Method of alunite processing

专利摘要:
An improvement in processes for recovering aluminum from alunite ore which processes include roasting the ore to remove water of hydration, removing sulfur and potassium compounds from the roasted ore by a procedure including a final leaching step resulting in a residue and a solution containing potassium sulfate, effecting partial recovery of potassium sulfate from the solution by crystallization with some potassium sulfate being bled off from the mother liquor, converting aluminum values in the residue to alkali metal aluminates by digesting the residue with alkali metal hydroxide including a substantial amount of sodium hydroxide, removing silicon from the alkali metal aluminates leaving a waste desilication product, recovering aluminum values from the desilicated aluminates by precipitation, circulating the mother liquor from the precipitation step to digestion as contaminated sodium hydroxide is bled off, the improvement which comprises enhancing the economics of the overall process by introducing therein an ion exchange procedure in which potassium hydroxide for the first leaching step is produced through ion exchange by use of potassium sulfate and sodium hydroxide, a further improvement being the use of the desilication product as the ion exchange agent.
公开号:SU858555A3
申请号:SU792368804D
申请日:1979-01-08
公开日:1981-08-23
发明作者:Джо Хартман Джордж；Ричард Ивинг Вернон
申请人:Саутвайр Компани Нэшнл Стил Корпорейшн И Эрт Сайенсис Инк (Фирма)；
IPC主号:

专利说明:

The invention relates to non-ferrous metallurgy and can be used in the processing of alunite. A method of processing alunite is known, including dehydrating calcination, three-stage leaching of calcined alunite, crystallization of potassium sulphate from the first extrusion solution, separation of the mother liquor from potassium sulfate crystals f crystallization solution after the second leaching stage, separation of the solid residue containing atomic sodium silicate the thief, the release of aluminum hydroxide from the both-solution of the solution with the production of uterine pfCTBOpa sodium hydroxide PC However, the efficiency of the known method low, as it does not imply the use of by-products (potassium sulfate and the residue obtained at the stage of silification). The purpose of the invention is to increase the efficiency of the process. The goal is achieved by the method of alunite processing, including dehydrating roasting, two-more calcination, crystallization of kssi sulfate from the solution of the first leaching stage, separation of the uterine solution from potassium sulfate crystals, desiliconization of the solution after the second leaching stage, separation of the residue, the area of the area, the area of the area, the area and the area of the area, the area of the area, the area of the area, the area of the area, the area of the area, the solidification of the solution after the second stage of leaching, the separation of solid residue, the area of the area, the area of the area, the area of the area, the area of the area, the area of the area, the area of the area separating aluminum hydroxide from the de-scrubbed solution to produce a sodium hydroxide mother liquor, passing the mother liquor after crystallization of potassium sulphate through cationite in sodium form, then cationic treatment with sodium hydroxide and feeding the resulting potassium hydroxide solution to the first stage of baking. Moreover, a solid residue after the desilication stage containing gshyumo yatri silicate is used as a cation exchanger, and a mother liquor is used as a sodium hydroxide to treat the cation exchanger after release of aluminum hydroxide. The method is carried out as follows.
After dehydrating roasting, alunite is fed to the first leaching stage, then the residue is separated from the potassium sulfate solution, from which the potassium sulfate is crystallized, and part of the mother liquor after crystallization is returned to the first leaching stage of the ore,
The residue after the first separation stage enters the second leaching stage with a solution of caustic soda to convert the aluminum-containing components to aluminates. After separation of the solid residue from the second leaching stage, the solution is fed to desilication, after which an aluminate solution and a residue containing mainly sodium aluminosilicate are obtained.
The aluminate solution proceeds further to the stage of release of aluminum hydroxide with the return of a part of the aluminum stock solution to the second leaching stage.
The potassium sulphate solution withdrawn from the potassium sulphate crystallization step is passed through a cationite to obtain the potassium hydroxide solution returned to the first leaching stage.
The cation exchanger is then treated with sodium hydroxide to regenerate it and produce sodium sulphate solution. As the sodium hydroxide, the mother solution can be used after the release of aluminum hydroxide, and the quality of the cation exchanger is the residue of the fossilization stage containing
Example. Use highly acidic sulfonated polystyrene
resin sewn DIVINILBENZOLOM in KOLI
as / «} .0%, containing sulfo groups as functional groups.
A resin resin with a wet volume of 48 ml is introduced into a vertical column 2.5 cm in diameter and 122 cm high. The particle size of the resin is 1,550 mesh. The sulfate solution used contains 50 g / l potassium sulfate and 0.02 g / l sodium. The sodium hydroxide solution used has a concentration of 26.9 g / l and contains V of 0.02 g / l of potassium.
The sulphate solution is passed through a cation exchanger in the sodium form, which is then treated with sodium hydroxide. The volumetric flow rate of the solutions through the cation exchanger is 0.3-0.5 ml / min. Samples of the effluent are subsequently taken and analyzed for sodium and potassium.
The results of the passage of the sulfate solution through the cationite are presented in Table. 1 and the treatment of cation exchanger with sodium hydroxide is given in tab. 2
The potassium saturation results show a very rapid saturation of the effluent stream, with maximum saturation being reached by the time the ninth and tenth samples are taken.
Potassium desorption (treatment with sodium hydroxide) is also achieved quickly;
The effectiveness of the proposed method lies in the fact that the potassium hydroxide necessary for the first leaching stage is obtained from the by-products potassium sulfate and sodium hydroxide, as well as using the residue from the desilicating stage.
Table 1
/ Tables

权利要求:
Claims (2)
[1]
1. A method of processing alunite, including dehydration, roasting, two-stage etching of burning alunite, crystallization of potassium sulphate from the solution of the first leaching stage, separation of the mother liquor from potassium sulphate crystals, desiliconization of the solution after
of the second stage, the separation of the solid residue containing sodium aluminosilicate from the solution, the release of aluminum hydroxide from
brittle solution to produce a sodium hydroxide mother liquor, characterized in that, in order to increase the process efficiency, the mother liquor after crystallization of potassium sulfate
1 "rop1 | gscaut through the cationic in the ipium” form, then the cation exchanger is treated with sodium hydroxide and the resulting potassium hydroxide solution is fed to the first leaching stage.
[2]
2. The method according to p. If of a tp and h and u and the fact that in the cation of the cation use a solid residue after the desilting stage, the content of sodium aluminosilicate
3 6 The method according to claim 1, distinguishing IS and using the mother liquor as sodium hydroxide for treating the cation exchanger after isolating apyumini hydroxide.
Information sources,
taken into consideration during the examination
1O Liner A.I., Production of Gold Izozemas M., 1961, p. 613-619.

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同族专利:

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公开号 | 公开日

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AR221322A1|1981-01-30|

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SU691072A3|1979-10-05|

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US3996334A|1976-12-07|

---

IT1065856B|1985-02-25|

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GR60624B|1978-07-05|

引用文献:

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US2099360A|1934-03-06|1937-11-16|Nihon Denki Kogyo Kabushiki Ka|Process of producing pure alumina and crude potassium sulphate from alunite|

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US2120840A|1934-08-20|1938-06-14|Bohn Aluminium & Brass Corp|Cyclic process for treating alunite|

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US2398425A|1943-04-27|1946-04-16|Elnathan H Steinman|Process for treating alunite ores and the like|

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US3063805A|1959-09-01|1962-11-13|Int Minerals & Chem Corp|Production of potassium hydroxide|

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US3890425A|1974-03-21|1975-06-17|Southwire Co|Redox treatment of alunite ore|

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US3890426A|1974-03-21|1975-06-17|Southwire Co|Method of treating alunite ore|US4064217A|1976-09-30|1977-12-20|Hartman George J|Process for recovering aluminum from alunite ore|

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US4423012A|1981-12-31|1983-12-27|Hazen Research Incorporated|Manganese and zinc solvent extraction process|

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US4618480A|1984-08-15|1986-10-21|Resource Technology Associates|Recovery of alumina values from alunite ore|

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US4786482A|1986-02-03|1988-11-22|Aluminum Company Of America|Bayer process for producing aluminum hydroxide having improved whiteness|

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US20060024769A1|2004-07-29|2006-02-02|Saladax Biomedical Inc.|Taxol immunoassay|

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US20060177883A1|2005-02-08|2006-08-10|Saladax Biomedical Inc.|5-Fluoro-uracil immunoassay|

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CN101913633B|2010-07-07|2014-12-10|紫金矿业集团股份有限公司|Extraction technology of alumina and potassium sulfate from alunite by using hot-pressing leaching process|

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CN103588232A|2012-08-16|2014-02-19|贵阳铝镁设计研究院有限公司|Method and apparatus for rapidly removing silicon from raw ore pulp|

法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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US05/582,806|US3996334A|1975-06-02|1975-06-02|Process for recovering aluminum from alunite|

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