SU106836A1 - The method of obtaining magnesium oxide for high refractories - Google Patents
The method of obtaining magnesium oxide for high refractoriesInfo
- Publication number
- SU106836A1 SU106836A1 SU552235A SU552235A SU106836A1 SU 106836 A1 SU106836 A1 SU 106836A1 SU 552235 A SU552235 A SU 552235A SU 552235 A SU552235 A SU 552235A SU 106836 A1 SU106836 A1 SU 106836A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- magnesium
- magnesium oxide
- obtaining magnesium
- oxide
- refractories
- Prior art date
Links
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 title description 13
- 239000000395 magnesium oxide Substances 0.000 title description 9
- 238000000034 method Methods 0.000 title description 8
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 title description 5
- 239000011819 refractory material Substances 0.000 title description 2
- 239000000243 solution Substances 0.000 description 9
- 239000000203 mixture Substances 0.000 description 7
- 239000010440 gypsum Substances 0.000 description 6
- 229910052602 gypsum Inorganic materials 0.000 description 6
- 239000012267 brine Substances 0.000 description 5
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 5
- 239000001095 magnesium carbonate Substances 0.000 description 5
- 235000014380 magnesium carbonate Nutrition 0.000 description 5
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 5
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 5
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 4
- 238000003763 carbonization Methods 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical class [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 3
- 235000012255 calcium oxide Nutrition 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 241001137251 Corvidae Species 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- QWDJLDTYWNBUKE-UHFFFAOYSA-L magnesium bicarbonate Chemical compound [Mg+2].OC([O-])=O.OC([O-])=O QWDJLDTYWNBUKE-UHFFFAOYSA-L 0.000 description 2
- 239000002370 magnesium bicarbonate Substances 0.000 description 2
- 229910000022 magnesium bicarbonate Inorganic materials 0.000 description 2
- 235000014824 magnesium bicarbonate Nutrition 0.000 description 2
- 159000000003 magnesium salts Chemical class 0.000 description 2
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 2
- 235000019341 magnesium sulphate Nutrition 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000009950 felting Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
Окись f;iritHJi, получаема из Природных магпезитоп (например прокалкой саткппского магнезита), содержит 1--, окиси кальци , что снижает срок службы изготовл емых из иее магпезиальиых огнеупорных изде,1И11.Oxide f; iritHJi, obtained from natural magpezitop (for example, by calcining satkapp magnesite), contains 1--, calcium oxides, which reduces the service life of the magpezial refractory articles manufactured from it, 1И11.
Предлагаетс способ получеин окиси магпи из сиван1ской рапы, (;беспечиваюи111Й более ntiicoKyto чистоту окиси . Кроме того, реа .чизаци этого способа позвол ет, обеспечить южпые районы страны местным (ысококмчсстиенП1 ,гм продуктом, необходимым д.ы метал.;|ургической промьипленпости.A method of obtaining papine oxide magpi from Sivania brine ((; ensuring more ntiicoKyto purity of oxide) is proposed. In addition, the refinement of this method allows the southern regions of the country to be local (a very high product, necessary for the use of metal;);
Стюсоб получени окиси магни из рапы Сиваи1а путем обработки ее пзвестыо по обычному методу приводит к целому ) ду затруднеП1ПТ . Сива1нска рапа содержит сульфаты, и это пргпшднт при обработке ее изгчестьк) к выделению гипса , загр зн ющего окись магни (вызываетс необходимость предварительной десульфатизации рапы); следует примен ть чистый исходный известн к и его высококачественный обжиг (дл уменыиепи содержани окиси кальци в конечном продукте до миинмума); при отмывке гндроокнси магни от балластных солей она загр зн етс карГюнлтом кальци .The production of magnesium oxide from Sivai1a by treating it well by the usual method results in a whole harder than 1PT. Siva1nska brine contains sulphates, and this is carried out by processing its extracts) to the release of gypsum contaminating magnesium oxide (the preliminary desulfation of the brine is required); one should use pure initial limestone and its high-quality calcination (to reduce the calcium oxide content in the final product to minimum); when washing gndrooknsi magnesium from ballast salts, it is contaminated with cargunlt calcium.
Все эти осложнени устран ютс применением простого приема карбонизации гипсомагнезнальной смесн в растворе 11,5%-ного сульфата магип , преЛотвран1аюн;его переход гипса в карбонат.All of these complications are eliminated by using a simple technique of carbonating a hypomagnesnal mixture in a solution of 11.5% sulfate slug, preferred, and its conversion of gypsum to carbonate.
Суниюсть предлагаемого способа состоит в следу1ОП1ем.The sunshine of the proposed method consists in the following.
Из р;иП) известковым мо.ппком осаждаютгннсома1незнальпук)From the p; IP) with a lime mob.
смесь, которую подвергают ка1эбопизации топочными газамн известковых HC4eii.a mixture that is subjected to felting the flue gases of calcareous HC4eii.
При карбонизации в раствор переходит бикарбонат магни , а гипс осаждаетс . Дл предупрежделн карбопнзацип гипса, карбонизации подвергают гппсомагнезиальную смесь, диспергированную в 11,5%иом растворе сульфата магни .During carbonization, magnesium bicarbonate goes into solution, and gypsum precipitates. For the prevention of carpaceous gypsum, carbonaceous mixture dispersed in a 11.5% solution of magnesium sulfate is subjected to carbonization.
Из раствора осповиой карбонат магни выдел ют пли путем нагрева жидкости до кипени , или обработкой возвратной окисью магпи . Выделенный продукт отфильтровывают , сушат и прока;1ивают. Гипс, поучаемый в качестве отхода, используетс .дл различных целей.Magnesium carbonate is separated from the solution by precipitation by heating the liquid to a boil, or by treating back to magpi. The isolated product is filtered, dried and rolled; 1. Gypsum, taught as waste, is used for various purposes.
И предлаглемом способе получени окиси магни из сивашской рапы может быть использована рапа любой когщептрации, без предварительной ее десульфатнзации, а также обычна строительпа нзвесь.And the proposed method of obtaining magnesia from Sivash brine can be used with brine of any kind, without prior desulfating it, as well as with ordinary builders.
Оптимальные услови процесса получени окиси магни заключаютс в иоследооателышм проведе1ГИИ следуюни1х операций:The optimal conditions for the production of magnesia are in the subsequent experiment carried out by the following operations:
1.Получение гинсомагпезиальной смеси.1. Getting ginsomagpezialnoy mixture.
2.Диспергирование гипсомагпезнальной парты, приводимое в растворе сульфата магни , содоржаИ1 ,ри 11,Г, (V, при 1Ч)дорЖ(И1И1Г м пульпе 3-3,5% Mg(Oll),j м гкфесчете па MgO. При этом выход иролукта в жидкую фазу составл ет 87-90% при давле1П1п 100%-ного углекислого газа в 3 ати нли 40%ного газа 7,5 ати. Длительность карбонизации в указанных услови х составл ет 25-30 минут, в течение которых в жидкую фазу переходит около 85% магни , и концентраци карбрйата магни составл ет 30- 35 г/л в пересчете на MgO.2.Dispersion of the hypomagical-desolate party, given in a solution of magnesium sulphate, SODI, RI 11, G, (V, at 1H) expensive (I1I1G m pulp 3-3.5% Mg (Oll), j mg Festochet PA MgO. The yield The liquid phase in the liquid phase is 87-90% at a pressure of 100% carbon dioxide in 3 atm of 40% gas at 7.5 at. The duration of carbonization under these conditions is 25-30 minutes, during which the liquid phase about 85% of magnesium is transferred, and the concentration of magnesium carbonate is 30-35 g / l in terms of MgO.
3.Выделепие основного карбоната магни путем 30-минутного кии . чени бпкарбонатного раствора при подаче и него острого пара.3. The release of basic magnesium carbonate by a 30-minute cue. bicarbonate solution when it is injected and in direct steam.
4.Фильтрование, сушка и прокалка карбоната магни в типовой аппаратуре известным способом.4. Filtration, drying and calcining of magnesium carbonate in a typical apparatus in a known manner.
Предметизобретени Subject matter
Способ получе 1и окиси магни дл высокоогнеупоров из природных сульфатных растворов солей магни нуюм осаждени из УТИХ растворов га1неной известью смеси гидроокиси магни и сул11фатп кальци , послсду| Л1и . )иилаци1( t пмспмагис:5И;1льпой смеси до получени растворимого бикарбоната магни и иеревода его нагреванием в основные соли магни , отличающийс тем, что, с целью иредртвращени карбонизации гипса и получени окиси магни , содержащей до 1% окиси кальци , гипсомагнезиальную смесь подвергают карбонизации в растворе, содержащем 11,5% сульфата магии .The method of obtaining 1 and magnesium oxide for high-refractories from natural sulphate solutions of magnesium salts, precipitating from UTIC solutions with a lime with a mixture of magnesium hydroxide and calcium sulfate, after | L1i. ) Silica1 (t pmspmagis: 5I; 1spa mixture to obtain soluble magnesium bicarbonate and a tree by heating it into basic magnesium salts, characterized in that in order to prevent the carbonization of gypsum and to obtain magnesium oxide containing up to 1% of calcium oxide, the hypomagnesium mixture is carbonized in a solution containing 11.5% sulfate magic.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU552235A SU106836A1 (en) | 1956-05-16 | 1956-05-16 | The method of obtaining magnesium oxide for high refractories |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU552235A SU106836A1 (en) | 1956-05-16 | 1956-05-16 | The method of obtaining magnesium oxide for high refractories |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU106836A1 true SU106836A1 (en) | 1956-11-30 |
Family
ID=48380092
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU552235A SU106836A1 (en) | 1956-05-16 | 1956-05-16 | The method of obtaining magnesium oxide for high refractories |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU106836A1 (en) |
-
1956
- 1956-05-16 SU SU552235A patent/SU106836A1/en active
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