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    • 11. 发明授权
    • Dual temperature deuterium extraction process
    • 双温氘提取工艺
    • US4015944A
    • 1977-04-05
    • US533768
    • 1974-12-18
    • Gerard J. C. A. PauluisAlistair I. Miller
    • Gerard J. C. A. PauluisAlistair I. Miller
    • B01D59/33B01D59/22C01B4/00C01B5/02C01D11/00
    • C01B5/02B01D59/22
    • A dual temperature isotope exchange process of the type having a first stage comprising a hot and a cold tower with liquid and gas passing in countercurrent exchange relation therein, the gas being recycled from the top of the cold tower to the bottom of the hot tower via a humidifier section through which a liquid stream also passes, a dehumidifier between hot and cold towers through which both gas and liquid streams pass, the improvement comprising the feeding of the inlet feed liquid at a raised temperature to the top of the humidifier section that is, to a point between the liquid outlet of the hot tower and the liquid input to the humidifier and the recycling of a portion of the liquid leaving the hot tower to the top of the cold tower preferably via a cooling device.
    • 具有第一级的双温度同位素交换过程包括具有液体和气体在其中逆流交换关系的热塔和冷塔,所述气体从冷塔的顶部再循环到热塔的底部,经由 加湿器部分,液体流也通过该加湿器部分,气体和液体流通过的热塔和冷塔之间的除湿器,其改进包括将升温时的入口进料液体供给到加湿器部分的顶部, ,到热塔的液体出口和输入到加湿器的液体之间的点,以及一部分离开热塔的液体优选通过冷却装置再循环到冷塔的顶部。
    • 18. 发明授权
    • Purification of trona ores by conditioning with an oil-in-water emulsion
    • 通过用水包油乳液进行调理来净化天然碱矿石
    • US07517509B2
    • 2009-04-14
    • US11094326
    • 2005-03-30
    • J. D. MillerXuming WangMinhua Li
    • J. D. MillerXuming WangMinhua Li
    • C01D11/00
    • C01D7/00C22B1/00C22B26/10
    • The present invention is a trona concentrate and a process for floating gangue material from trona ore that comprises forming an emulsion, conditioning the trona ore at a high solids content in a saturated trona suspension, and then floating and removing the gangue material. The process for separating trona from gangue materials in trona ore can include emulsifying an oil in an aqueous solution to form an oil-in-water emulsion. A saturated trona suspension having a high solids content can also be formed having trona of a desired particle size. The undissolved trona in the saturated suspension can be conditioned by mixing the saturated suspension and the oil-in-water emulsion to form a conditioning solid suspension of trona and gangue material. A gas can be injected through the conditioning solid suspension to float the gangue material. Thus, the floated gangue material can be readily separated from the trona to form a purified trona concentrate without requirements of additional heat or other expensive processing steps.
    • 本发明是天然精浓缩物和用于从天然碱矿石中漂浮的ang石材料的方法,其包括形成乳液,以饱和的天然碱悬浮液中的高固体含量调节天然碱矿石,然后漂浮并除去脉石材料。 将天然碱与天然碱矿石中的脉石材料分离的方法可以包括在水溶液中乳化油以形成水包油乳液。 也可以形成具有高固体含量的饱和天然碱悬浮液,其具有所需粒径的天然碱。 可以通过混合饱和悬浮液和水包油乳液来调节饱和悬浮液中未溶解的天然碱,以形成天然碱和脉石材料的调理固体悬浮液。 可以通过调理固体悬浮液注入气体以漂浮ang石材料。 因此,漂浮的脉石材料可以容易地从天然碱分离以形成纯化的天然碱浓缩物,而不需要额外的热量或其它昂贵的加工步骤。
    • 20. 发明授权
    • Process for the preparation of perhydrates
    • 过程的制备过程
    • US3860694A
    • 1975-01-14
    • US28512572
    • 1972-08-31
    • DU PONT
    • JAYAWANT MADHUSUDAN D
    • C01B3/16C01B15/00C01B15/10C01B15/16C01B25/26C01B31/00C01D7/26C01D11/00C22B29/00
    • C01B15/103C01B3/16C01B15/00
    • A process for producing stable, particular perhydrates of sodium carbonate and phosphates comprising contacting the precursor of the perhydrate with concentrated hydrogen peroxide solution in such quantity as to develop the desired active oxygen content in the particles. The perhydrate is recovered by drying. Stabilizers may be present in the precursor or may be added prior to, with, or after hydrogen peroxide addition. The perhydrate may be agglomerated to meet end-use particle size requirements by contacting the particles with water, optionally containing an agglomerating agent or stabilizer. Reaction and perhydrate uniformity are achieved by balancing water content, reaction conditions, residence time under reaction conditions, and stabilizer content.
    • 一种生产稳定,特定的碳酸钠和磷酸盐过碳酸盐的方法,包括使过水合物的前体与浓缩的过氧化氢溶液接触,其量使颗粒中产生所需的活性氧含量。 通过干燥回收过水合物。 稳定剂可以存在于前体中,或者可以在添加过氧化氢之前,之后或之后加入。 通过使颗粒与水接触,任选地含有附聚剂或稳定剂,可将过水合物凝聚以满足最终用途的粒度要求。 通过平衡水含量,反应条件,在反应条件下的停留时间和稳定剂含量来实现反应和过水合物的均匀性。