SU481543A1 - The method of cleaning aluminate solutions - Google Patents
The method of cleaning aluminate solutionsInfo
- Publication number
- SU481543A1 SU481543A1 SU1895872A SU1895872A SU481543A1 SU 481543 A1 SU481543 A1 SU 481543A1 SU 1895872 A SU1895872 A SU 1895872A SU 1895872 A SU1895872 A SU 1895872A SU 481543 A1 SU481543 A1 SU 481543A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- solution
- cleaning
- manganese
- aluminate
- aluminate solutions
- Prior art date
Links
- 238000000034 method Methods 0.000 title description 14
- 150000004645 aluminates Chemical class 0.000 title description 7
- 238000004140 cleaning Methods 0.000 title description 6
- 239000000243 solution Substances 0.000 description 19
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 7
- 229910052748 manganese Inorganic materials 0.000 description 7
- 239000011572 manganese Substances 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 229910052717 sulfur Inorganic materials 0.000 description 6
- 239000011593 sulfur Substances 0.000 description 6
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000002386 leaching Methods 0.000 description 3
- 150000002697 manganese compounds Chemical class 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910001570 bauxite Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 150000002696 manganese Chemical class 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000004131 Bayer process Methods 0.000 description 1
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011538 cleaning material Substances 0.000 description 1
- HOOWDPSAHIOHCC-UHFFFAOYSA-N dialuminum tricalcium oxygen(2-) Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[Al+3].[Al+3].[Ca++].[Ca++].[Ca++] HOOWDPSAHIOHCC-UHFFFAOYSA-N 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- AMWRITDGCCNYAT-UHFFFAOYSA-L manganese oxide Inorganic materials [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 1
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000009856 non-ferrous metallurgy Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
(54) СПОСОБ ОЧИСТКИ АЛЮМИНАТНЫХ РАСТВОРОВ(54) METHOD FOR CLEANING ALUMINATE SOLUTIONS
1one
Изобрсгение относитс к цветной металлургии , в частности к производству окиси алюмини .,The image refers to non-ferrous metallurgy, in particular to the production of alumina.,
Известен способ очистки обескремненных алюминатных растворов от железа перманганатом кали с посдедуюшей фильтрацией через слой гидроокиси алюмини или трехкальциевого алюмината.A known method of purification of demineralized aluminate solutions from iron with potassium permanganate with subsequent filtration through a layer of aluminum hydroxide or tricalcium aluminate.
В данном способе соединение марганца ввод т с целью ойислени двухвалентного, железа в трехвалентное.In this method, the manganese compound is introduced for the purpose of adding bivalent, ferric to ferric iron.
Однако известный способ требует использовани дорогих и дефицитных чистых солей марганца, приготовление и применение адсор бентов, процесс осуществл етс в две стадии, он имеет низкую производительность стадии фильтрации раствора через слой адсорбента, алюминатный раствор загр зн етс калием, а степень очистки растворов от железа составл ет не более 7О%.However, the known method requires the use of expensive and scarce pure manganese salts, the preparation and use of adsorbents, the process is carried out in two stages, it has a low productivity of the solution filtration stage through the adsorbent layer, the aluminate solution is contaminated with potassium, em no more than 7%.
Если алюминатный раствор загр знен сульфидной серой, то расход окислителей резко возрастает и процесс очистки становитс намного дороже.If the aluminate solution is contaminated with sulfide sulfur, the consumption of oxidants increases dramatically and the cleaning process becomes much more expensive.
Цель изобретени - повысить степень очистки раствора, упростить и удешевить процесс удалени примесей.The purpose of the invention is to increase the degree of purification of the solution, to simplify and cheapen the process of removing impurities.
Это достигаетс использованием соеднени марганца в смеси с двуокисью кремни . В данном случае используют способность окислов марганца даватльг малорастворимые соеданени с окислами железа и кремни , а также с сульфидной серой. Окислительные способности, окислов марганца здесь не играют существенной роли. В ка«- честве очищающих материалов можно использовать дешевую марганцевую пиролизитовую руду и марганцовистые .металлургические шлаки.This is achieved by using a compound of manganese mixed with silica. In this case, the ability of oxides of manganese makes low-soluble compounds with oxides of iron and silicon, as well as with sulfide sulfur. Oxidizing ability, manganese oxides do not play a significant role here. As a cleaning material, cheap manganese pyrolysite ore and manganese metallurgical slags can be used.
.Приме р. 20 г измельченного боксита выщелачивают щелочным раствором, содержащим 315 г/л 134 г/л.Prime p. 20 g of crushed bauxite is leached with an alkaline solution containing 315 g / l 134 g / l
А1„О и 4 г/л сульфидной серы при 230°С i. о,A1 „O and 4 g / l of sulfide sulfur at 230 ° С i. about,
в течение 2 час при Ж:Т равном 4. : В пульпу перед выщелачиванием ввод т марганцевую руду из расчета 2,5 г на 100 мл раствора. После выщелачивани пульпу разбавл ют водой, охлаждают до 96°С, выдерживают дл сгущени шлама ЗО мин и осветленный раствор фильтруют, (TO е. имитируют процесс получени алюми натного раствора в способе Байера), Фильтрат анализируют на содержание глинозема, щелочи кремни железа и су л фидной серы. Согласно анализу содержание железа в растворе уменьшают на 93,2% „ сульфидной серы - на 8158%. Пр этом снижают содержание кремни на 42,5%, Концентраци щелочи и , окиси агиомини растворе остались такими же как iF растворе, .без добавки марганцевой рудьи Содержание марганца в растворе г/ Преимущества способа состо т в том,. что отпадает необходимость применени дорогих чистых солей марганца, исключаетс фильтраци раствора через слой адсорбента, повышаетс степень очистки раствора от железа. Кроме того, раствор о шшаетс от вре.цных примесей сульфи,|дной серы и кремнйЯ; значите шно снижаютс затраты на очистку раствора Операци очистки алюминатного раствора совмеща- ечс с процессом выщелачивани боксита е и не требует дополнительного технологического оборудовани . Предлагаемый споооб может быть внедрен на алюминиевых заводах Урала„ Предметизобретени Способ очистки алюминатнь1х растворов от примесей путем обработки кислородсо- j держащими соединени ми марганца, о т л и ч а ю щ и и с тем, что,, с целью повышени степени очистки и упрощени процесса, соединени марганца используют Б смеси с двуокисью кремниЯоfor 2 hours at L: T equal to 4.: Manganese ore at the rate of 2.5 g per 100 ml of solution is introduced into the pulp before leaching. After leaching, the pulp is diluted with water, cooled to 96 ° C, kept for thickening of the sludge DZ min and the clarified solution is filtered, (TO e. Simulate the process of obtaining an alumina solution in the Bayer process). l feed sulfur. According to the analysis, the iron content in the solution is reduced by 93.2% „of sulfide sulfur - by 8158%. This reduces the silicon content by 42.5%. The concentration of alkali and, agiomini oxide solution remained the same as the iF solution, without the addition of manganese ore manganese content in solution g / The advantages of the method are. that there is no need to use expensive pure manganese salts, filtering the solution through the adsorbent layer is eliminated, the degree of purification of the solution from iron increases. In addition, the solution is shed from the impurities of sulfide, sulfur and silicon; This means that the cost of solution cleaning is reduced. The cleaning of the aluminate solution is combined with the leaching process of bauxite e and does not require additional technological equipment. The proposed method can be implemented at aluminum plants in the Urals. Subject matter The method of cleaning aluminate solutions from impurities by treating with oxygen-containing manganese compounds so that, in order to increase the degree of purification and simplify process, manganese compounds use B mixtures with silicon dioxide
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1895872A SU481543A1 (en) | 1973-03-14 | 1973-03-14 | The method of cleaning aluminate solutions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1895872A SU481543A1 (en) | 1973-03-14 | 1973-03-14 | The method of cleaning aluminate solutions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU481543A1 true SU481543A1 (en) | 1975-08-25 |
Family
ID=20546129
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1895872A SU481543A1 (en) | 1973-03-14 | 1973-03-14 | The method of cleaning aluminate solutions |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU481543A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1985005095A1 (en) * | 1984-05-03 | 1985-11-21 | The Broken Hill Proprietary Company Limited | Removal of organics from bayer process streams |
| US4609534A (en) * | 1984-10-09 | 1986-09-02 | Aluminum Company Of America | Lime cleaning process to remove manganese oxide |
-
1973
- 1973-03-14 SU SU1895872A patent/SU481543A1/en active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1985005095A1 (en) * | 1984-05-03 | 1985-11-21 | The Broken Hill Proprietary Company Limited | Removal of organics from bayer process streams |
| US4836990A (en) * | 1984-05-03 | 1989-06-06 | The Broken Hill Proprietary Company Ltd. | Removal of organics from Bayer process streams |
| US4609534A (en) * | 1984-10-09 | 1986-09-02 | Aluminum Company Of America | Lime cleaning process to remove manganese oxide |
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