SU65522A1 - The method of producing manganese dioxide - Google Patents

The method of producing manganese dioxide

Info

Publication number
SU65522A1
SU65522A1 SU414-44A SU334242A SU65522A1 SU 65522 A1 SU65522 A1 SU 65522A1 SU 334242 A SU334242 A SU 334242A SU 65522 A1 SU65522 A1 SU 65522A1
Authority
SU
USSR - Soviet Union
Prior art keywords
manganese dioxide
manganese
producing manganese
ore
pyrolusite
Prior art date
Application number
SU414-44A
Other languages
Russian (ru)
Inventor
И.С. Морозов
Original Assignee
И.С. Морозов
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by И.С. Морозов filed Critical И.С. Морозов
Priority to SU414-44A priority Critical patent/SU65522A1/en
Application granted granted Critical
Publication of SU65522A1 publication Critical patent/SU65522A1/en

Links

Description

Неоднократно делались попытки получени  активной двуокиси марганца путем хлорировани  как щелочного раствора гидрата окиси марганца, так и углекислого марганца; однако при этом получалс  продукт, неприменимый в элементной промышленности.Attempts have been made to obtain active manganese dioxide by chlorinating both an alkaline solution of manganese oxide hydrate and manganese carbonate; however, a product was obtained that was not applicable in the element industry.

Предлагаетс  способ получени  двуокиси марганца, годной в качестве депол ризатора, основанный на предварительном процессе превращени  пиролюзита в браунит с последующей обработкой последнего хлором в водной среде, что ведет к достаточно полному использованию марганцевой руды.A method is proposed for producing manganese dioxide suitable as a depot, based on a preliminary process of converting pyrolusite to brown, with subsequent treatment of the latter with chlorine in an aqueous medium, which leads to a fairly complete use of manganese ore.

Предлагаемый способ в целом сводитс  к следующему.The proposed method generally boils down to the following.

Природный пиролюзит подвергаетс  восстановлению или термической диссо-циации, причем образуетс  браунит и частично гаусманнт .Natural pyrolusite is subjected to reduction or thermal dissociation, with brownite and, in part, hausmanth being formed.

МпОа -+ МпаОд -+ МпзО4 Процесс восстановлени  руды восстановительными газами; протекает при тем пературе 250° в течение часов. В результате-, этой реакции получаетс  браунит с примесью гаусманита.MpOa - + MpAOD - + MpzO4 The process of ore reduction by reducing gases; proceeds at a temperature of 250 ° for hours. As a result, this reaction produces brownish with an admixture of hausmanite.

Браунит получаетс  и при термической диссоциации руды, дл  чего пеобходимо нагревать ее при 750 в течение трех часов или же при 1000-1050° в течение 5-10 минут. Обожженный или восстановленньп продукт размалываетс  до частиц 100 мещ и подвергаетс  воздействию газообразного хлора в водной среде прн Т ; Ж 1 : 3,5.Braunite is also obtained during thermal dissociation of ore, for which it is necessary to heat it at 750 for three hours or at 1000-1050 ° for 5-10 minutes. The calcined or reconstituted product is milled to a particle size of 100 mes and is exposed to chlorine gas in an aqueous medium; G 1: 3,5.

Гидрат марганца, полученный из бедных руд, сначала окисл етс  до браунита на воздухе лрн 120°, а потом подвергаетс  процессу хлорировани .Manganese hydrate, obtained from poor ores, is first oxidized to braunite in air of lrn 120 °, and then subjected to the chlorination process.

Температура хлорировани  восстановленной руды около 75°, а обожженной при высоких температурах - 75-85°.The chlorination temperature of the reduced ore is about 75 °, and calcined at high temperatures is 75-85 °.

Весь процесс окислени  продолжаетс  3-5 часов.The entire oxidation process lasts 3-5 hours.

В результате предлагаемой обработки низщих окислов марганца газообразным хлором получаетс  активна  двуокись марганца со свойствами, необходимыми, дл  элементной промышленности.As a result of the proposed treatment of low manganese oxides with chlorine gas, active manganese dioxide with the properties necessary for the elemental industry is obtained.

Готовый продукт отмывают от ионов хлора; при этом в раствор переходит только около 15% марганца , а преобладающа  часть марганца из браунпта или : аусмапнта upeiipaiuacTcst к активную двуо:кись марганца. Предмст изобретени  затора, 1(рслва;)1ггс-лы1ым: преврКщспием пиролюзита н браупит, о т л и ч а ю щ i-ii с   тем, что брау нодвергают окнслению хлороуThe finished product is washed from chlorine ions; at the same time, only about 15% of manganese passes into the solution, and the predominant part of manganese from Braunpt or: Ausmapnt upeiipaiuacTcst to the active two-way manganese. Prevention of the invention of the mash, 1 (rlva;) 1ggs-ly1ym: transform pyrolusite and bout, about tl and h and ii ii with the fact that the br

SU414-44A 1944-05-29 1944-05-29 The method of producing manganese dioxide SU65522A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU414-44A SU65522A1 (en) 1944-05-29 1944-05-29 The method of producing manganese dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU414-44A SU65522A1 (en) 1944-05-29 1944-05-29 The method of producing manganese dioxide

Publications (1)

Publication Number Publication Date
SU65522A1 true SU65522A1 (en) 1944-11-30

Family

ID=48245768

Family Applications (1)

Application Number Title Priority Date Filing Date
SU414-44A SU65522A1 (en) 1944-05-29 1944-05-29 The method of producing manganese dioxide

Country Status (1)

Country Link
SU (1) SU65522A1 (en)

Similar Documents

Publication Publication Date Title
SU65522A1 (en) The method of producing manganese dioxide
US1986509A (en) Process for making magnesium hydroxide
GB1008676A (en) Improvements in and relating to the manufacture of titanium dioxide
Gump et al. Preparation and analysis of barium ferrate (VI)
GB1196494A (en) Process for the Production of Ferric Oxide
US2397430A (en) Process of developing pigment properties of titanium dioxide
GB455734A (en) Process for the absorption, in highly-concentrated nitric acid, of nitrous gases formed by the combustion of ammonia
JPS605533B2 (en) Process for producing substantially vanadium-free chromate
GB597824A (en) Method of manufacture of depolarizing manganese dioxides
US1592480A (en) Process for the production of alkali-earth metal permanganates
GB829093A (en) Recovery of uranium by precipitation as peroxide
GB1040661A (en) A method of producing lithium fluoride
US2368481A (en) Production of calcium chromate
GB814688A (en) The production of manganese hydroxide
GB717938A (en) Improvements in or relating to the manufacture of red iron oxides
GB181719A (en) Process for making prussian blue, starting from coal gas
GB625649A (en) Improved process of producing magnesium sulphate
GB765514A (en) Process for the purification of diphenylol propane
GB422080A (en) Improvements in or relating to the manufacture of aluminium fluoride
SU77110A2 (en) The method of obtaining the absorbent for the extraction of sulfur dioxide from industrial gases
GB629313A (en) Improvements in and relating to the manufacture of chlorine
GB367525A (en) Improvements in process for the production of aluminium oxide from aluminium nitrate, in which the decomposition of nitric acid is reduced to a minimum
GB417276A (en) Improvements in or relating to processes for the recovery of sulphur from sulphide ores
US1918941A (en) Method of producing nitrates
GB719099A (en) Purification of caustic alkali liquor