RU99101660A - METHOD OF PREPARING MAGNESIUM - Google Patents
METHOD OF PREPARING MAGNESIUMInfo
- Publication number
- RU99101660A RU99101660A RU99101660/12A RU99101660A RU99101660A RU 99101660 A RU99101660 A RU 99101660A RU 99101660/12 A RU99101660/12 A RU 99101660/12A RU 99101660 A RU99101660 A RU 99101660A RU 99101660 A RU99101660 A RU 99101660A
- Authority
- RU
- Russia
- Prior art keywords
- chloride
- magnesium
- carnallite
- dehydration
- calcium
- Prior art date
Links
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims 7
- 239000011777 magnesium Substances 0.000 title claims 7
- 229910052749 magnesium Inorganic materials 0.000 title claims 7
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L MgCl2 Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims 14
- PALNZFJYSCMLBK-UHFFFAOYSA-K magnesium;potassium;trichloride;hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[Cl-].[Cl-].[Cl-].[K+] PALNZFJYSCMLBK-UHFFFAOYSA-K 0.000 claims 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims 7
- 238000006297 dehydration reaction Methods 0.000 claims 7
- 229910001629 magnesium chloride Inorganic materials 0.000 claims 7
- 239000000243 solution Substances 0.000 claims 6
- UXVMQQNJUSDDNG-UHFFFAOYSA-L cacl2 Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims 5
- 239000001110 calcium chloride Substances 0.000 claims 5
- 229910001628 calcium chloride Inorganic materials 0.000 claims 5
- 239000007789 gas Substances 0.000 claims 5
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 claims 5
- 229910000041 hydrogen chloride Inorganic materials 0.000 claims 5
- 239000000460 chlorine Substances 0.000 claims 4
- 229910052801 chlorine Inorganic materials 0.000 claims 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims 4
- 238000005868 electrolysis reaction Methods 0.000 claims 4
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims 4
- 229940077747 antacids containing calcium compounds Drugs 0.000 claims 3
- 150000001674 calcium compounds Chemical class 0.000 claims 3
- 229940043430 calcium compounds Drugs 0.000 claims 3
- 238000000034 method Methods 0.000 claims 3
- 239000011780 sodium chloride Substances 0.000 claims 3
- 239000007790 solid phase Substances 0.000 claims 3
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L Calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims 2
- 230000015572 biosynthetic process Effects 0.000 claims 2
- 150000001805 chlorine compounds Chemical class 0.000 claims 2
- 238000004140 cleaning Methods 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 2
- 239000003792 electrolyte Substances 0.000 claims 2
- 239000000446 fuel Substances 0.000 claims 2
- 238000004519 manufacturing process Methods 0.000 claims 2
- 239000000155 melt Substances 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 2
- 239000001103 potassium chloride Substances 0.000 claims 2
- 235000011164 potassium chloride Nutrition 0.000 claims 2
- 238000002360 preparation method Methods 0.000 claims 2
- 239000007787 solid Substances 0.000 claims 2
- 238000003786 synthesis reaction Methods 0.000 claims 2
- 230000002194 synthesizing Effects 0.000 claims 2
- 239000002912 waste gas Substances 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims 1
- 238000009825 accumulation Methods 0.000 claims 1
- 239000007864 aqueous solution Substances 0.000 claims 1
- 239000012267 brine Substances 0.000 claims 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims 1
- 238000005119 centrifugation Methods 0.000 claims 1
- 238000002485 combustion reaction Methods 0.000 claims 1
- 239000002826 coolant Substances 0.000 claims 1
- 230000000875 corresponding Effects 0.000 claims 1
- 230000005611 electricity Effects 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 235000014380 magnesium carbonate Nutrition 0.000 claims 1
- 235000019341 magnesium sulphate Nutrition 0.000 claims 1
- CSNNHWWHGAXBCP-UHFFFAOYSA-L mgso4 Chemical class [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims 1
- 239000012452 mother liquor Substances 0.000 claims 1
- 230000003472 neutralizing Effects 0.000 claims 1
- 150000002927 oxygen compounds Chemical class 0.000 claims 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims 1
- 239000011591 potassium Substances 0.000 claims 1
- 229910052700 potassium Inorganic materials 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 235000011152 sodium sulphate Nutrition 0.000 claims 1
- 239000011550 stock solution Substances 0.000 claims 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 claims 1
- 239000002699 waste material Substances 0.000 claims 1
Claims (1)
Хлорид калия - 21-25
Хлорид магния - 30-32
Хлорид натрия - 3,5-9,0,
Хлорид кальция - 0,3 - 2,0,
Вода - Остальное
2. Способ по пп. 1 и 2, отличающийся тем, что молярное соотношение хлорида калия к хлориду магния в синтетическом карналлите, поступающим на обезвоживание, поддерживают в пределах 0,9-1,05.1. The method of obtaining magnesium, including the preparation of carnallite from a solution of magnesium chloride released during the processing of magnesium-containing raw materials and waste (sea water, brine of salt lakes, carbonates, magnesites, etc.) chlorides, potassium, sodium separation by settling and / or centrifugation returned to the head the process of mother liquor from the solid phase, dehydration of the solid phase with heated gases obtained by burning fuel with primary air, and then cooling the combustion products with secondary air, gas cleaning and electrolysis to obtain magnesium, chlorine and spent electrolyte, returning the whole or part of the latter to the process, preparing carnallite, characterized in that the chlorine obtained during electrolysis is fully or partially preliminarily reduced to hydrogen chloride, feeding chlorine into the high-temperature furnace in the flame of hydrogen-containing fuel, and after cooling the superheated more than usual coolant with secondary air and dehydrate the resulting mixture with synthetic carnallite in a fluidized bed due to the heat of the mixture or additionally supplying part of the heat to carnallite using a contact method from heated devices placed in a layer or in contact with it, and then either absorbing hydrogen chloride from waste gases of dehydration with an aqueous solution circulating in a gas cleaning to obtain hydrochloric acid of a given concentration and oxygen or calcium compounds with it separately or together / or magnesium, or directly absorbing hydrogen chloride from dehydration waste gases by pulp containing the above oxygenated calcium compounds and / or magnesium to produce calcium and / or magnesium chloride solutions; however, all of the original components are introduced into the process in ratios that provide the following contents of the components in synthetic carnallite entering the dehydration, wt.%:
Potassium chloride - 21-25
Magnesium chloride - 30-32
Sodium chloride - 3.5-9.0,
Calcium chloride - 0.3 - 2.0,
Water - The Rest
2. The method according to paragraphs. 1 and 2, characterized in that the molar ratio of potassium chloride to magnesium chloride in synthetic carnallite, fed to dehydration, is maintained within 0.9-1.05.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU99101660A RU2158787C2 (en) | 1999-01-27 | 1999-01-27 | Process of winning of magnesium |
AU13565/00A AU767164B2 (en) | 1999-01-27 | 2000-01-25 | Method of magnesium production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU99101660A RU2158787C2 (en) | 1999-01-27 | 1999-01-27 | Process of winning of magnesium |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2158787C2 RU2158787C2 (en) | 2000-11-10 |
RU99101660A true RU99101660A (en) | 2000-12-20 |
Family
ID=20215208
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU99101660A RU2158787C2 (en) | 1999-01-27 | 1999-01-27 | Process of winning of magnesium |
Country Status (2)
Country | Link |
---|---|
AU (1) | AU767164B2 (en) |
RU (1) | RU2158787C2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150218720A1 (en) * | 2012-08-24 | 2015-08-06 | Orbite Aluminae Inc. | Process for treating magnesium-bearing ores |
-
1999
- 1999-01-27 RU RU99101660A patent/RU2158787C2/en not_active IP Right Cessation
-
2000
- 2000-01-25 AU AU13565/00A patent/AU767164B2/en not_active Ceased
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