• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Organic reagents e.g., diethyl ether; 75% vol. of tributyl phosphate (TBP) in light oil etc., may be used to extract monobasic acids e.g., HNO3 and metals from waste waters or byproduct solns. e.g., from pickling baths. Recovery of these products is by formation of adducts with the organic reagent and removal by washing and (for metals) by precipitation methods. The presence of at least equiv. amounts of H2SO4 and metal ions is necessary, the acid being added where necessary to achieve this condition. Very high recovery (up to 99%) of monobasic acids is possible and the process may also be applied to the extraction of metals from low grade ore leachings.
    公开号:SU862819A3
    申请号:SU731879421
    申请日:1973-01-24
    公开日:1981-09-07
    发明作者:Лильенцин Ян-Олов；Рейнгардт Ганс；Ян Арнольд Ридберг Хельге
    申请人:Стора Коппарбергс Бергслагс Актиеболаг (Фирма)；
    IPC主号:
    专利说明:

    (54) METHOD FOR REMOVAL OF MONOVALENT INORGANIC ACIDS FROM WATER
    The invention relates to a method by which monovalent inorganic acids can be removed from an aqueous solution containing metal salts of acids using liquid extraction. This invention can also be used to treat various industrial wastewaters, such as pickling baths, as well as for hydrometallurgical processes.,
    , In industrial form many liquid effluents are one-way solution; containing metal salts of acids.
    In such cases, when such industrial effluents contain mainly sulphates or sulfuric acid, rather effective methods are used to extract metals from solutions: However, if these liquid effluents contain larger or smaller amounts of monovalent inorganic acids, especially nitric acid or halogen acid, or their salt, there are significant problems due to the harmfulness of these compounds (for example, nitric acid, fluorides, nitrates), their corrosivity (for example, chlorides), or because of the difficulties associated with Kisg extract SOLUTION
    lot or metals (for example, hydrofluoric acid is a compound that is extremely difficult to precipitate with many metals) ..
    The closest to the technical essence is the method of removing monovalent acids (for example, HNOa) from an aqueous solution by extracting an organic phase (tributyl phosphate in kerosene), which is not miscible with the solution and forms adducts with monovalent acids, followed by separation
    10 organic and aqueous FB and the release of monovalent inorganic acids 1.
    In order to increase the degree of removal and the possibility of removing monovalent acids from solutions of their salts, sulfuric acid is introduced into the solution.
    15 acid in an amount equivalent to the content of metal ions in a strainer.
    Addition of Hj SO4 to the treated solution before extraction is significantly improved by the selectivity of the monovalent extractable
    20 acids and metals. In the absence of HjSO4, the extracted acid fraction contains almost 8 times more Fe and Ni and 5 times more Cr than the corresponding acid fraction when HjSO is added.
    25 Comparative data is given in Table. 1. Monovalent inorganic acids, mainly nitric acid and halogen acid, are removed from the aqueous solution of the metal salts of these acids as follows. The content of sulfuric acid in the solution is set so that it is at least equivalent to the content of metal ions in the solution, after which the movalent inorganic acids are extracted by bringing the solution into contact with the organic phase containing the compounds forming aaductes with monovalent acids. The aqueous solution may contain water-soluble salts of one or more monovalent acids and one or more metal ions, starting with alkali metal liOHoB to heavy metal ions. If the solution contains strong oxidizing agents, for example chromic acid, chlorine or chlorine oxides, then it may be desirable to restore them before extraquids. The organic phase consists of a diluent and an adduct forming agent. It must have a high separation ratio of monovalent HX acids relative to sulfuric acid and metal ions. The separation factor is the ratio between the distribution coefficients D of the organic and aqueous phase of the corresponding medium. The organic phases suitable for the extraction of monovalent acids are given in table. During the extraction, an adduct is formed in the form of the organic phase in accordance with the reactions Nve% zx - b (z / 2) HiS04 (g / g) MX Q z HXQCopr-V where X is a halogen ion or a nitrate ion in the aqueous phase; organic phase, (org.) adduct formed in the organic phase. There is no universal agent forming adducts of monovalent acids C, therefore the composition of the organic phase is determined by the composition of the solution being treated. Along with monovalent acids, some inorganic acids, such as phosphoric and boron, can be extracted into the organic phase. In some, certain heavy metals, such as molybdenum and tungsten, also show a tendency to transition into the organic phase. The method of extracting monovalent inorganic acids from an aqueous solution is recovered in conventional apparatus used for the extraction of liquids. The contact between phases 94 is carried out in a mixer, after which the phases are separated in a separate apparatus. Extraction is conveniently carried out in several stages, while ensuring backflow between the phases. It is desirable to cleave the resulting adduct in the organic extract obtained by extraction, and thus regenerate the organic phase for reuse. Many different ways of accomplishing this type of cleavage are known. For example, acids can be leached in the form of metal salts, using alkalis. After extraction, the organic phase and the aqueous solution are treated separately by known methods. Example. The pickling bath used to pickle stainless steel has the following composition: HN03 - 150 g / l; HF - 30 g / l; Fe - Dfg / l; .CN-- 4.8 g / l; 5 g / l; Mo -1,2g / l. H2SO4 is added in an amount of 54 g / l. This amount is equivalent to the metal content in the solution. The etching bath is cooled to normal temperature, the extraction is carried out. is by means of an organic phase consisting of 25% kerosene and 75% tributyl phosphate. Nitric acid, hydrofluoric acid, molybdenum are transferred to the orthanic phase. The acids in the organic phase are extracted with water and revolved into the pickling bath. Any remaining Hbie amounts of acids in the organic and molybdenum are extracted with sodium hydroxide solution, and the iron metals precipitate as hydroxides, which are regenerated as starting materials. PRI mme R 2. Sulfide ore with a content of 20.6% copper is leached with an acid mixture containing 6 mol per liter of nitric acid and 4.5 mol per liter of sulfuric acid. The resulting nitrogen gases are oxidized and recycled as nitric acid. The leach solution contains 18.4 g / l of copper, 2.1 g / l of iron and 147 g / l of nitric acid, together with sulfuric acid, obtained from both added acid and from oxidized sulfide sulfur. The perfecting solution is extracted with an organic phase containing 25% kerosene and 75% tributyl phosphate. The organic phase removes 99.9% nitric acid, which is regenerated from the organic phase by leaching and recycled during the process. After extraction, the leach solution consists of a solution of sulfuric acid containing 25.5 g / l of copper, 2.9 g / l of iron and only 0.05 g / l of nitric acid. Copper can be extracted from the solution selectively by extraction with an organic reagent using a known method.
    With addition 1 {N2804, mg metal / l
    Without adding Hg8O4
    Fe G Mi I Cr
    3.3
    0.9
    Q.4
    100% 1M HjSO
    gek dream
    100% 6M H2SO4
    diethyl eff
    Formula and a o b p t
    A method for removing monovaleic i-orotanic acids from an aqueous solution, comprising extracting the organic liquid phase, mixing the rie with the solution and forming adducts with monovalent acids, followed by separating the organic and aqueous phases and isolating the monovalent inorganic acids, characterized by that.
    HF
    HCIOD. 4.io- (C 10)
    THAT, with a chain of increase in the degree of removal and the possibility of removing monovalent acids from the pactBOtioB of their salts, sulfuric acid is introduced into the aqueous solution in an amount equivalent to the content of metal ions in the solution.
    Historical forms taken into account during the examination 1. Journal of Organic Chemistry, Vol. 5, N 6, 1960, p. 1337.
    权利要求:
    Claims (1)
    [1]
    Claim
    A method for removing monovalent inorganic acids from an aqueous solution, including extraction with an organic liquid phase that is not miscible with the solution and forming adducts with monovalent acids, followed by separation of the organic and aqueous phases and the isolation of monovalent inorganic acids, characterized in that, in order to increase the degree of removal and the possibility of removing monovalent acids from solutions of their salts, sulfuric acid is introduced into the aqueous solution in an amount equivalent to the content of metal ions in the solution.
    类似技术:
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    同族专利:
    公开号 | 公开日
    FR2169167B1|1977-02-04|
    DE2302563A1|1973-08-02|
    IT988104B|1975-04-10|
    FR2169167A1|1973-09-07|
    DE2302563C3|1981-07-16|
    SE364187B|1974-02-18|
    CA998841A|1976-10-26|
    DE2302563B2|1980-09-25|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    WO2014137237A1|2013-03-05|2014-09-12|Opened Joint Stock Company "United Chemical Company Uralchem"|A method for purification of circulating leaching solutions from phosphates and fluorides|
    US9631258B2|2013-03-05|2017-04-25|Opened Joint Stock Company “United Chemical Company Uralchem”|Methods for extracting rare-earth metals and preparing gypsum plaster from phosphogypsum hemihydrate|
    US9657371B2|2013-03-05|2017-05-23|Opened Joint-Stock Company “United Chemical Company Uralchem”|Methods for extracting rare-earth metals and preparing gypsum plaster from phosphogypsum hemihydrate|
    US10011891B2|2013-03-18|2018-07-03|Open Joint-Stock Company “United Chemical Company Uralchem”|Methods for concentrating rare-earth metals in phosphogypsum and removing thereof from wet process phosphoric acid|US3186809A|1961-08-10|1965-06-01|Gen Mills Inc|Extraction of mineral acids using dodecylphenol|
    FR1417037A|1964-12-09|1965-11-05|Continuous regeneration of hydrochloric acid|
    GB1142719A|1968-10-24|1969-02-12|Israel Mining Ind Inst For Res|Phosphoric acid recovery|AU501823B2|1975-03-14|1979-06-28|Solex Research Corporation Of Japan|Removing heavy metals froman acid waste liquid|
    US4113588A|1976-03-09|1978-09-12|Solex Research Corporation Of Japan|Process for recovery of waste H2 SO4 and HCl|
    FR2391953B1|1976-11-02|1979-08-17|Ugine Kuhlmann|
    AT370449B|1981-02-10|1983-03-25|Ruthner Industrieanlagen Ag|METHOD FOR TREATING USED TREATMENT LIQUIDS CONTAINING IRON ION OR LIQUID LIQUIDS FOR METAL MATERIALS OR ORES BY LIQUID-LIQUID EXTRACTION|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE76072A|SE364187B|1972-01-24|1972-01-24|
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