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    • 42. 发明授权
    • Process for separating arsenic acid from an aqueous mixture comprising
sulfuric and arsenic acids
    • 从含有硫酸和砷酸的含水混合物中分离砷酸的方法
    • US5449503A
    • 1995-09-12
    • US296983
    • 1994-08-26
    • Charles L. RedmonSomanahalli N. SubbannaRobert A. Smith
    • Charles L. RedmonSomanahalli N. SubbannaRobert A. Smith
    • C01B17/90C01G28/00C01B9/08C22B30/00
    • C01G28/005C01B17/907
    • The present invention provides a process for recovering arsenic acid from a starting mixture comprising sulfuric and arsenic acids and water. In step (a), the starting mixture is treated with a sulfur (IV) compound which will reduce the arsenic acid to arsenic (III) compound under conditions sufficient to substantially convert the arsenic acid to arsenic (III) wherein the resulting mixture comprises arsenic (III) compound, the sulfur (IV) compound, sulfuric acid, and water. In step (b), the resulting mixture is purged with gas to substantially remove the sulfur (IV) compound from the mixture wherein the purged mixture comprises the arsenic (III) compounds, sulfuric acid, and water. In step (c), the purged mixture is treated under conditions sufficient to substantially separate the arsenic (III) compounds from the purged mixture. In step (d), the separated arsenic (III) compound is reacted with an oxidizing agent to substantially convert arsenic (III) compound to arsenic acid wherein the final mixture comprises arsenic acid, unreacted oxidizing agent, and water. In step (e), impurities are removed from the final mixture to provide substantially pure aqueous arsenic acid.
    • 本发明提供从包含硫酸和砷酸和水的起始混合物中回收砷酸的方法。 在步骤(a)中,起始混合物用硫(IV)化合物处理,该化合物在足以将砷酸基本转化成砷(III)的条件下将砷酸还原为砷(III)化合物,其中所得混合物包含砷 (III)化合物,硫(IV)化合物,硫酸和水。 在步骤(b)中,将所得混合物用气体吹扫以从混合物中基本上除去硫(IV)化合物,其中清除的混合物包含砷(III)化合物,硫酸和水。 在步骤(c)中,将清洗的混合物在足以使砷(III)化合物与被清除的混合物基本分离的条件下进行处理。 在步骤(d)中,分离的砷(III)化合物与氧化剂反应,以将砷(III)化合物基本上转化为砷酸,其中最终混合物包含砷酸,未反应的氧化剂和水。 在步骤(e)中,从最终混合物中除去杂质以提供基本上纯的砷酸水溶液。
    • 43. 发明授权
    • Process for converting hexafluoroarsenic acid or any salt thereof to
arsenic acid or salt thereof which can then be rendered nonhazardous
    • 将六氟砷酸或其盐转化成砷酸或其盐,然后可以使其成为非危险的方法
    • US5089241A
    • 1992-02-18
    • US633652
    • 1990-12-20
    • Robert A. SmithDouglas G. FrickCharles L. RedmonSomanahalli N. Subbanna
    • Robert A. SmithDouglas G. FrickCharles L. RedmonSomanahalli N. Subbanna
    • A62D3/00A62D3/34A62D3/35A62D3/36A62D101/22A62D101/43A62D101/49
    • A62D3/35C01B7/195C01G28/005A62D2101/43A62D2101/49
    • The present invention provides a process for the conversion of hazardous hexafluoroarsenic acid or any salt thereof to arsenic acid or salt thereof which can be rendered nonhazardous. In particular, the hexafluoroarsenic acid or salt is converted to arsenic acid or salt which can be converted to a water insoluble salt. Known insolubilization and stabilization technology then renders the material nonhazardous.The present process involves converting hexafluoroarsenic acid or salt thereof contained in an aqueous mixture to arsenic acid or salt thereof. The process comprises the steps of: (a) adding acid selected from the group consisting of sulfuric acid, arsenic acid, perchloric acid, and mixtures thereof to the aqueous mixture in an amount sufficient to catalyze the hydrolysis of the hexafluoroarsenic acid or salt thereof and raising the temperature of the aqueous mixture before, during, or after the acid addition sufficient to remove substantially all of the hydrogen fluoride in subsequent step (b); (b) passing an inert gas through the heated acid mixture steam in a quantity sufficient to remove substantially all of the hydrogen fluoride in the heated acid mixture from the heated acid mixture; and (c) separating substantially all of the hydrogen fluoride from the heated acid mixture whereupon the hexafluoroarsenic acid or salt thereof converts substantially to arsenic acid or salt thereof.
    • 本发明提供了将危险的六氟砷酸或其盐转化成可以变得不危险的砷酸或其盐的方法。 特别地,将六氟砷酸或盐转化为可转化为水不溶性盐的砷酸或盐。 已知的不溶化和稳定化技术使材料无害化。 本方法涉及将含水混合物中所含的六氟砷酸或其盐转化为砷酸或其盐。 该方法包括以下步骤:(a)以足以催化六氟砷酸或其盐的水解的量向该含水混合物中加入选自硫酸,砷酸,高氯酸及其混合物的酸,以及 在酸加入之前,期间或之后提高含水混合物的温度,足以在随后的步骤(b)中除去基本上所有的氟化氢; (b)使惰性气体通过加热的酸性混合物蒸汽,其量足以从加热的酸混合物中除去加热的酸混合物中的基本上所有的氟化氢; 和(c)从加热的酸混合物中基本上分离所有氟化氢,因此六氟砷酸或其盐基本上转化为砷酸或其盐。
    • 48. 发明授权
    • Process for extracting arsenic from oxidic materials
    • 从氧化材料中提取砷的方法
    • US4218425A
    • 1980-08-19
    • US920604
    • 1978-06-29
    • Thomas L. CharltonRobert F. Redden
    • Thomas L. CharltonRobert F. Redden
    • C01G28/00C22B30/04C01B27/02
    • C22B30/04C01G28/005C01P2006/80Y02P10/234
    • A process is disclosed for the selective extraction of arsenic from oxidic materials containing compounds such as arsenic trioxide, arsenic pentoxide, antimony trioxide, antimony pentoxide, antimony tetroxide and mixtures thereof in which arsenic is effectively separated from antimony. Said oxidic materials are subjected to a leach with a lixiviant containing arsenic acid or hydrogen peroxide at a temperature in the range of 40.degree. C. to the boiling point of the reaction mixture, preferably in the range of 80.degree. to 100.degree. C., for 5 to 90 minutes. The leach solution containing arsenic oxides is separated from leach residue. The leach solution is either cooled to a temperature in the range of 5.degree. to 25.degree. C. to crystallize and subsequently recover arsenic trioxide or the solution is oxidized and evaporated and arsenic pentoxide is recovered. Arsenic acid lixiviant contains 5 to 500 g/l arsenic as arsenic pentoxide, preferably 25 to 200 g/l, and hydrogen peroxide lixiviant preferably contains a 10 to 60% hydrogen peroxide concentration.
    • 公开了从含有三氧化二砷,五氧化二锑,三氧化锑,五氧化二锑,四氧化锑及其混合物的化合物的氧化物质中选择性提取砷的方法,其中砷与锑有效分离。 所述氧化物质在含有砷酸或过氧化氢的浸液中在40℃至反应混合物的沸点,优选在80℃至100℃的范围内进行浸提, 5至90分钟。 含有氧化砷的浸出溶液与浸出残渣分离。 将浸出溶液冷却至5〜25℃的温度,结晶并随后回收三氧化二砷或溶液氧化并蒸发,回收五氧化二砷。 砷酸浸剂含有5〜500g / l的砷作为五氧化二砷,优选为25〜200g / l,过氧化氢浸泡剂优选含有10〜60%的过氧化氢浓度。