RU2186020C2 - Method of sulfur production - Google Patents
Method of sulfur production Download PDFInfo
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- RU2186020C2 RU2186020C2 RU99119653/12A RU99119653A RU2186020C2 RU 2186020 C2 RU2186020 C2 RU 2186020C2 RU 99119653/12 A RU99119653/12 A RU 99119653/12A RU 99119653 A RU99119653 A RU 99119653A RU 2186020 C2 RU2186020 C2 RU 2186020C2
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- Prior art keywords
- sulfur
- solution
- sulfite
- sulfide
- production
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- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 229910052717 sulfur Inorganic materials 0.000 title claims abstract description 21
- 239000011593 sulfur Substances 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title abstract description 7
- 239000000243 solution Substances 0.000 claims abstract description 17
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims abstract description 14
- YALHCTUQSQRCSX-UHFFFAOYSA-N sulfane sulfuric acid Chemical compound S.OS(O)(=O)=O YALHCTUQSQRCSX-UHFFFAOYSA-N 0.000 claims abstract description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 10
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 7
- JQYCSHXHVCKLGB-UHFFFAOYSA-N S.OS(O)=O Chemical compound S.OS(O)=O JQYCSHXHVCKLGB-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 5
- 239000012670 alkaline solution Substances 0.000 claims abstract description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 13
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 3
- 229910021626 Tin(II) chloride Inorganic materials 0.000 abstract 1
- 230000000694 effects Effects 0.000 abstract 1
- 230000020477 pH reduction Effects 0.000 abstract 1
- AXZWODMDQAVCJE-UHFFFAOYSA-L tin(II) chloride (anhydrous) Chemical compound [Cl-].[Cl-].[Sn+2] AXZWODMDQAVCJE-UHFFFAOYSA-L 0.000 abstract 1
- 238000000605 extraction Methods 0.000 description 5
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 4
- 229910052711 selenium Inorganic materials 0.000 description 4
- 239000011669 selenium Substances 0.000 description 4
- 229910052714 tellurium Inorganic materials 0.000 description 4
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAAXRTPGRLVPFH-UHFFFAOYSA-N [Bi].[Cu] Chemical compound [Bi].[Cu] QAAXRTPGRLVPFH-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- ZETCGWYACBNPIH-UHFFFAOYSA-N azane;sulfurous acid Chemical class N.OS(O)=O ZETCGWYACBNPIH-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 229940059867 sulfur containing product ectoparasiticides Drugs 0.000 description 1
- 125000000101 thioether group Chemical group 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
Изобретение относится к способам получения серы из раствора, содержащего сульфидную, сульфитную и сульфатную серу. The invention relates to methods for producing sulfur from a solution containing sulfide, sulfite and sulfate sulfur.
В частности, из водных растворов, полученных при переработке руд и шламов металлургического производства, содержащих элементарную, сульфидную, сульфитную и сульфатную серу. In particular, from aqueous solutions obtained in the processing of ores and sludges of metallurgical production containing elemental, sulfide, sulfite and sulfate sulfur.
Известен способ получения элементарной серы из водного раствора, содержащего сульфиты, бисульфиты аммония, щелочных или щелочноземельных металлов, путем обработки восстанавливающим агентом при 20-150oС и давлении, достаточно высоком для предотвращения перехода жидкости в пар. Обработку ведут в две ступени. В качестве катализатора используют серу, полисульфитные соединения, растворимые в воде сульфиды, водород, угарный газ или их смесь (Патент США 3728439, опубл. 17.04.1973) (1).A known method of producing elemental sulfur from an aqueous solution containing sulfites, ammonium bisulfites, alkali or alkaline earth metals, by treatment with a reducing agent at 20-150 o C and a pressure high enough to prevent the transition of liquid into steam. Processing is carried out in two stages. Sulfur, polysulfite compounds, water-soluble sulfides, hydrogen, carbon monoxide or a mixture thereof are used as a catalyst (US Patent 3,728,439, publ. 04/17/1973) (1).
Наиболее близким является способ получения элементарной серы из щелочного раствора, полученного при переработке твердого остатка от кислотного выщелачивания медно-висмутового концентрата после извлечения из него селена и теллура путем обработки его восстановителем (патент РФ RU 2097316 С1, опубл. 27.11.1997 (2). The closest is the method of producing elemental sulfur from an alkaline solution obtained by processing the solid residue from acid leaching of copper-bismuth concentrate after extracting selenium and tellurium from it by treating it with a reducing agent (RF patent RU 2097316 C1, publ. 11/27/1997 (2).
Недостатком этого способа является то, что этот метод не позволяет извлечь сульфатную серу и требует предварительного извлечения селена и теллура, а в качестве исходного сырья используется только медно-висмутовый концентрат и при этом скорость реакции извлечения сульфидной и сульфитной серы низкая. The disadvantage of this method is that this method does not allow the extraction of sulfate sulfur and requires preliminary extraction of selenium and tellurium, and only copper-bismuth concentrate is used as a feedstock, and the reaction rate for the extraction of sulfide and sulfite sulfur is low.
Целью изобретения является получение серы из раствора,содержащего сульфатную серу наряду с сульфидной и сульфитной серой без предварительного удаления селена и теллура, кроме того, увеличение скорости реакции получения серы из ее сульфидных и сульфитных соединений. The aim of the invention is to obtain sulfur from a solution containing sulfate sulfur along with sulfide and sulfite sulfur without prior removal of selenium and tellurium, in addition, an increase in the reaction rate of sulfur production from its sulfide and sulfite compounds.
Указанная цель достигается дополнительным введением пероксида водорода в раствор, содержащий сульфатную, сульфидную и сульфитную серу. Заявленный способ позволяет извлечь сульфатную серу наряду с сульфитной и сульфидной с предварительным и без предварительного извлечения селена и теллура. В качестве исходного сырья может быть любой серосодержащий материал, из которого можно извлечь серу по заявленному способу. This goal is achieved by the additional introduction of hydrogen peroxide in a solution containing sulfate, sulfide and sulfite sulfur. The claimed method allows to extract sulfate sulfur along with sulfite and sulfide with preliminary and without preliminary extraction of selenium and tellurium. The source of raw materials can be any sulfur-containing material from which sulfur can be extracted by the claimed method.
Способ осуществляется следующим образом. The method is as follows.
При обработке руд, содержащих элементарную, сульфидную, сульфитную, и сульфатную серу минеральными кислотами (HCl, H2SO4, HNO3) (независимо от исходного состава полиметаллической руды), в результате реакции с серосодержащими продуктами, в зависимости от различных ситуаций, зачастую образуется элементарная сера, которая затем переходит в твердую фазу.When processing ores containing elemental, sulfide, sulfite, and sulfate sulfur with mineral acids (HCl, H 2 SO 4 , HNO 3 ) (regardless of the initial composition of polymetallic ore), as a result of reaction with sulfur-containing products, depending on various situations, often elemental sulfur is formed, which then passes into the solid phase.
1) SO2 + 2Н2S = 3S + 2Н2O
2) 6HCl + Н2SO4 (при концентрации более 80%) = 3Сl2 + 4H2O + S
3) HClO + H2S = HCl + S + Н2О
4) H2S + Cl2 = 2HCl + S
5) H2S + 2HNO3 = S + 2NO2 + 2Н2О
Затем твердую фазу или материал, содержащий указанные виды серы, обрабатывают концентрированным раствором щелочи при t=150-200oС.1) SO 2 + 2H 2 S = 3S + 2H 2 O
2) 6HCl + H 2 SO 4 (at a concentration of more than 80%) = 3Cl 2 + 4H 2 O + S
3) HClO + H 2 S = HCl + S + H 2 O
4) H 2 S + Cl 2 = 2HCl + S
5) H 2 S + 2HNO 3 = S + 2NO 2 + 2H 2 O
Then the solid phase or material containing these types of sulfur is treated with a concentrated alkali solution at t = 150-200 o C.
6) 3S + 6NaOH = Na2SO3 + 2Na2S + 3H2O.6) 3S + 6NaOH = Na 2 SO 3 + 2Na 2 S + 3H 2 O.
В результате реакции сера переходит в сульфитную и сульфидную форму. Такой раствор зачастую содержит и сульфатную серу. Для получения серы из всех перечисленных форм в щелочной раствор подкисляют соляной кислотой до рН 3-4 и вводят в него востановитель SnCl2 до 10 мас.% от общего содержания серы в растворе.As a result of the reaction, sulfur transforms into a sulfite and sulfide form. Such a solution often also contains sulfate sulfur. To obtain sulfur from all of these forms, the alkaline solution is acidified with hydrochloric acid to pH 3-4 and the SnCl 2 reducing agent is introduced into it to 10 wt.% Of the total sulfur content in the solution.
Для того чтобы извлечь сульфатную серу и наряду с этим увеличить скорость реакции извлечения сульфитной и сульфидной серы в раствор, дополнительно вводят пероксид водорода. Последнее наглядно видно из оценки констант равновесия реакции (7) и (8) в соответствии с законом действующих масс. В частности, оценка отношения реакции аналога к скорости предлагаемой реакции составляет величину порядка Ехр(145). Расчеты констант равновесия реакции проводились на основании термодинамических данных справочника (3):
7) Na2SO3*2Na2S + 8HCl + SnCl2 = 6NaCl + 3S + SnCl4 + 4H2O.In order to extract sulfate sulfur and at the same time increase the reaction rate of extraction of sulfite and sulfide sulfur into the solution, hydrogen peroxide is additionally introduced. The latter is clearly seen from the estimate of the equilibrium constants of reaction (7) and (8) in accordance with the law of mass action. In particular, an estimate of the ratio of the analogue reaction to the rate of the proposed reaction is of the order of Exp (145) . The calculation of the equilibrium constants of the reaction was carried out on the basis of the thermodynamic data of the handbook (3):
7) Na 2 SO 3 * 2Na 2 S + 8HCl + SnCl 2 = 6NaCl + 3S + SnCl 4 + 4H 2 O.
Скорость реакции аналогичного способа:
V' = Kp'[Na2SO3*2Na2S] • [HCl]8 • [SnCl2]
8) Na2SО3*2Na2S + 4H2O2 + 14HCl + 4SnCl2 = NaCl + 3S + 4SnCl4 + 11H2O
Скорость реакции предлагаемого способа:
V'' = Kp''[Na2SO3*2Na2S] • [H2O2]4 • [HCl]14 • [SnCl2]4
9) Na2SО4 + H2O2 + 4SnCl2 + 10HCl = S + 6H2O + 4SnCl4 + 2NaCl
Описанный метод был опробирован в шеелитовом и молибденовом концентратах.The reaction rate of a similar method:
V '= K p ' [Na 2 SO 3 * 2Na 2 S] • [HCl] 8 • [SnCl 2 ]
8) Na 2 SO 3 * 2Na 2 S + 4H 2 O 2 + 14HCl + 4SnCl 2 = NaCl + 3S + 4SnCl 4 + 11H 2 O
The reaction rate of the proposed method:
V '' = K p '' [Na 2 SO 3 * 2Na 2 S] • [H 2 O 2 ] 4 • [HCl] 14 • [SnCl 2 ] 4
9) Na 2 SO 4 + H 2 O 2 + 4SnCl 2 + 10HCl = S + 6H 2 O + 4SnCl 4 + 2NaCl
The described method was tested in scheelite and molybdenum concentrates.
На рудах Радужного и Карачаево-Черкесского месторождений, на искусственных смесях. После извлечения серы указанные виды серы в растворе не обнаруживаются качественными реакциями. On the ores of the Rainbow and Karachay-Cherkess deposits, on artificial mixtures. After sulfur recovery, these types of sulfur in the solution are not detected by qualitative reactions.
Литература:
1. US, патент, 3728439, кл. С01 В 17/02,1973.Literature:
1. US patent 3728439, cl. C01 B 17/02/1973.
2. Патент РФ 2097316 - прототип. 2. RF patent 2097316 - prototype.
3. Рябин В.А. и др. Термодинамические свойства веществ. Справочник. - М. : Химия, 1977. 3. Ryabin V.A. et al. Thermodynamic properties of substances. Directory. - M.: Chemistry, 1977.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU99119653/12A RU2186020C2 (en) | 1999-09-13 | 1999-09-13 | Method of sulfur production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU99119653/12A RU2186020C2 (en) | 1999-09-13 | 1999-09-13 | Method of sulfur production |
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| Publication Number | Publication Date |
|---|---|
| RU99119653A RU99119653A (en) | 2001-08-10 |
| RU2186020C2 true RU2186020C2 (en) | 2002-07-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| RU99119653/12A RU2186020C2 (en) | 1999-09-13 | 1999-09-13 | Method of sulfur production |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3728439A (en) * | 1970-11-05 | 1973-04-17 | Universal Oil Prod Co | Treatment of a sulfite containing aqueous steam to selectively produce elemental sulfur |
| FR2422588A1 (en) * | 1978-04-10 | 1979-11-09 | Cyprus Metallurg Process | PROCESS FOR RECOVERING ELEMENTARY SULFUR AND METALS FROM CONCENTRATES OR RESIDUES OF COPPER SULPHIDE ORES |
| DE3713088A1 (en) * | 1986-04-17 | 1987-10-22 | Elf Aquitaine | IMPROVED METHOD FOR THE EXTRACTION OF SULFUR FROM OXIDATED ORES |
| WO1995015918A1 (en) * | 1993-12-09 | 1995-06-15 | N.V. Union Miniere S.A. | Method for recovering sulphur from ores |
| RU2069172C1 (en) * | 1992-07-24 | 1996-11-20 | Институт теоретических проблем химической технологии | Process for preparing sulfur and hydrogen |
| RU2097316C1 (en) * | 1993-06-18 | 1997-11-27 | Научно-техническое бюро "Экос" | Method of producing sulfur from an aqueous solution of inorganic sulfur compounds |
| US9440026B2 (en) * | 2008-08-13 | 2016-09-13 | Owen Mumford Limited | Autoinjection devices |
-
1999
- 1999-09-13 RU RU99119653/12A patent/RU2186020C2/en not_active IP Right Cessation
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3728439A (en) * | 1970-11-05 | 1973-04-17 | Universal Oil Prod Co | Treatment of a sulfite containing aqueous steam to selectively produce elemental sulfur |
| FR2422588A1 (en) * | 1978-04-10 | 1979-11-09 | Cyprus Metallurg Process | PROCESS FOR RECOVERING ELEMENTARY SULFUR AND METALS FROM CONCENTRATES OR RESIDUES OF COPPER SULPHIDE ORES |
| DE3713088A1 (en) * | 1986-04-17 | 1987-10-22 | Elf Aquitaine | IMPROVED METHOD FOR THE EXTRACTION OF SULFUR FROM OXIDATED ORES |
| RU2069172C1 (en) * | 1992-07-24 | 1996-11-20 | Институт теоретических проблем химической технологии | Process for preparing sulfur and hydrogen |
| RU2097316C1 (en) * | 1993-06-18 | 1997-11-27 | Научно-техническое бюро "Экос" | Method of producing sulfur from an aqueous solution of inorganic sulfur compounds |
| WO1995015918A1 (en) * | 1993-12-09 | 1995-06-15 | N.V. Union Miniere S.A. | Method for recovering sulphur from ores |
| US9440026B2 (en) * | 2008-08-13 | 2016-09-13 | Owen Mumford Limited | Autoinjection devices |
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