CN106276819A - A kind of method being catalyzed reduction selenium - Google Patents
A kind of method being catalyzed reduction selenium Download PDFInfo
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- CN106276819A CN106276819A CN201610580542.XA CN201610580542A CN106276819A CN 106276819 A CN106276819 A CN 106276819A CN 201610580542 A CN201610580542 A CN 201610580542A CN 106276819 A CN106276819 A CN 106276819A
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- 229910052711 selenium Inorganic materials 0.000 title claims abstract description 126
- 239000011669 selenium Substances 0.000 title claims abstract description 126
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 title claims abstract description 123
- 238000000034 method Methods 0.000 title claims abstract description 37
- 230000009467 reduction Effects 0.000 title claims abstract description 34
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 15
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910001447 ferric ion Inorganic materials 0.000 claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 4
- 238000009776 industrial production Methods 0.000 claims abstract description 4
- 238000006722 reduction reaction Methods 0.000 claims description 28
- -1 selenium ions Chemical class 0.000 claims description 21
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 12
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- 150000002505 iron Chemical class 0.000 claims description 4
- 239000012279 sodium borohydride Substances 0.000 claims description 4
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 4
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 3
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 3
- 229940082569 selenite Drugs 0.000 claims description 3
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 claims description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 claims description 2
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 claims description 2
- 229910000358 iron sulfate Inorganic materials 0.000 claims description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical group [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 2
- QYHFIVBSNOWOCQ-UHFFFAOYSA-N selenic acid Chemical compound O[Se](O)(=O)=O QYHFIVBSNOWOCQ-UHFFFAOYSA-N 0.000 claims description 2
- MCAHWIHFGHIESP-UHFFFAOYSA-N selenous acid Chemical compound O[Se](O)=O MCAHWIHFGHIESP-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 8
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 5
- 238000011946 reduction process Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- 229940091258 selenium supplement Drugs 0.000 description 97
- 238000001514 detection method Methods 0.000 description 19
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 15
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 15
- 239000012265 solid product Substances 0.000 description 13
- 239000007787 solid Substances 0.000 description 11
- PMYDPQQPEAYXKD-UHFFFAOYSA-N 3-hydroxy-n-naphthalen-2-ylnaphthalene-2-carboxamide Chemical compound C1=CC=CC2=CC(NC(=O)C3=CC4=CC=CC=C4C=C3O)=CC=C21 PMYDPQQPEAYXKD-UHFFFAOYSA-N 0.000 description 9
- 229960001881 sodium selenate Drugs 0.000 description 9
- 239000011655 sodium selenate Substances 0.000 description 9
- 235000018716 sodium selenate Nutrition 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- 238000002441 X-ray diffraction Methods 0.000 description 7
- 238000009616 inductively coupled plasma Methods 0.000 description 6
- 238000011084 recovery Methods 0.000 description 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 5
- 238000001914 filtration Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 5
- 229910017604 nitric acid Inorganic materials 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000002378 acidificating effect Effects 0.000 description 4
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910021642 ultra pure water Inorganic materials 0.000 description 3
- 239000012498 ultrapure water Substances 0.000 description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910001448 ferrous ion Inorganic materials 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 238000004255 ion exchange chromatography Methods 0.000 description 2
- 238000002386 leaching Methods 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 230000033116 oxidation-reduction process Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 229940065287 selenium compound Drugs 0.000 description 2
- 150000003343 selenium compounds Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 2
- 229910052714 tellurium Inorganic materials 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005363 electrowinning Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid 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
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 229940006163 selenate ion Drugs 0.000 description 1
- 229940005981 selenite ion Drugs 0.000 description 1
- MCAHWIHFGHIESP-UHFFFAOYSA-L selenite(2-) Chemical compound [O-][Se]([O-])=O MCAHWIHFGHIESP-UHFFFAOYSA-L 0.000 description 1
- 235000010265 sodium sulphite Nutrition 0.000 description 1
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B19/00—Selenium; Tellurium; Compounds thereof
- C01B19/02—Elemental selenium or tellurium
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/80—Compositional purity
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
Abstract
本发明公开了一种催化还原硒的方法,用三价铁离子为催化剂,在含六价硒的溶液中加入还原剂进行反应使硒还原成硒单质。本发明实现了短流程、直接还原为硒单质的目标,解决现有技术中采用还原剂难以一步将六价硒还原成单质硒的技术难题。本发明还实现了快速高效还原,仅需要1‑2小时的反应时间,即可实现硒还原率不低于98%,明显缩短了硒还原的时间,提高了还原率。本发明的还原过程所需条件温和、反应流程短效果好、所需试剂及设备均为常见的湿法冶金工业设备及试剂,整体非常容易实现工业化生产应用。
The invention discloses a method for catalytically reducing selenium. Ferric ions are used as a catalyst, and a reducing agent is added to a solution containing hexavalent selenium to react to reduce selenium into simple selenium. The invention realizes the goal of short process and direct reduction to simple selenium, and solves the technical problem in the prior art that it is difficult to reduce hexavalent selenium to simple selenium in one step by using a reducing agent. The present invention also realizes rapid and efficient reduction, and only needs 1-2 hours of reaction time to achieve a selenium reduction rate of not less than 98%, which obviously shortens the time for selenium reduction and improves the reduction rate. The reduction process of the present invention requires mild conditions, short reaction process and good effect, and the required reagents and equipment are all common hydrometallurgical industrial equipment and reagents, which is very easy to realize industrial production and application as a whole.
Description
技术领域technical field
本发明涉及一种催化还原硒的方法,尤其涉及一种将六价硒催化还原成单质硒的方法。The invention relates to a method for catalytically reducing selenium, in particular to a method for catalytically reducing hexavalent selenium into elemental selenium.
背景技术Background technique
据不完全统计,2013年中国硒消费量在1800吨左右,超过全球消费量的50%,其中1500多吨来源于进口,300多吨由国内铜冶炼企业生产。目前国内90%的硒产自于铜、铅阳极泥,生产硒的主要工艺有:硫酸化焙烧和苏打焙烧法,这两种工艺均采用适当的氧化气氛破坏原料中硒原有结构,使硒以单质或氧化物的形式分离,后经过收集与还原过程产生单质硒。但在氧化分离过程中,硒极易被过氧化成六价的硒化合物,这类高价硒化合物严重降低了硒回收率。According to incomplete statistics, China's selenium consumption in 2013 was about 1,800 tons, more than 50% of global consumption, of which more than 1,500 tons were imported, and more than 300 tons were produced by domestic copper smelting enterprises. At present, 90% of selenium in China is produced from copper and lead anode slime. The main processes for producing selenium are: sulfated roasting and soda roasting. It is separated in the form of elemental or oxide, and then is collected and reduced to produce elemental selenium. However, during the oxidation separation process, selenium is easily peroxidized into hexavalent selenium compounds, and such high-valent selenium compounds seriously reduce the recovery rate of selenium.
并且,随着硒鼓为代表的含硒城市矿产中硒资源回收问题日益严峻。冶炼企业对于这类复杂资源往往采用强的氧化方式将硒与原料进行分离,分离后的硒多以六价形式存在,这类六价硒的回收问题阻挠了含硒复杂城市矿产的资源综合利用。目前高价硒的回收技术主要有电积、离子交换、反渗透、光催化还原、浓盐酸蒸煮还原、金属(如铝、锌、铜)置换等。但是采用离子交换、反渗透等,在实现六价硒离子与其余杂质分离净化的过程后,仍然需要进一步的还原工序,这类还原工序主要采用浓盐酸还原、蒸发碳还原等工艺,整体来看硒回收过程长、步骤复杂,并且能耗高,产能低难以大规模产业化应用。Moreover, the problem of selenium resource recovery in selenium-containing urban minerals represented by toner cartridges is becoming increasingly serious. For such complex resources, smelting enterprises often use strong oxidation methods to separate selenium from raw materials, and the separated selenium mostly exists in the form of hexavalent selenium. The recovery of hexavalent selenium hinders the comprehensive utilization of selenium-containing complex urban mineral resources . At present, the recovery technologies of high-priced selenium mainly include electrowinning, ion exchange, reverse osmosis, photocatalytic reduction, concentrated hydrochloric acid cooking reduction, metal (such as aluminum, zinc, copper) replacement, etc. However, after ion exchange, reverse osmosis, etc. are used to separate and purify hexavalent selenium ions from other impurities, a further reduction process is still required. This type of reduction process mainly uses concentrated hydrochloric acid reduction, evaporation carbon reduction and other processes. Overall The selenium recovery process is long, complicated steps, high energy consumption, low production capacity and difficult for large-scale industrial application.
发明内容Contents of the invention
本发明所要解决的技术问题是,克服现有技术中高价硒回收的难题,提供一种简单、快速、高效的六价硒直接还原为硒单质的方法,从而降低硒资源浪费、提高硒回收率,解决我国硒资源缺乏的问题。The technical problem to be solved by the present invention is to overcome the problem of recovering high-priced selenium in the prior art and provide a simple, fast and efficient method for directly reducing hexavalent selenium to simple selenium, thereby reducing the waste of selenium resources and improving the recovery rate of selenium , to solve the problem of lack of selenium resources in my country.
为解决上述技术问题,本发明提出的技术方案为:In order to solve the problems of the technologies described above, the technical solution proposed by the present invention is:
一种催化还原硒的方法,用三价铁离子为催化剂,在含六价硒的溶液中加入还原剂进行反应使硒还原成硒单质。具体的操作方法是在含六价硒溶液中加入三价铁离子和还原剂进行反应,固液分离后得到硒单质。The invention relates to a method for catalytically reducing selenium. Ferric ions are used as catalysts, and a reducing agent is added to a solution containing hexavalent selenium for reaction to reduce selenium into simple selenium. The specific operation method is to add ferric ions and reducing agent to the solution containing hexavalent selenium to react, and obtain selenium simple substance after solid-liquid separation.
上述的催化还原硒的方法,优选的,所述三价铁离子是以可溶性铁盐的形式加入的,所述可溶性铁盐包括但不限于硫酸铁、氯化铁;所述三价铁离子的加入量为溶液中硒离子浓度含量的10%以上。The method for the above-mentioned catalytic reduction of selenium, preferably, the ferric ion is added in the form of soluble iron salt, and the soluble iron salt includes but not limited to ferric sulfate, ferric chloride; The added amount is more than 10% of the selenium ion concentration in the solution.
上述的催化还原硒的方法,优选的,所述还原剂的标准氧化还原电位低于六价硒转化为硒单质的标准氧化还原电位。还原剂的加入量为将含六价硒溶液中硒离子全部还原成硒单质的理论量的1.2倍以上。In the above method for catalytic reduction of selenium, preferably, the standard oxidation-reduction potential of the reducing agent is lower than the standard oxidation-reduction potential of hexavalent selenium converted into simple selenium. The addition amount of the reducing agent is more than 1.2 times of the theoretical amount for reducing all the selenium ions in the hexavalent selenium-containing solution to simple selenium.
上述的催化还原硒的方法,优选的,所述还原剂选自水合肼、二氧化硫、亚硫酸盐和硼氢化钠中的一种或几种。In the above method for catalytic reduction of selenium, preferably, the reducing agent is selected from one or more of hydrazine hydrate, sulfur dioxide, sulfite and sodium borohydride.
上述的催化还原硒的方法,优选的,还包括调节所述含六价硒溶液pH值的步骤:通过加入硫酸或盐酸调节含六价硒溶液pH值小于1。The above method for catalytic reduction of selenium preferably further includes the step of adjusting the pH value of the hexavalent selenium-containing solution: adjusting the pH value of the hexavalent selenium-containing solution to be less than 1 by adding sulfuric acid or hydrochloric acid.
上述的催化还原硒的方法,优选的,所述含六价硒溶液为含六价硒的硒酸或硒酸盐溶液,包括化工或冶金类科学研究或工业生产中产生的含有六价硒的溶液。In the above method for catalytic reduction of selenium, preferably, the hexavalent selenium-containing solution is a selenic acid or selenate solution containing hexavalent selenium, including selenium containing hexavalent selenium produced in chemical or metallurgical scientific research or industrial production. solution.
上述的催化还原硒的方法,优选的,所述反应的温度一般不高于100℃。In the above method for catalytic reduction of selenium, preferably, the reaction temperature is generally not higher than 100°C.
发明人在通过大量文献调研和探索实验研究后,发现三价铁离子可以用作六价硒离子还原的催化剂,使包括二氧化硫在内的一系列还原剂有效地将六价硒离子还原为硒单质,克服了二氧化硫等还原剂无法将六价硒离子还原为硒单质的技术难题。After a large amount of literature research and exploratory experimental research, the inventor found that ferric ions can be used as a catalyst for the reduction of hexavalent selenium ions, so that a series of reducing agents including sulfur dioxide can effectively reduce hexavalent selenium ions into simple selenium , overcoming the technical problem that reducing agents such as sulfur dioxide cannot reduce hexavalent selenium ions to simple selenium.
本发明利用三价铁离子的催化效应降低了六价硒还原的反应活化能,在还原过程中,还原剂首先与三价铁离子发生中间反应,生成活性亚铁离子,活性亚铁离子随后将六价硒离子还原为四价的亚硒酸离子的同时被氧化为三价铁离子复原,随后亚硒酸离子被还原剂直接还原为硒单质,从而实现了催化还原全过程。The present invention utilizes the catalytic effect of ferric ions to reduce the reaction activation energy of hexavalent selenium reduction. In the reduction process, the reducing agent first reacts with ferric ions to generate active ferrous ions, which are then converted into active ferrous ions. Hexavalent selenium ions are reduced to tetravalent selenite ions while being oxidized to ferric ions for restoration, and then the selenite ions are directly reduced to selenium by the reducing agent, thereby realizing the whole process of catalytic reduction.
与现有技术相比,本发明的优点在于:Compared with the prior art, the present invention has the advantages of:
(1)本发明实现了短流程、直接还原为硒单质的目标,解决现有技术中采用还原剂难以一步将六价硒还原成单质硒的技术难题。(1) The present invention realizes the goal of short process and direct reduction to simple selenium, and solves the technical problem that it is difficult to reduce hexavalent selenium to simple selenium in one step by using a reducing agent in the prior art.
(2)本发明实现了快速高效还原,仅需要1-2小时的反应时间,即可实现硒还原率不低于98%,明显缩短了硒还原的时间,提高了还原率。(2) The present invention realizes fast and efficient reduction, only needs 1-2 hours of reaction time, can realize selenium reduction rate not lower than 98%, obviously shortens the time of selenium reduction, improves reduction rate.
(3)本发明的还原过程所需条件温和、反应流程短效果好、所需试剂及设备均为常见的湿法冶金工业设备及试剂,整体非常容易实现工业化生产应用。(3) The reduction process of the present invention requires mild conditions, short reaction process and good effect, and the required reagents and equipment are all common hydrometallurgical industrial equipment and reagents, which is very easy to realize industrial production and application as a whole.
附图说明Description of drawings
图1为本发明实施例1还原产物的X射线衍射检测图。Figure 1 is an X-ray diffraction detection diagram of the reduction product of Example 1 of the present invention.
图2为本发明实施例1还原产物的扫描电镜检测图。Fig. 2 is a scanning electron microscope detection diagram of the reduction product of Example 1 of the present invention.
图3为本发明实施例3还原产物的X射线衍射检测图。Fig. 3 is an X-ray diffraction detection diagram of the reduction product of Example 3 of the present invention.
具体实施方式detailed description
为了便于理解本发明,下文将结合说明书附图和较佳的实施例对本文发明做更全面、细致地描述,但本发明的保护范围并不限于以下具体实施例。In order to facilitate the understanding of the present invention, the invention will be described more comprehensively and in detail below in conjunction with the accompanying drawings and preferred embodiments, but the protection scope of the present invention is not limited to the following specific embodiments.
除非另有定义,下文中所使用的所有专业术语与本领域技术人员通常理解含义相同。本文中所使用的专业术语只是为了描述具体实施例的目的,并不是旨在限制本发明的保护范围。Unless otherwise defined, all technical terms used hereinafter have the same meanings as commonly understood by those skilled in the art. The terminology used herein is only for the purpose of describing specific embodiments, and is not intended to limit the protection scope of the present invention.
除非另有特别说明,本发明中用到的各种原材料、试剂、仪器和设备等均可通过市场购买得到或者可通过现有方法制备得到。Unless otherwise specified, various raw materials, reagents, instruments and equipment used in the present invention can be purchased from the market or prepared by existing methods.
实施例1:Example 1:
一种本发明的催化还原硒的方法,具体步骤如下:A kind of method of catalytic reduction selenium of the present invention, concrete steps are as follows:
(1)将硒酸钠(Na2SeO4)用超纯水溶解配制成硒酸钠溶液,使溶液中硒含量为10g/L,然后加入硫酸调节溶液至氢离子浓度为1mol/L;(1) Sodium selenate (Na 2 SeO 4 ) was dissolved in ultrapure water to prepare a sodium selenate solution, so that the selenium content in the solution was 10 g/L, and then sulfuric acid was added to adjust the solution until the hydrogen ion concentration was 1 mol/L;
(2)取100mL步骤(1)制备的酸性硒酸钠溶液,加入硫酸铁固体后充分搅拌直至硫酸铁固体完全溶解(硫酸铁的加入量使溶液中铁离子浓度为0.5g/L);(2) Get the acidic sodium selenate solution prepared by 100mL step (1), add ferric sulfate solid and fully stir until ferric sulfate solid dissolves completely (the addition of ferric sulfate makes the iron ion concentration in the solution be 0.5g/L);
(3)随后向溶液中通入工业级二氧化硫气体(气体流速为1L/min),同时采用水浴控制反应体系温度为60℃,反应2小时,过滤后得到的固体产物即为单质硒。(3) Pass into the solution subsequently industrial-grade sulfur dioxide gas (gas flow rate is 1L/min), while using a water bath to control the temperature of the reaction system to be 60°C, react for 2 hours, and the solid product obtained after filtration is elemental selenium.
检测步骤(3)过滤后得到的溶液中剩余硒含量,最终硒还原率为99.95%。The remaining selenium content in the solution obtained after the detection step (3) is filtered, and the final selenium reduction rate is 99.95%.
对步骤(3)得到的固体产物进行X射线衍射检测(如图1所示)、扫描电镜检测(如图2所示);由图1可知,固体产物为三方晶型的黑硒单质;由图2可知,硒单质为不规则的颗粒,有团聚现象,颗粒尺寸不一。将步骤(3)得到的固体产物用浓硝酸煮沸后溶解,溶液用电感耦合等离子体原子发射光谱仪检测,固体产物溶解后电感耦合等离子体原子发射光谱仪检测结果显示硒单质纯度为99.75%。Carry out X-ray diffraction detection (as shown in Figure 1) and scanning electron microscope detection (as shown in Figure 2) to the solid product that step (3) obtains; As can be seen from Figure 1, solid product is the black selenium simple substance of trigonal crystal form; By It can be seen from Figure 2 that the selenium element is an irregular particle with agglomeration phenomenon, and the particle size is different. The solid product obtained in step (3) is dissolved after being boiled with concentrated nitric acid, and the solution is detected by an inductively coupled plasma atomic emission spectrometer. After the solid product is dissolved, the inductively coupled plasma atomic emission spectrometer detection result shows that the purity of the selenium element is 99.75%.
实施例2:Example 2:
一种本发明的催化还原硒的方法,具体步骤如下:A kind of method of catalytic reduction selenium of the present invention, concrete steps are as follows:
(1)将硒酸钠(Na2SeO4)用超纯水溶解配制成硒酸钠溶液,使溶液中硒含量为10g/L,然后加入盐酸调节溶液至氢离子浓度为1mol/L;(1) Sodium selenate (Na 2 SeO 4 ) was dissolved in ultrapure water to prepare a sodium selenate solution, so that the selenium content in the solution was 10 g/L, and then hydrochloric acid was added to adjust the solution until the hydrogen ion concentration was 1 mol/L;
(2)取100mL步骤(1)制备的酸性硒酸钠溶液,加入硫酸铁固体后充分搅拌直至硫酸铁固体完全溶解(硫酸铁的加入量使溶液中铁离子浓度为0.5g/L);(2) Get the acidic sodium selenate solution prepared by 100mL step (1), add ferric sulfate solid and fully stir until ferric sulfate solid dissolves completely (the addition of ferric sulfate makes the iron ion concentration in the solution be 0.5g/L);
(3)随后向溶液中加入8g硼氢化钠,同时采用水浴控制反应体系温度为50℃,反应2小时,过滤后得到的固体产物即为单质硒。(3) Add 8 g of sodium borohydride to the solution, and simultaneously use a water bath to control the temperature of the reaction system to 50° C., react for 2 hours, and the solid product obtained after filtration is elemental selenium.
检测步骤(3)过滤后得到的溶液中剩余硒含量,最终硒还原率为99.98%。还原产物的X射线衍射检测与扫描电镜检测与实施例1相似为三方晶型的黑硒单质。将固体产物用浓硝酸煮沸后溶解,溶液用电感耦合等离子体原子发射光谱仪检测,结果显示硒单质纯度为98.92%。The residual selenium content in the solution obtained after the detection step (3) is filtered, and the final selenium reduction rate is 99.98%. The X-ray diffraction detection and scanning electron microscope detection of the reduction product are similar to Example 1, which is trigonal black selenium simple substance. The solid product is boiled with concentrated nitric acid and then dissolved, and the solution is detected by an inductively coupled plasma atomic emission spectrometer, and the result shows that the purity of the selenium element is 98.92%.
实施例3:Example 3:
一种本发明的催化还原硒的方法,具体步骤如下:A kind of method of catalytic reduction selenium of the present invention, concrete steps are as follows:
(1)将硒酸钠(Na2SeO4)用超纯水溶解配制成硒酸钠溶液,使溶液中硒含量为10g/L,然后加入盐酸调节溶液至氢离子浓度为1mol/L;(1) Sodium selenate (Na 2 SeO 4 ) was dissolved in ultrapure water to prepare a sodium selenate solution, so that the selenium content in the solution was 10 g/L, and then hydrochloric acid was added to adjust the solution until the hydrogen ion concentration was 1 mol/L;
(2)取100mL步骤(1)制备的酸性硒酸钠溶液,加入硫酸铁固体后充分搅拌直至硫酸铁固体完全溶解(硫酸铁的加入量使溶液中铁离子浓度为0.5g/L);(2) Get the acidic sodium selenate solution prepared by 100mL step (1), add ferric sulfate solid and fully stir until ferric sulfate solid dissolves completely (the addition of ferric sulfate makes the iron ion concentration in the solution be 0.5g/L);
(3)随后向溶液中加入8g硼氢化钠,同时采用水浴控制反应体系温度为0℃,反应2小时,过滤后得到的固体产物即为单质硒。(3) Add 8 g of sodium borohydride to the solution, and simultaneously use a water bath to control the temperature of the reaction system to 0° C., react for 2 hours, and the solid product obtained after filtration is elemental selenium.
检测步骤(3)过滤后得到的溶液中剩余硒含量,最终硒还原率为99.96%。还原产物的X射线衍射图如图3所示,显示还原产物为无定型的红硒单质,扫描电镜检测与实施例1相似。将固体产物用浓硝酸煮沸后溶解,溶液用电感耦合等离子体原子发射光谱仪检测,结果显示硒单质纯度为99.01%。The residual selenium content in the solution obtained after the detection step (3) is filtered, and the final selenium reduction rate is 99.96%. The X-ray diffraction pattern of the reduction product is shown in Figure 3, which shows that the reduction product is an amorphous red selenium simple substance, and the scanning electron microscope detection is similar to that of Example 1. The solid product is boiled with concentrated nitric acid and then dissolved, and the solution is detected by an inductively coupled plasma atomic emission spectrometer, and the result shows that the purity of selenium is 99.01%.
实施例4:Example 4:
一种本发明的催化还原硒的方法,具体步骤如下:A kind of method of catalytic reduction selenium of the present invention, concrete steps are as follows:
(1)选取200mL加压氧化酸浸处理含硒碲废料溶液(经过离子色谱检测其中含有2.1g/L六价硒酸根离子,5g/L的亚硒酸根离子),加入硫酸调节至溶液中的氢离子浓度为2mol/L;(1) Choose 200mL pressurized oxidative acid leaching to process selenium tellurium waste material solution (contain 2.1g/L hexavalent selenate ion, the selenite ion of 5g/L through ion chromatography detection wherein), add sulfuric acid to adjust to the solution The hydrogen ion concentration is 2mol/L;
(2)在步骤(1)后的溶液中加入硫酸铁固体后充分搅拌直至氯化铁固体完全溶解(硫酸铁的加入量使溶液中铁离子浓度为1g/L);(2) fully stir after adding ferric sulfate solid in the solution after step (1) until ferric chloride solid dissolves completely (the add-on of ferric sulfate makes iron ion concentration in the solution be 1g/L);
(3)随后向溶液中加入20g亚硫酸钠固体,同时采用水浴控制反应体系温度为80℃,反应2小时,过滤后得到的固体产物即为单质硒。(3) Add 20 g of solid sodium sulfite to the solution, and simultaneously use a water bath to control the temperature of the reaction system to 80° C., react for 2 hours, and the solid product obtained after filtration is elemental selenium.
检测步骤(3)过滤后得到的溶液中剩余硒含量,最终硒还原率为99.24%。还原产物的X射线衍射检测与扫描电镜检测与实施例1相似为三方晶型的黑硒单质。将固体产物用浓硝酸煮沸后溶解,溶液用电感耦合等离子体原子发射光谱仪检测,结果显示硒单质纯度为91.23%。The remaining selenium content in the solution obtained after the detection step (3) is filtered, and the final selenium reduction rate is 99.24%. The X-ray diffraction detection and scanning electron microscope detection of the reduction product are similar to Example 1, which is trigonal black selenium simple substance. The solid product was boiled with concentrated nitric acid and dissolved, and the solution was detected by an inductively coupled plasma atomic emission spectrometer, and the result showed that the purity of selenium was 91.23%.
实施例5:Example 5:
一种本发明的催化还原硒的方法,具体步骤如下:A kind of method of catalytic reduction selenium of the present invention, concrete steps are as follows:
(1)选取200mL硒碲混合物酸性氧化浸出液(经过离子色谱检测其中含有5.2g/L六价硒离子,18.9g/L的四价硒离子),加入氢氧化钠调节至溶液中的氢离子浓度为3mol/L;(1) Select 200mL of selenium-tellurium mixture acidic oxidation leaching solution (contains 5.2g/L hexavalent selenium ions and 18.9g/L tetravalent selenium ions through ion chromatography), add sodium hydroxide to adjust the concentration of hydrogen ions in the solution 3mol/L;
(2)在步骤(1)后的溶液中加入硫酸铁固体后充分搅拌直至硫酸铁固体完全溶解(硫酸铁的加入量使溶液中铁离子浓度为2g/L);(2) fully stir after adding ferric sulfate solid in the solution after step (1) until ferric sulfate solid dissolves completely (the add-on of ferric sulfate makes iron ion concentration in the solution be 2g/L);
(3)随后向溶液中通入工业级二氧化硫(气体流速为0.7L/min),同时采用水浴控制反应体系温度为25℃,反应2小时,过滤后得到的固体产物即为单质硒。(3) Then pass into the solution industrial-grade sulfur dioxide (gas flow rate is 0.7L/min), while using a water bath to control the temperature of the reaction system to be 25 ° C, react for 2 hours, and the solid product obtained after filtration is elemental selenium.
检测步骤(3)过滤后得到的溶液中剩余硒含量,最终硒还原率为99.53%。还原产物的X射线衍射检测与扫描电镜检测与实施例1相似为三方晶型的黑硒单质。将固体产物用浓硝酸煮沸后溶解,溶液用电感耦合等离子体原子发射光谱仪检测,结果显示硒单质纯度为96.26%。The remaining selenium content in the solution obtained after the detection step (3) is filtered, and the final selenium reduction rate is 99.53%. The X-ray diffraction detection and scanning electron microscope detection of the reduction product are similar to Example 1, which is trigonal black selenium simple substance. The solid product was boiled with concentrated nitric acid and then dissolved. The solution was detected by an inductively coupled plasma atomic emission spectrometer, and the result showed that the purity of the selenium element was 96.26%.
对比例:Comparative example:
本对比例与实施例5的区别仅在于不含有步骤(2)加入硫酸铁的过程,其他工艺参数与实施例5相同,最终溶液中六价硒离子浓度为5.1g/L,六价硒离子还原率仅为2%。The difference between this comparative example and Example 5 is only that it does not contain the process of adding iron sulfate in step (2), and other process parameters are the same as in Example 5. In the final solution, the hexavalent selenium ion concentration is 5.1g/L, and the hexavalent selenium ion The reduction rate is only 2%.
由上述实施例和对比例的比较可知,本发明的催化还原硒的方法实现了硒的高效还原,六价硒的还原率不低于98%,还原率远远高于常规方法。From the comparison of the above examples and comparative examples, it can be seen that the method for catalytic reduction of selenium in the present invention realizes the efficient reduction of selenium, and the reduction rate of hexavalent selenium is not less than 98%, which is much higher than that of conventional methods.
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CN108558086A (en) * | 2018-01-10 | 2018-09-21 | 南京大学 | A kind of group technology removing hexavalent selenium in water removal |
CN109438104A (en) * | 2019-01-10 | 2019-03-08 | 中南民族大学 | A kind of rich nanometer elemental selenium/organic selenium rapid production process of organic fertilizer of low smelly point of volatilization |
CN109467467A (en) * | 2019-01-10 | 2019-03-15 | 中南民族大学 | A production process of selenium-enriched organic fertilizer with low odor and volatilization |
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CN108558086A (en) * | 2018-01-10 | 2018-09-21 | 南京大学 | A kind of group technology removing hexavalent selenium in water removal |
CN108558086B (en) * | 2018-01-10 | 2020-08-04 | 南京大学 | A combined process for removing hexavalent selenium from water |
CN109438104A (en) * | 2019-01-10 | 2019-03-08 | 中南民族大学 | A kind of rich nanometer elemental selenium/organic selenium rapid production process of organic fertilizer of low smelly point of volatilization |
CN109467467A (en) * | 2019-01-10 | 2019-03-15 | 中南民族大学 | A production process of selenium-enriched organic fertilizer with low odor and volatilization |
CN109467483A (en) * | 2019-01-10 | 2019-03-15 | 中南民族大学 | A kind of low odor volatilization rich nanometer elemental selenium/organic selenium organic fertilizer production process |
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