SU46259A1 - The method of obtaining zirconium oxide and Norwegian nitrate - Google Patents
The method of obtaining zirconium oxide and Norwegian nitrateInfo
- Publication number
- SU46259A1 SU46259A1 SU171388A SU171388A SU46259A1 SU 46259 A1 SU46259 A1 SU 46259A1 SU 171388 A SU171388 A SU 171388A SU 171388 A SU171388 A SU 171388A SU 46259 A1 SU46259 A1 SU 46259A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- nitrate
- norwegian
- zirconium oxide
- eudiolite
- obtaining zirconium
- Prior art date
Links
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 title description 4
- MCMNRKCIXSYSNV-UHFFFAOYSA-N ZrO2 Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 title 1
- 229910001928 zirconium oxide Inorganic materials 0.000 title 1
- 239000012141 concentrate Substances 0.000 description 6
- GFQYVLUOOAAOGM-UHFFFAOYSA-N Zirconium(IV) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229910052845 zircon Inorganic materials 0.000 description 3
- 229910052846 zircon Inorganic materials 0.000 description 3
- 229910000166 zirconium phosphate Inorganic materials 0.000 description 3
- LEHFSLREWWMLPU-UHFFFAOYSA-B zirconium(4+);tetraphosphate Chemical compound [Zr+4].[Zr+4].[Zr+4].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LEHFSLREWWMLPU-UHFFFAOYSA-B 0.000 description 3
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N Calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating Effects 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- GEIAQOFPUVMAGM-UHFFFAOYSA-N oxozirconium Chemical compound [Zr]=O GEIAQOFPUVMAGM-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- -1 -0.55 Inorganic materials 0.000 description 1
- KYARBIJYVGJZLB-UHFFFAOYSA-N 7-amino-4-hydroxy-2-naphthalenesulfonic acid Chemical compound OC1=CC(S(O)(=O)=O)=CC2=CC(N)=CC=C21 KYARBIJYVGJZLB-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical class Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N TiO Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910052586 apatite Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000005712 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- YIXQSYHBXUBLPM-UHFFFAOYSA-N dioxido(oxo)silane;zirconium(4+) Chemical compound [Zr+4].[O-][Si]([O-])=O.[O-][Si]([O-])=O YIXQSYHBXUBLPM-UHFFFAOYSA-N 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- QOKYJGZIKILTCY-UHFFFAOYSA-J hydrogen phosphate;zirconium(4+) Chemical compound [Zr+4].OP([O-])([O-])=O.OP([O-])([O-])=O QOKYJGZIKILTCY-UHFFFAOYSA-J 0.000 description 1
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012452 mother liquor Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
Description
Дл получени ZrOs за границей примен ют высокопроцентные цирконовые минералы, как-то: баделит (ZrO2), циркон (ZrSiO).To obtain ZrOs abroad, high-grade zircon minerals are used, such as: Badelite (ZrO2), Zircon (ZrSiO).
Дл переработки этих минералов примен ют либо щелочные методы, либо кислотные, причем из кислотных методов , из журнальной и патентной литературы известны сернокислотный и сол нокислотный .Either alkaline or acidic methods are used to process these minerals, and sulfuric acid and hydroacidic are known from acidic methods from the journal and patent literature.
У нас в СССР залежей высокопроцентных цирконовых минералов не имеетс , но имеютс большие запасы (до 50 млн. тонн) эвдиолитовых пород в Ловозерских тундрах, каковые после механического обогащени дают эвдиолитовый концентрат, представл ющий собой кальциево-железистый силикат циркони , имеющий следующий состав: ZrO..-в/о, TiO,-0,55, SiOz -51,82, Саб - 9,16, FejOs - 8,40.We in the USSR do not have deposits of high-grade zircon minerals, but there are large reserves (up to 50 million tons) of eudiolite rocks in the Lovozero tundras, which, after mechanical enrichment, produce eudiolite concentrate, which is calcium-ferrous zirconium silicate, having the following composition: ZrO ..- w / o, TiO, -0.55, SiOz -51.82, Sab - 9.16, FejOs - 8.40.
Суд по заграничной патентной и журнальной литературе, на практике одним из наиболее прин тых способов выделени циркони из кислых растворов (НС или ) вл етс осаждение The court in overseas patent and journal literature, in practice, one of the most accepted methods for separating zirconium from acidic solutions (HC or) is precipitation
его в виде фосфата циркони фосфорной its in the form of zirconium phosphate phosphate
J кислотой.J acid
Применение серной и сол ной кислот дл разложени эвдиолита авторы считают нецелесообразным по следующим причинам:The use of sulfuric and hydrochloric acids for the decomposition of eudiolite is considered inappropriate for the following reasons:
1) потер как так и HCI в виде1) lost both HCI in the form
(95)(95)
малоценных продуктов СаЗОч и СаС за счет СаО эвдиолитового концентрата;low-value products of SaZOCH and CaC due to the CaO of eudiolite concentrate;
2)обработка HCI эвдиолитового концентрата при нагревании крайне затрудн ет выбор материала дл аппаратуры и, наконец,2) HCI treatment of the eudiolite concentrate when heated makes it extremely difficult to choose the material for the apparatus and, finally,
3)необходимость применени фосфорной кислоты дл осаждени фосфата циркони , крайне удорожает продукт .3) the need to use phosphoric acid to precipitate zirconium phosphate, extremely expensive product.
Исход из вышеизложенного, предлагаетс новый способ переработки эвдиолитового концентрата с получением ZrO2 и норвежской селитры, заключающийс в следующем. Эвдиолит подвергают разложению избытком азотной кислоты; при этом в раствор переход т Са, Zr и Fe в виде соответствующих нитратов, оставл в остатке SiOj. Полученный азотнокислый раствор подвергаетс осаждению апатитовым концентратом с образованием фосфата циркони и норвежской селитры. Полученный фосфат циркони подвергаетс , как обычно, спеканию с содой с получением NajPOd и ZrOj, каковые раздел ютс выщелачиванием водой. /Азотнокислый раствор нитрата кальци и нитрата железа подвергаетс выправке и кристаллизации с выделением норвежской селитры, а маточный раствор подвергаетс очистке от железа и идет на вторичную обработку эвдиолитового концентрата (см. прилагаемую схему).Based on the foregoing, a new method is proposed for processing eudiolite concentrate to produce ZrO2 and Norwegian nitrate, as follows. Evdiolit decomposed with an excess of nitric acid; at the same time, Ca, Zr and Fe are transferred to the solution in the form of the corresponding nitrates, leaving SiOj as a residue. The resulting nitric acid solution is subjected to precipitation with an apatite concentrate to form zirconium phosphate and Norwegian nitrate. The zirconium phosphate obtained is subjected, as usual, to sintering with soda to obtain NajPOd and ZrOj, which are separated by leaching with water. / The nitric acid solution of calcium nitrate and iron nitrate undergoes straightening and crystallization to liberate Norwegian nitrate, and the mother liquor is purified from iron and is recycled to the eudiolite concentrate (see the attached diagram).
Publications (1)
Publication Number | Publication Date |
---|---|
SU46259A1 true SU46259A1 (en) | 1936-03-31 |
Family
ID=
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4297326A (en) | Method of producing a pure aluminiumoxide from solutions containing dissolved ions of aluminium and iron | |
SU46259A1 (en) | The method of obtaining zirconium oxide and Norwegian nitrate | |
DE424017C (en) | Process for the production of acidic sodium formates | |
GB159086A (en) | An improved process of producing oxide of aluminium from chloride of aluminium | |
GB800052A (en) | Process for recovering acid from waste acid liquors | |
DE641300C (en) | Process for the production of alumina from an ammonium alum | |
DE570015C (en) | Process for de-ironing minerals such as bauxite, clay, kieselguhr, and residues such as coal slag, blast furnace slag | |
DE641207C (en) | Process for the production of alumina from an alkali metal alum | |
SU60252A1 (en) | The method of obtaining uranium oxide | |
DE448848C (en) | Process for the production of iron-free metal salts, in particular aluminum salts | |
DE562498C (en) | Manufacture of practically iron-free alumina from clay | |
DE461556C (en) | Process for the production of pure metal oxides or metal hydroxides from precipitates containing basic metal compounds | |
DE602281C (en) | Process for the extraction of manganese | |
AT151634B (en) | Process for processing aluminum ores. | |
DE512130C (en) | Process for the production of aluminum compounds and phosphoric acid | |
DE600175C (en) | Process for the production of thorium-free chlorides of the cerium group | |
DE688564C (en) | Process for the extraction of manganese from substances containing manganese | |
AT138006B (en) | Process for the production of thorium-free chlorides of the cerium group. | |
DE1116693B (en) | Process for processing iron ore | |
DE369041C (en) | Process for the extraction of nickel from nickel-containing hydrosilicates | |
DE570589C (en) | Separation of trialkali phosphate from this and alkaline hydrolytically cleaved salts, e.g. B. sodium aluminate containing solutions | |
AT80341B (en) | Process for the separation of thorium from oxalate Process for the separation of thorium from oxalate-containing soda solutions. old soda eyes. | |
DE525157C (en) | Process for the production of chromate with the simultaneous extraction of alumina | |
DE366969C (en) | Process for the production of sodium nitrate | |
AT134244B (en) | Process for the production of alumina from clay and other alumina-containing substances. |