CN203320083U - Rhodium refining airtight extraction equipment - Google Patents
Rhodium refining airtight extraction equipment Download PDFInfo
- Publication number
- CN203320083U CN203320083U CN2013202385298U CN201320238529U CN203320083U CN 203320083 U CN203320083 U CN 203320083U CN 2013202385298 U CN2013202385298 U CN 2013202385298U CN 201320238529 U CN201320238529 U CN 201320238529U CN 203320083 U CN203320083 U CN 203320083U
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- China
- Prior art keywords
- tank body
- port
- air pressure
- extraction equipment
- rhodium
- Prior art date
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- 229910052703 rhodium Inorganic materials 0.000 title claims abstract description 23
- 239000010948 rhodium Substances 0.000 title claims abstract description 23
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 title claims abstract description 23
- 238000000605 extraction Methods 0.000 title claims abstract description 18
- 238000007670 refining Methods 0.000 title claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 239000000523 sample Substances 0.000 claims abstract description 5
- 239000011521 glass Substances 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims 2
- 238000010168 coupling process Methods 0.000 claims 2
- 238000005859 coupling reaction Methods 0.000 claims 2
- 238000007789 sealing Methods 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 9
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000010953 base metal Substances 0.000 description 5
- -1 platinum group metals Chemical class 0.000 description 4
- 239000005388 borosilicate glass Substances 0.000 description 3
- 229910052741 iridium Inorganic materials 0.000 description 3
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 238000000638 solvent extraction Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000005341 cation exchange Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052762 osmium Inorganic materials 0.000 description 2
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- STCOOQWBFONSKY-UHFFFAOYSA-N tributyl phosphate Chemical compound CCCCOP(=O)(OCCCC)OCCCC STCOOQWBFONSKY-UHFFFAOYSA-N 0.000 description 2
- JWEWNTJADCWFRP-UHFFFAOYSA-N 3-methyl-1-(3-methylbutylsulfanyl)butane Chemical compound CC(C)CCSCCC(C)C JWEWNTJADCWFRP-UHFFFAOYSA-N 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
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- 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
Abstract
本实用新型涉及萃取设备,尤其是涉及铑精炼密闭萃取设备。铑精炼密闭萃取设备,包括罐体(1)、罐盖(2)和支架(3),罐体(1)为直立圆筒状,底部有一个放料口(4),放料口(4)上有放料阀(5),罐体(1)外有加热套(6);罐盖(2)上有进料口(7)、测量口(8)、气压调节口(9)和搅拌器(10),气压调节口(9)上有气压调节阀(11);支架(3)上有自动温度控制仪(12),与自动温度控制仪(12)连接的测温探头(13)从测量口(8)伸入罐体(1)内。本实用新型结构简单,操作方便;便于观察萃取过程;全密闭操作,操作环境友好;对于黏度较高或有操作温度要求的物料,可采用夹套供热方式来实现。
The utility model relates to extraction equipment, in particular to rhodium refining airtight extraction equipment. Rhodium refining airtight extraction equipment, including tank body (1), tank cover (2) and support (3), tank body (1) is an upright cylindrical shape, with a discharge port (4) at the bottom, discharge port (4 ) has a discharge valve (5), and a heating jacket (6) outside the tank body (1); the tank cover (2) has a feed port (7), a measuring port (8), an air pressure regulating port (9) and Stirrer (10), air pressure regulating valve (11) on the air pressure regulating port (9); automatic temperature controller (12) on the bracket (3), temperature measuring probe (13) connected with automatic temperature controller (12) ) into the tank (1) from the measuring port (8). The utility model has the advantages of simple structure and convenient operation; it is convenient to observe the extraction process; it is fully enclosed and friendly to the operating environment; for materials with high viscosity or operating temperature requirements, it can be realized by jacket heating.
Description
技术领域 technical field
本实用新型涉及萃取设备,尤其是涉及铑精炼密闭萃取设备。 The utility model relates to extraction equipment, in particular to rhodium refining airtight extraction equipment.
背景技术 Background technique
铂族金属有6个元素,包括铂、钯、铑、铱、钌、锇。一般情况下,铂族金属以络阴离子形态存在于溶液中,贱金属以水合阳离子形态存在溶液中,阳离子交换是铂族金属与贱金属分离的重要手段。因此,在铑精炼过程中,铑与贱金属的分离相对容易,先采用阳离子交换分离贱金属,得到铑溶液中贱金属合格,再采用溶剂萃取技术分离其它的铂族金属杂质。 There are six elements in the platinum group metals, including platinum, palladium, rhodium, iridium, ruthenium, and osmium. Generally, platinum group metals exist in solution in the form of complex anions, and base metals exist in solution in the form of hydrated cations. Cation exchange is an important means for separating platinum group metals from base metals. Therefore, in the rhodium refining process, the separation of rhodium and base metals is relatively easy. Firstly, cation exchange is used to separate base metals to obtain qualified base metals in rhodium solution, and then solvent extraction technology is used to separate other platinum group metal impurities.
铂族金属的化学性质相近,相互分离很困难。一般先氧化蒸馏分出锇、钌,再用溶剂萃取分离铂、钯,最后才分离铑、铱。 Platinum group metals have similar chemical properties and are difficult to separate from each other. Generally, osmium and ruthenium are separated by oxidative distillation first, then platinum and palladium are separated by solvent extraction, and finally rhodium and iridium are separated.
铑的精炼过程中,采用溶剂萃取技术分离提纯铑,一般采用二异戊基硫醚(S201)萃取钯、磷酸三丁酯(TBP)萃取铂、铱,最后精炼铑,由于溶液中金属杂质的不同,往往需要采用不同的分离方法和设备。 During the rhodium refining process, solvent extraction technology is used to separate and purify rhodium. Generally, diisoamyl sulfide (S201) is used to extract palladium, tributyl phosphate (TBP) to extract platinum and iridium, and finally rhodium is refined. Due to the concentration of metal impurities in the solution Different, often need to use different separation methods and equipment.
现有分离提纯铑的萃取设备抗腐蚀性差,振动大,使用寿命短,操作不方便,劳动强度大,规模较小。 The existing extraction equipment for separating and purifying rhodium has poor corrosion resistance, large vibration, short service life, inconvenient operation, high labor intensity and small scale.
发明内容 Contents of the invention
本实用新型针对现有技术的不足,提供了一种铑精炼密闭萃取设备,有效的解决从含铑废催化剂、铑废渣、铑废液中分离回收铑。 The utility model aims at the deficiencies of the prior art, and provides a rhodium refining airtight extraction device, which can effectively solve the problem of separating and recovering rhodium from rhodium-containing waste catalyst, rhodium waste residue and rhodium waste liquid.
为实现上述目的,本实用新型所采用的技术解决方案是: In order to achieve the above object, the technical solution adopted by the utility model is:
铑精炼密闭萃取设备,包括罐体、罐盖和支架,罐体为直立圆筒状且竖直安装在支架上,底部有一个放料口,放料口上有放料阀,罐体外有加热套;罐盖上有进料口、测量口、气压调节口和钛材搅拌器,进料口平时用玻璃塞封闭,用时打开,气压调节口上有气压调节阀;罐体和罐盖通过连接装置连接成一整体,支架上有自动温度控制仪,与自动温度控制仪连接的测温探头从测量口伸入罐体内,加热套的电源线与自动温度控制仪连接。 Rhodium refining airtight extraction equipment, including tank body, tank cover and bracket, the tank body is upright cylindrical and installed vertically on the bracket, there is a discharge port at the bottom, there is a discharge valve on the discharge port, and there is a heating jacket outside the tank ;The tank cover has a feed inlet, a measuring port, an air pressure adjustment port and a titanium stirrer. The feed inlet is usually closed with a glass plug and opened when it is used. There is an air pressure regulating valve on the air pressure adjustment port; the tank body and the tank cover are connected by a connecting device As a whole, there is an automatic temperature controller on the bracket, and the temperature measuring probe connected with the automatic temperature controller extends into the tank from the measuring port, and the power line of the heating jacket is connected with the automatic temperature controller.
工作时,关闭放料阀,进料口处接上软管,打开气压调节阀,从气压调节口处抽真空使罐体产生内负压,通过软管的另一端分别把萃取剂和萃取物料吸入罐体内,然后停止抽真空使罐体内的气压为常压,卸下进料口处的软管,后用玻璃塞封闭,设定自动温度控制仪的温度,通过加热套对罐体内的物料进行加热,开启搅拌器搅拌罐体内的物料。反应完成后停止搅拌器和自动温度控制仪,打开放料阀排出物料,清洗罐体并进行下一工序。 When working, close the discharge valve, connect the hose to the feed port, open the air pressure regulating valve, and draw a vacuum from the air pressure regulating port to generate internal negative pressure in the tank. Inhale into the tank, then stop vacuuming to make the air pressure in the tank be normal pressure, remove the hose at the inlet, and then close it with a glass plug, set the temperature of the automatic temperature controller, and control the material in the tank through the heating jacket Heating is carried out, and the agitator is turned on to stir the materials in the tank. After the reaction is completed, stop the agitator and the automatic temperature controller, open the discharge valve to discharge the material, clean the tank and proceed to the next process.
所述搅拌器转速为40~200转/分钟。 The rotational speed of the agitator is 40-200 rpm.
所述连接装置为螺栓或螺钉连接。 The connecting device is a bolt or screw connection.
本实用新型的有益效果:The beneficial effects of the utility model:
1、本实用新型结构简单,操作方便,萃取效率高,可放大到较大规模; 1. The utility model has the advantages of simple structure, convenient operation, high extraction efficiency, and can be enlarged to a larger scale;
2、本实用新型的罐体及罐盖均采用高硼硅玻璃材料,便于观察萃取过程; 2. Both the tank body and the tank cover of the utility model are made of high borosilicate glass material, which is convenient for observing the extraction process;
3、本实用新型全密闭操作,操作环境友好; 3. The utility model is fully enclosed and operates in a friendly environment;
4、本实用新型对于黏度较高或有操作温度要求的物料,可采用夹套供热方式来实现。 4. For materials with high viscosity or operating temperature requirements, the utility model can adopt the jacket heating method to realize.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
1-罐体;2-罐盖;3-支架;4-放料口;5-放料阀;6-加热套;7-进料口;8-测量口;9-气压调节口;10-搅拌器;11-气压调节阀;12-自动温度控制仪;13-测温探头。 1- tank body; 2- tank cover; 3- bracket; 4- discharge port; 5- discharge valve; 6- heating mantle; 7- feed port; 8- measuring port; Stirrer; 11-air pressure regulating valve; 12-automatic temperature controller; 13-temperature measuring probe.
具体实施方式 Detailed ways
实施例1Example 1
如图1所示,铑精炼密闭萃取设备,包括高硼硅玻璃罐体1、高硼硅玻璃罐盖2和支架3,罐体1为直立圆筒状且竖直安装在支架3上,底部有一个放料口4,放料口4上有放料阀5,罐体1外有加热套6;罐盖2上有进料口7、测量口8、气压调节口9和钛材搅拌器10,进料口7平时用玻璃塞封闭,用时打开,气压调节口9上有气压调节阀11;罐体1和罐盖2通过连接装置连接成一整体,支架3上有自动温度控制仪12,与自动温度控制仪12连接的测温探头13从测量口8伸入罐体1内,加热套6的电源线与自动温度控制仪12连接。
As shown in Figure 1, the rhodium refining airtight extraction equipment includes a high borosilicate glass tank body 1, a high borosilicate
工作时,关闭放料阀5,进料口7处接上软管,打开气压调节阀11,从气压调节口9处抽真空使罐体1产生内负压,通过软管的另一端分别把萃取剂和萃取物料吸入罐体1内,然后停止抽真空使罐体1内的气压为常压,卸下进料口7处的软管,后用玻璃塞封闭,设定自动温度控制仪12的温度,通过加热套6对罐体1内的物料进行加热,开启搅拌器10搅拌罐体1内的物料。反应完成后停止搅拌器10和自动温度控制仪12,打开放料阀5排出物料,清洗罐体1并进行下一工序。
When working, close the
所述搅拌器10转速为40转/分钟。
The rotational speed of the
所述连接装置为螺栓连接。 The connecting device is a bolt connection.
实施例2Example 2
具体实施方式如实施例1,不同之处在于所述搅拌器转速为200转/分钟。所述连接装置为螺钉连接。 DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT As in Example 1, the difference is that the rotational speed of the agitator is 200 rpm. The connecting device is a screw connection.
Claims (3)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202385298U CN203320083U (en) | 2013-05-07 | 2013-05-07 | Rhodium refining airtight extraction equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013202385298U CN203320083U (en) | 2013-05-07 | 2013-05-07 | Rhodium refining airtight extraction equipment |
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| Publication Number | Publication Date |
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| CN203320083U true CN203320083U (en) | 2013-12-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2013202385298U Expired - Lifetime CN203320083U (en) | 2013-05-07 | 2013-05-07 | Rhodium refining airtight extraction equipment |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107840302A (en) * | 2017-10-26 | 2018-03-27 | 北京航天发射技术研究所 | Rocket Normal Atmospheric Temperature Liquid propellant loading facility and the method for eliminating filling liquid stream gas enclosure |
-
2013
- 2013-05-07 CN CN2013202385298U patent/CN203320083U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107840302A (en) * | 2017-10-26 | 2018-03-27 | 北京航天发射技术研究所 | Rocket Normal Atmospheric Temperature Liquid propellant loading facility and the method for eliminating filling liquid stream gas enclosure |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131204 |
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| CX01 | Expiry of patent term |