WO1991001271A1 - Procede pour obtenir de la poudre de disiliciure de molybdene - Google Patents
Procede pour obtenir de la poudre de disiliciure de molybdene Download PDFInfo
- Publication number
- WO1991001271A1 WO1991001271A1 PCT/SU1989/000197 SU8900197W WO9101271A1 WO 1991001271 A1 WO1991001271 A1 WO 1991001271A1 SU 8900197 W SU8900197 W SU 8900197W WO 9101271 A1 WO9101271 A1 WO 9101271A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- mixture
- magnesium
- weight
- ore
- κachesτve
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/06—Metal silicides
Definitions
- the resulting molybdenum dyslicide is in the form of a coolant, finishes and treats the investigated saline acid and click to isolate the mild mild disincide.
- the described method is distinguished by the duration of the process, the power process, and the resulting process.
- the method of producing molybdenum disilicide is known, including the preparation of an ectothermic mixture from
- the target product is contaminated with aluminum oxide.
- the mill is grinded, and additionally, it is contaminated
- composition in the middle of particles with a range of 2-5 microns, for example, is no more than $ 30.
- the product made from such molybdenum disilicide 5 is not suitable for frequent use, but it is often very difficult.
- the main task was to develop the task.
- Task 15 ⁇ eshae ⁇ sya ⁇ em, ch ⁇ ⁇ edlagae ⁇ sya s ⁇ s ⁇ b ⁇ - radiation ⁇ sh ⁇ b ⁇ azn ⁇ g ⁇ disil ⁇ schda m ⁇ libdena, v ⁇ lyuchayu- sch ⁇ y ⁇ ig ⁇ vlenie e ⁇ z ⁇ e ⁇ miches ⁇ y smes ⁇ of ⁇ sh ⁇ v m ⁇ - libdens ⁇ de ⁇ zhascheg ⁇ ⁇ m ⁇ nen ⁇ a, ⁇ emniys ⁇ de ⁇ zhascheg ⁇ ⁇ m ⁇ nen ⁇ a and me ⁇ alla, and its u ⁇ l ⁇ nenie ⁇ e ⁇ m ⁇ b ⁇ ab ⁇ u in ⁇ ezhime
- the mixture be injected with magnesium oxide in a quantity of 10-15% of its mass and its consumption of 0.5-1.0%.
- the structure and the quality of the disposable disilyodets can be divided by a free-flowing mixture, and it is free of charge for the user.
- the concentrate of ore from ore contains 90-95 wt. % ⁇ 0 3 and ⁇ ⁇ and 5-10 wt. % impurities, hazardous oxides, alkaline and alkaline-earth metals. To increase the efficiency of the mixture and create the most favorable
- 25 rhenium magnesium ensures the restoration of mogbdenum and winter from their oxides, which are directly related to the interaction between molybdenum. Due to the composition of the mixture, its efficiency and density, equal to 1.25- 1.45 g / cm 3 , the combustion process is lower than the temperature of the mixture
- 35 may contain non-reactive original components. Depending on the percentage of magnesium in the mixture, the latter is recommended to be diluted with magnesium oxide, in the amount of 10-15% of its total mass. It provides the necessary e-mail. - 5 - the thermal stability of the mixture and its mixture.
- the content of magnesium oxide in the mixture which is characterized by a significant effec- tivity, is less than 10 wt. % of the burned burner may have a 5 burner burner that may increase the temperature of the melting oven, which may result in a malfunctioning burner that is not being burned.
- the hot magnesium oxide in the ectothermic mixture is more than 15 wt. % can reduce the incineration rate of combustion by preventing the incineration of incineration
- the density of the mixture should be in the range of 1.25-1.45 g / cm 3 . With a surface area of less than 1.25 g / cm 3, the combustion process due to the lack of particle contact is not available. It also doesn’t occur at a density greater than 1.45
- inert gas such as gas, gas
- Slag which is a representative of the oxides of magnesium, hard liquor halides and oxides of alkaline, alkaline-earth metals, is disposed of, and the waste is disposed of
- 35th disilicide maybdenum remains in the sediment. It dries and sends to the user. - 6 -
- the invention will find an explanation for the use of metallurgical materials for the manufacture of refractory materials, exhaustive materials, and electrical equipment.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Le procédé consiste à préparer un mélange exothermique de la composition suivante, en pour cent en poids: concentré de minerai de molybdène 30-35, minerai concentré de silicium 25-30, magnésium le solde. Le mélange est ensuite concentré jusqu'à obtention d'une masse volumique de 1,25-1,45 g/cm3 et soumis au traitement thermique dans un régime de calcination avec séparation ultérieure de la poudre de disiliciure de molybdène et des scories. Il est recommandé d'introduire dans le mélange l'oxyde de magnésium dans une quantité égale à 10-15 % de son poids et d'effectuer le traitement thermique sous une pression de 0,5-1 MPa.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/SU1989/000197 WO1991001271A1 (fr) | 1989-07-14 | 1989-07-14 | Procede pour obtenir de la poudre de disiliciure de molybdene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/SU1989/000197 WO1991001271A1 (fr) | 1989-07-14 | 1989-07-14 | Procede pour obtenir de la poudre de disiliciure de molybdene |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1991001271A1 true WO1991001271A1 (fr) | 1991-02-07 |
Family
ID=21617517
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SU1989/000197 WO1991001271A1 (fr) | 1989-07-14 | 1989-07-14 | Procede pour obtenir de la poudre de disiliciure de molybdene |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO1991001271A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5618429A (en) * | 1994-03-24 | 1997-04-08 | Lumos Trading & Investments Corporation | Method for reducing slime and film formation in plants in which the water of paper and pulp machines is circulated and in plants in which cooling water is circulated |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2619406A (en) * | 1949-04-27 | 1952-11-25 | Union Carbide & Carbon Corp | Method for the solid phase production of a disilicide |
US3362787A (en) * | 1964-02-04 | 1968-01-09 | Norton Co | Preparation of molybdenum silicides |
US3726643A (en) * | 1970-04-09 | 1973-04-10 | I Khim Fiz Akademii Nauk | Method of producing refractory carbides,borides,silicides,sulfides,and nitrides of metals of groups iv,v,and vi of the periodic system |
SU617485A1 (ru) * | 1975-06-26 | 1978-07-30 | Отделение Ордена Ленина Институт Химической Физик Ан Ссср | Способ получени тугоплавких неорганически материалов |
GB2166160A (en) * | 1984-08-30 | 1986-04-30 | Mitsubishi Metal Corp | Sputtering target material and process for producing the same |
-
1989
- 1989-07-14 WO PCT/SU1989/000197 patent/WO1991001271A1/fr unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2619406A (en) * | 1949-04-27 | 1952-11-25 | Union Carbide & Carbon Corp | Method for the solid phase production of a disilicide |
US3362787A (en) * | 1964-02-04 | 1968-01-09 | Norton Co | Preparation of molybdenum silicides |
US3726643A (en) * | 1970-04-09 | 1973-04-10 | I Khim Fiz Akademii Nauk | Method of producing refractory carbides,borides,silicides,sulfides,and nitrides of metals of groups iv,v,and vi of the periodic system |
SU617485A1 (ru) * | 1975-06-26 | 1978-07-30 | Отделение Ордена Ленина Институт Химической Физик Ан Ссср | Способ получени тугоплавких неорганически материалов |
GB2166160A (en) * | 1984-08-30 | 1986-04-30 | Mitsubishi Metal Corp | Sputtering target material and process for producing the same |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5618429A (en) * | 1994-03-24 | 1997-04-08 | Lumos Trading & Investments Corporation | Method for reducing slime and film formation in plants in which the water of paper and pulp machines is circulated and in plants in which cooling water is circulated |
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