RU95103820A - METHOD FOR PREPARING MAGNESIUM AND CHLORINE IN A FLOW LINE - Google Patents
METHOD FOR PREPARING MAGNESIUM AND CHLORINE IN A FLOW LINEInfo
- Publication number
- RU95103820A RU95103820A RU95103820/02A RU95103820A RU95103820A RU 95103820 A RU95103820 A RU 95103820A RU 95103820/02 A RU95103820/02 A RU 95103820/02A RU 95103820 A RU95103820 A RU 95103820A RU 95103820 A RU95103820 A RU 95103820A
- Authority
- RU
- Russia
- Prior art keywords
- raw materials
- closed loop
- production line
- magnesium
- solid
- Prior art date
Links
- FYYHWMGAXLPEAU-UHFFFAOYSA-N magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims 4
- 229910052749 magnesium Inorganic materials 0.000 title claims 4
- 239000011777 magnesium Substances 0.000 title claims 4
- 239000000460 chlorine Substances 0.000 title claims 2
- 229910052801 chlorine Inorganic materials 0.000 title claims 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title claims 2
- 239000002994 raw material Substances 0.000 claims 12
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L MgCl2 Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims 8
- 238000004519 manufacturing process Methods 0.000 claims 7
- 239000007787 solid Substances 0.000 claims 7
- 239000003792 electrolyte Substances 0.000 claims 5
- 229910001629 magnesium chloride Inorganic materials 0.000 claims 4
- -1 chlorine-magnesium Chemical compound 0.000 claims 2
- 239000000155 melt Substances 0.000 claims 2
- 229910052751 metal Inorganic materials 0.000 claims 2
- 239000002184 metal Substances 0.000 claims 2
- 239000007789 gas Substances 0.000 claims 1
- 230000001105 regulatory Effects 0.000 claims 1
- 238000005070 sampling Methods 0.000 claims 1
- 239000010802 sludge Substances 0.000 claims 1
- 239000011343 solid material Substances 0.000 claims 1
- 238000004642 transportation engineering Methods 0.000 claims 1
Claims (7)
Рт = [р•Рм - Рр•Ср + (С2 - С1)•Мр]: Ст : Э : Т,
где Pт - задаваемая средняя скорость загрузки твердого сырья в единичный электролизер замкнутого контура;
р - нормативный расход хлористого магния на единицу массы полученного металла;
Рм - количество полученного в расчетный промежуток времени магния во всей поточной линии;
Рр - количество сырья, загруженного в агрегаты поточной линии в расплавленном состоянии в расчетный промежуток времени;
Ср - среднее содержание хлористого магния в загружаемом в агрегаты поточной линии расплавленном сырье;
Ст - среднее содержание хлористого магния в загружаемом в электролизеры замкнутого контура твердом сырье;
С2 и С1 - среднее содержание хлористого магния в системе за расчетный и предшествующий ему промежутки времени;
Мр - масса расплава во всех агрегатах поточной линии;
Э - количество электролизеров, работающих в замкнутом контуре, в которые производится загрузка сырья;
Т - длительность расчетного промежутка времени.2. The method according to p. 1, characterized in that the average rate of loading of solid raw materials in the closed loop electrolyzer is calculated by the formula
Р т = [р • Р м - Р р • С р + (С 2 - С 1 ) • М р ]: С т : Э: Т,
where P t - set the average download speed of solid raw materials in a single closed loop electrolyzer;
p is the standard consumption of magnesium chloride per unit mass of the obtained metal;
P m - the amount of magnesium obtained in the calculated period of time in the entire production line;
R p - the number of raw materials loaded into the units of the production line in the molten state in the estimated period of time;
C p - the average content of magnesium chloride in the molten raw material loaded into the aggregates of the production line;
C t is the average content of magnesium chloride in the solid material loaded in the closed loop electrolytic cells;
C 2 and C 1 - the average content of magnesium chloride in the system for the calculated and preceding periods of time;
M p - the mass of the melt in all units of the production line;
E - the number of electrolyzers operating in a closed loop, in which the raw material is loaded;
T - the duration of the estimated period of time.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU95103820A RU2095479C1 (en) | 1995-03-17 | 1995-03-17 | Magnesium and chlorine in-line production process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
RU95103820A RU2095479C1 (en) | 1995-03-17 | 1995-03-17 | Magnesium and chlorine in-line production process |
Publications (2)
Publication Number | Publication Date |
---|---|
RU95103820A true RU95103820A (en) | 1997-07-27 |
RU2095479C1 RU2095479C1 (en) | 1997-11-10 |
Family
ID=20165699
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU95103820A RU2095479C1 (en) | 1995-03-17 | 1995-03-17 | Magnesium and chlorine in-line production process |
Country Status (1)
Country | Link |
---|---|
RU (1) | RU2095479C1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2719215C1 (en) * | 2019-07-12 | 2020-04-17 | Публичное Акционерное Общество "Корпорация Всмпо-Ависма" | Method for thermal control of magnesium electrolytic production process and device for its implementation |
-
1995
- 1995-03-17 RU RU95103820A patent/RU2095479C1/en active
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