SU386018A1 - - Google Patents
Info
- Publication number
- SU386018A1 SU386018A1 SU1702550A SU1702550A SU386018A1 SU 386018 A1 SU386018 A1 SU 386018A1 SU 1702550 A SU1702550 A SU 1702550A SU 1702550 A SU1702550 A SU 1702550A SU 386018 A1 SU386018 A1 SU 386018A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- slag
- consumption
- calcium
- depletion
- coke
- Prior art date
Links
- 239000002893 slag Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 6
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 4
- 229910052683 pyrite Inorganic materials 0.000 description 4
- 239000011028 pyrite Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229940043430 calcium compound Drugs 0.000 description 3
- 150000001674 calcium compounds Chemical class 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 3
- 238000009856 non-ferrous metallurgy Methods 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical class [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000004579 marble Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 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
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- APVPOHHVBBYQAV-UHFFFAOYSA-N n-(4-aminophenyl)sulfonyloctadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(=O)NS(=O)(=O)C1=CC=C(N)C=C1 APVPOHHVBBYQAV-UHFFFAOYSA-N 0.000 description 1
- XIKYYQJBTPYKSG-UHFFFAOYSA-N nickel Chemical compound [Ni].[Ni] XIKYYQJBTPYKSG-UHFFFAOYSA-N 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
СПОСОБ ОБЕДНЕНИЯ ШЛАКОВ ВОССТАНОВИТЕЛЬНОСУЛЬФИДИРУЮЩЕЙ ПЛАВКОЙMETHOD OF SLOOTING SLAGS OF RESTORING SULPHIDING FUSION
1one
Изобретение отно:ситс к области цветной металлургии и, в частности, к способам обеднени шлакой цветной металлургии;The invention relates: to the field of non-ferrous metallurgy and, in particular, to the methods of depletion of slag from non-ferrous metallurgy;
Известен способ обеднени шлаков цветной металлургии восстановительно-сульфидЕрующей плавкой с применением сульфидизатора (пирит), коксика и соединений .кальци (окись кальци ), 1СО:Провождающийс высоким .расходом сульфидизатора.The known method of depletion of slags of non-ferrous metallurgy with a sulphide-reducing smelting using a sulphidizer (pyrite), coke and calcium (calcium oxide) compounds, 1CO: Conducted with high sulphidizer consumption.
П,ре|Дложенный способ отличаетс тем, что сульфидизатор, коксик « соединени кальци ввод т в шлак при температуре 1150-1350°С при .весовом соотношении (1-2) : (0,2-0,4) : 1, что позвол ет снизить расход сульфидизатора в 1,5-2 ,pa3ai. Снижение расхода колчедана и повышение степени использо;ва;ни серы достигают 1путем обработки шлака смесью, содержаш ,ей пи,рит, восстановитель .и карбонат кальци . При ЭТО.М карбонат кальци IB П рисутствии , мину стадию диссоциациИ, перехо.дит :в сульфид ,кальи.и , св зы.ва часть летучей серы, что не д.о.стигаетс п-ри стадиальной обработке шлака указан1ными .компонентами . Этот процесс осуш,ест:вл ет1с без дополнительных зат1рат тепла в ш.ир0ком интервале темларатур и соотношений реагентов.P, re | The added method is characterized in that the sulphidization, coking of the calcium compound is introduced into the slag at a temperature of 1150-1350 ° C with a weight ratio of (1-2): (0.2-0.4): 1, that allows you to reduce the consumption of sulfidization 1.5-2, pa3ai. Reducing the consumption of pyrites and increasing the degree of utilization; sulfur does not reach by means of treating the slag with a mixture containing py, rit, reducing agent, and calcium carbonate. At THIS .M calcium carbonate IB Presence, mine dissociation stage, goes into: sulphide, calium, and bonds in a part of volatile sulfur, which is not attained by slag processing of the indicated components. This process is drying, eating: it is 1 s without additional heat consumption in the air gap of the temperature and the ratios of the reactants.
Обеднение шлака осушествл ют путем загрузки на по;верх.ность шлакового расплава, имеющего температуру 1150-1350°С, предварительно перемешанной смеси указанных ко.мпонентов . Способ позвол ет повысить степень использовани пиритной серы до 70-75%. Более низка в сравнении с окисью кальци стоимость ка.рбоната ц возможность применени различных отходов производства, содержащих мрамор, известп к, доломит и др., снижают затраты на обеднение о лаков.The depletion of slag is accomplished by loading on to; the upper part of a slag melt having a temperature of 1150–1350 ° C, a pre-mixed mixture of the specified components. The method allows to increase the degree of utilization of pyrite sulfur to 70-75%. Compared to calcium oxide, the cost of carbonate is lower. The possibility of using various industrial wastes containing marble, limestone, dolomite, etc., reduces the cost of depletion of varnishes.
Пример. Конверте,рный шлак никелевого производства, содержащий 0,5-0,8% Ni и 0,2-0,4% Со, обедн ют в электропечи восстано;витель )по-сульфидирующей смесью, состо щей из лнрита, отсева, об.разующегос при дроблении мрамора и коксика. Крупность компонентов минус 20 мм, весовое отношение (1-2) : 1 : (0,25-0,4). При расходе смесиExample. An envelope, a nickel nickel production slag, containing 0.5-0.8% Ni and 0.2-0.4% Co, is depleted in an electric furnace (reducer); the driver) is a sulphidizing mixture consisting of lrith, screening, vol. razobuegos when crushing marble and coke. The size of the components is minus 20 mm, the weight ratio (1-2): 1: (0.25-0.4). At a mix consumption
15-20% от веса шлака степень использовани пиритной серы достигает 70-75%, расход колчедана уменьшаетс IB 1,5-2 раза. Извлечение металло.В в штейн составл ет: никел - 96-98%, кобальта -75-80%. Одновременно15-20% by weight of slag, the degree of utilization of pyrite sulfur reaches 70-75%, the pyrite consumption is reduced by IB 1.5-2 times. Metal recovery. In matte is: nickel - 96-98%, cobalt -75-80%. At the same time
снижаетс расход электроэнергии на 5,0-7,0% и коксика на 10-20%. 34electricity consumption is reduced by 5.0-7.0% and coke by 10-20%. 34
Предмет изобретени отличающийс тем, что, с целью сокращеви Способ обеднени шлаков восстановительно- сик и соединени кальци ввод т в шлак три сульфидирующей плавкой с применением суль- температуре 1150-1350°С .при весовом соотфидизаторов , коксика и соединений кальци , 5 ношении (1-2) : (0,2-0,4) : 1.The subject matter of the invention is that, in order to reduce the amount of slag depletion, reducing and calcium compounds are introduced into the slag three by sulphidizing smelting using a sulf temperature of 1150-1350 ° C., By weight of co-oxidizers, coke and calcium compounds, 5 wearing (1 -2): (0,2-0,4): 1.
S&SOiS S & SOiS
расхода сульфидизато1ра, сульфидизаторы, кокsulfidisatom consumption, sulfidization, coc
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1702550A SU386018A1 (en) | 1971-10-04 | 1971-10-04 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1702550A SU386018A1 (en) | 1971-10-04 | 1971-10-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU386018A1 true SU386018A1 (en) | 1973-06-14 |
Family
ID=20489488
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1702550A SU386018A1 (en) | 1971-10-04 | 1971-10-04 |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU386018A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2195508C1 (en) * | 2001-05-31 | 2002-12-27 | Закрытое акционерное общество "Производственно-творческое предприятие "Резонанс" | Method of complex processing of slags of copper- smelting process |
-
1971
- 1971-10-04 SU SU1702550A patent/SU386018A1/ru active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2195508C1 (en) * | 2001-05-31 | 2002-12-27 | Закрытое акционерное общество "Производственно-творческое предприятие "Резонанс" | Method of complex processing of slags of copper- smelting process |
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