US08361175B2

    公开(公告)日:2013-01-29

    申请号:US12522833

    申请日:2007-12-20

    摘要: A method for converting biomass having a water content of at least 50% into gaseous products includes providing a reactor containing supercritical water and a salt melt. The salt melt includes at least one of a salt and a salt mixture. The reactor and the salt melt are heated to the reaction temperature. The biomass is heated to a preheat temperature. The biomass heated to the preheat temperature is fed into the salt melt. The biomass is heated to the reaction temperature so as to commence a conversion of the biomass into the gaseous products, so as to release from the biomass at least one additional salt into the salt melt. An amount of the salt melt containing at least a portion of the at least one additional salt is withdrawn from the reactor and the amount of the withdrawn salt melt is replaced with a fresh salt solution. The gaseous products are removed from the reactor.

    摘要翻译: 将具有至少50%的含水量的生物质转化为气态产物的方法包括提供含有超临界水和盐熔体的反应器。 盐熔体包括盐和盐混合物中的至少一种。 将反应器和盐熔体加热至反应温度。 将生物质加热至预热温度。 将加热到预热温度的生物质加入到盐熔体中。 将生物质加热至反应温度,以便开始将生物质转化为气态产物,从而将生物质从至少一种另外的盐释放到盐熔体中。 将含有至少一部分至少一种另外的盐的盐熔体的量从反应器中取出,并且用新鲜盐溶液代替取出的盐熔体的量。 从反应器中除去气态产物。

    METHOD AND DEVICE FOR CONVERTING BIOMASS INTO GASEOUS PRODUCTS
    2.
    发明申请
    METHOD AND DEVICE FOR CONVERTING BIOMASS INTO GASEOUS PRODUCTS 失效
    将生物质转化为气体产品的方法和装置

    公开(公告)号:US20100037520A1

    公开(公告)日:2010-02-18

    申请号:US12522833

    申请日:2007-12-20

    IPC分类号: C10J3/00 C10J3/57

    摘要: A method for converting biomass having a water content of at least 50% into gaseous products includes providing a reactor containing supercritical water and a salt melt. The salt melt includes at least one of a salt and a salt mixture. The reactor and the salt melt are heated to the reaction temperature. The biomass is heated to a preheat temperature. The biomass heated to the preheat temperature is fed into the salt melt. The biomass is heated to the reaction temperature so as to commence a conversion of the biomass into the gaseous products, so as to release from the biomass at least one additional salt into the salt melt. An amount of the salt melt containing at least a portion of the at least one additional salt is withdrawn from the reactor and the amount of the withdrawn salt melt is replaced with a fresh salt solution. The gaseous products are removed from the reactor.

    摘要翻译: 将具有至少50%的含水量的生物质转化为气态产物的方法包括提供含有超临界水和盐熔体的反应器。 盐熔体包括盐和盐混合物中的至少一种。 将反应器和盐熔体加热至反应温度。 将生物质加热至预热温度。 将加热到预热温度的生物质加入到盐熔体中。 将生物质加热至反应温度,以便开始将生物质转化为气态产物,从而将生物质从至少一种另外的盐释放到盐熔体中。 将含有至少一部分至少一种另外的盐的盐熔体的量从反应器中取出,并且用新鲜盐溶液代替取出的盐熔体的量。 从反应器中除去气态产物。

    Method for purifying actinides which are in low oxidation states
    4.
    发明授权
    Method for purifying actinides which are in low oxidation states 失效
    纯化处于低氧化态的锕系元素的方法

    公开(公告)号:US4021313A

    公开(公告)日:1977-05-03

    申请号:US624106

    申请日:1975-10-20

    摘要: A method is provided for purifying actinides which are present in a low oxidation state in aqueous solution. The actinides are purified of fission products by extracting the actinides from aqueous solution while confining the fission products to the aqueous solution. The actinides that are purified are selected from the group of uranium (IV), neptunium (IV) and plutonium (III). An aqueous nitric acid solution containing the actinides, hydrazine nitrate or hydroxyl ammonium nitrate, as well as fission products is initially subjected to an electrolysis voltage. If Pu (III) is involved, the electrolysis voltage is below the voltage at which oxygen develops at the anode and anodically oxidizes the Pu (III) to Pu (IV). The Pu (IV) which is formed is transferred by means of an organic extraction agent from the aqueous solution to an organic phase. The organic phase is then separated and used for the plutonium recovery process. If U (IV) and/or Np (IV) are involved, the aqueous nitric acid solution is initially subjected to an electrolysis voltage in the vicinity of the voltage at which oxygen develops at the anode or higher to anodically oxidize the U (IV) to U (VI) and the Np (IV) to Np (VI). The U (VI) and/or Np (VI) which is formed is transferred by means of an organic extraction agent from the aqueous phase to the organic phase. The organic phase is then separated and used for the uranium or neptunium recovery process.

    摘要翻译: 提供了一种用于纯化在水溶液中以低氧化态存在的锕系元素的方法。 锕系元素通过从水溶液中提取锕系元素而将裂变产物限制在水溶液中来纯化裂变产物。 纯化的锕系选自铀(IV),ium(IV)和钚(III)。 含有锕系元素,硝酸肼或硝酸铵的硝酸水溶液以及裂变产物最初经受电解电压。 如果涉及Pu(III),则电解电压低于在阳极处产生氧气的电压,并将Pu(III)阳极氧化为Pu(IV)。 形成的Pu(IV)通过有机萃取剂从水溶液中转移到有机相中。 然后将有机相分离并用于钚回收过程。 如果涉及U(IV)和/或Np(IV),则硝酸水溶液最初经受在阳极或更高氧发生的电压附近的电解电压,以阳极氧化U(IV) 到U(VI)和Np(IV)到Np(VI)。 形成的U(VI)和/或Np(VI)通过有机萃取剂从水相转移到有机相中。 然后将有机相分离并用于铀或铀回收过程。

    Countercurrent extraction column for liquid-liquid extraction
    7.
    发明授权
    Countercurrent extraction column for liquid-liquid extraction 失效
    液 - 液萃取逆流萃取柱

    公开(公告)号:US4101408A

    公开(公告)日:1978-07-18

    申请号:US757062

    申请日:1976-12-30

    摘要: A countercurrent extraction column for a liquid-liquid extraction of two phases which are insoluble in each other with simultaneous electrolysis. The column comprises an outer tube, an inner tube within the outer tube, with the inner tube dividing the column into an inner anode chamber and an outer cathode chamber which encloses the anode chamber without the use of a diaphragm. A plurality of bores establish communication between the anode chamber and the cathode chamber. An anode is provided in the anode chamber and a cathode is provided in the cathode chamber. A hollow sheet metal cylinder is disposed around the inner tube in the area of the bores between the cathode chamber and the anode chamber. The cylinder acts as a cathode cylinder member and is chargeable in its interior by one of the phases through bores located at the top of the cathode cylinder. Sheet metal strips are attached in a radially inwardly extending manner to the interior surface of the cathode cylinder.

    摘要翻译: 一种用于液相萃取的逆流提取塔,两相不溶于同时电解。 该柱包括外管,外管内管,内管将柱分成内阳极室和外阳极室,其不使用隔膜而封闭阳极室。 多个孔在阳极室和阴极室之间建立连通。 阳极设置在阳极室中,阴极设置在阴极室中。 在阴极室和阳极室之间的孔的区域内围绕内管设置中空的金属板。 气缸用作阴极筒构件,并且可通过位于阴极筒顶部的孔之一通过其中一个相位将其内部充电。 钣金条以径向向内延伸的方式附接到阴极筒的内表面。