CN1034027A - 活化性炭阳极 - Google Patents
活化性炭阳极 Download PDFInfo
- Publication number
- CN1034027A CN1034027A CN88100103.1A CN88100103A CN1034027A CN 1034027 A CN1034027 A CN 1034027A CN 88100103 A CN88100103 A CN 88100103A CN 1034027 A CN1034027 A CN 1034027A
- Authority
- CN
- China
- Prior art keywords
- carbon anode
- electrolyting
- active carbon
- quilonum retard
- anode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
- C25C3/08—Cell construction, e.g. bottoms, walls, cathodes
- C25C3/12—Anodes
- C25C3/125—Anodes based on carbon
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
本发明为用于电解生产铝的一种阳极,将含0.4
~1.5%的碳酸锂与沥青、焦炭混捏而制成,其特点是
与已有的炭阳极相比,阳极的过电压可降低150~
200mV,从而生产每吨铝可节电300~600度。除此
而外,还可提高电解质的导电率。
Description
本发明属于电解生产铝的技术领域。
目前的电解工艺,是将氧化铝在冰晶石溶液中进行电解而生产铝,而所采用的阳极为炭素阳极。由于在电解过程中炭阳极与放电的氧离子反应迟缓,造成炭阳极的过电压高达400~600mV,占槽电压的9~14%。因此,现行的工艺因采用炭阳极所浪费的电能较多,因而设法降低阳极的过电压是解决此问题的关键。
鉴于上述情况本发明的目的在于改变现有的炭阳极成份,提供一种能降低阳极过电压的活化性炭阳极。
为实现上述目的本发明提供的一种活化性炭阳极,由含有0.4~1.5%的碳酸锂的炭质材料制成。具体为将0.4~1.5%碳酸锂加入到熔化的沥青中,经搅拌均匀后再与煅后焦炭混捏成炭糊,这样碳酸锂可均匀地分布在炭阳极的表面和内部。这种含碳酸锂的炭阳极在电解过程中具有较高的化学反应活性,能促使炭与氧离子间的化学反应速度加快,从而可降低阳极的过电压。因而碳酸锂的含量要在上述范围内取值,若碳酸锂的含量低于0.4%,则其催化效果不明显;若碳酸锂的含量高于1.5%,虽然具有一定的化学反应活性,但因其含量的增加促成电极的制造成本提高、电极的比电阻也随之增加。
本发明提供的活化性炭阳极与已有的纯炭阳极相比,可使阳极过电压降低150~200mV、槽电压比原来减少2.5~5%,从而生产每吨铝可节省电能300~600度。除此而外,由于活化性炭阳极中所含的碳酸锂在电解过程中溶解在电解质中,可使电解质的温度降低、提高电解质的导电率。
本发明的实施例之一:
自焙炭阳极中添加0.4%的碳酸锂,阳极过电压比原来降低150mV生产每吨铝可节省电能约400度。
本发明的实施例之二:
自焙炭阳极中添加1.5%的碳酸锂,阳极过电压比原来降低200mV生产每吨铝可节省电能约600度。
Claims (1)
- 用于电解生产铝领域的一种活化性炭阳极,其特征在于它是含有0.4~1.5%碳酸锂的炭质材料制成。
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN88100103.1A CN1014911B (zh) | 1988-01-06 | 1988-01-06 | 铝电解用活性炭阳极材料 |
US07/292,383 US4885073A (en) | 1988-01-06 | 1988-12-30 | Activated carbon anode including lithium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN88100103.1A CN1014911B (zh) | 1988-01-06 | 1988-01-06 | 铝电解用活性炭阳极材料 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1034027A true CN1034027A (zh) | 1989-07-19 |
CN1014911B CN1014911B (zh) | 1991-11-27 |
Family
ID=4831176
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN88100103.1A Expired CN1014911B (zh) | 1988-01-06 | 1988-01-06 | 铝电解用活性炭阳极材料 |
Country Status (2)
Country | Link |
---|---|
US (1) | US4885073A (zh) |
CN (1) | CN1014911B (zh) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1985025B (zh) * | 2004-06-22 | 2010-11-10 | Cⅱ炭素有限责任公司 | 用于氧化铝到铝的熔盐电解的电极 |
CN112853401A (zh) * | 2020-12-30 | 2021-05-28 | 江苏苏菱铝用阳极有限公司 | 一种抑制阳极内活性碱金属的预焙阳极 |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5310476A (en) | 1992-04-01 | 1994-05-10 | Moltech Invent S.A. | Application of refractory protective coatings, particularly on the surface of electrolytic cell components |
US5651874A (en) | 1993-05-28 | 1997-07-29 | Moltech Invent S.A. | Method for production of aluminum utilizing protected carbon-containing components |
US6001236A (en) | 1992-04-01 | 1999-12-14 | Moltech Invent S.A. | Application of refractory borides to protect carbon-containing components of aluminium production cells |
US5397450A (en) * | 1993-03-22 | 1995-03-14 | Moltech Invent S.A. | Carbon-based bodies in particular for use in aluminium production cells |
DE69509540T2 (de) | 1994-09-08 | 1999-09-30 | Moltech Invent Sa | Aluminium-elektrogewinnungszelle mit verbesserten kohlenstoff-kathodeblöcken |
US5753163A (en) | 1995-08-28 | 1998-05-19 | Moltech. Invent S.A. | Production of bodies of refractory borides |
BR9900252A (pt) | 1999-02-02 | 2000-08-29 | Companhia Brasileira Carbureto | Recipiente de aço inoxidável para a formação de eletrodos de autocozimento para a utilização em baixos-fornos elétricos de redução |
BR9900253A (pt) | 1999-02-02 | 2000-08-29 | Companhia Brasileira Carbureto | Recipiente de alumìnio e aço inoxidável a formação de eletrodos de autocozimento para a utilização em baixos-fornos elétricos de redução |
CN116444273A (zh) * | 2022-01-10 | 2023-07-18 | 山东圣泉新材料股份有限公司 | 树脂炭素阳极生坯及制备方法、生坯中间体及制备方法、炭素阳极及制备方法 |
CN115142093B (zh) * | 2022-07-14 | 2024-01-30 | 湖南大学 | 一种预焙阳极抗氧化剂、其制备方法及应用 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4011374A (en) * | 1975-12-02 | 1977-03-08 | The United States Of America As Represented By The United States Energy Research And Development Administration | Porous carbonaceous electrode structure and method for secondary electrochemical cell |
-
1988
- 1988-01-06 CN CN88100103.1A patent/CN1014911B/zh not_active Expired
- 1988-12-30 US US07/292,383 patent/US4885073A/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1985025B (zh) * | 2004-06-22 | 2010-11-10 | Cⅱ炭素有限责任公司 | 用于氧化铝到铝的熔盐电解的电极 |
CN112853401A (zh) * | 2020-12-30 | 2021-05-28 | 江苏苏菱铝用阳极有限公司 | 一种抑制阳极内活性碱金属的预焙阳极 |
Also Published As
Publication number | Publication date |
---|---|
US4885073A (en) | 1989-12-05 |
CN1014911B (zh) | 1991-11-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1034027A (zh) | 活化性炭阳极 | |
CN1967912A (zh) | 电动助力车用铅蓄电池的极板和电解液 | |
CA2071235A1 (en) | Anodic electrode for electrochemical fluorine cell | |
CN101368281A (zh) | 熔盐电解法制备铝锂合金的方法 | |
CN107740143B (zh) | 一种具有铁酸锂保护膜的铁基惰性阳极及其制备方法、应用 | |
CN101841031A (zh) | 一种铅蓄电池正极板栅的制备方法 | |
MY109274A (en) | Process of producing metallic foil by electrolysis | |
CN1021120C (zh) | 用于铝电解复合节能炭阳极的制备方法 | |
CN208104570U (zh) | 一种贵金属回收电极组 | |
CN2381648Y (zh) | 铝基金属陶瓷不溶阳极 | |
CN101608319A (zh) | 一种低收缩率阴极糊料 | |
CN1030619A (zh) | 一种阳极 | |
CN109326782A (zh) | 一种锂电池生产用负极材料及其制备方法 | |
JPH0336910B2 (zh) | ||
EP0422116A1 (en) | Process for producing improved electrolytic manganese dioxide | |
CN1044305A (zh) | 含碳酸锂预焙炭阳极 | |
US4582584A (en) | Metal electrolysis using a semiconductive metal oxide composite anode | |
CN2310078Y (zh) | 高效制氧装置 | |
SU1523596A1 (ru) | Способ электролитического получени сурьмы | |
CN201485509U (zh) | 氯酸盐电解槽极板连接装置 | |
Wang et al. | Studies on SnO sub 2-Based Inert Anode in Aluminium Electrolysis | |
CN108642525A (zh) | 一种铝-碳复合阴极铝电解槽 | |
Lebedev | Low-Temperature Electrolysis of Chloride Melts for the Production of Aluminium Powders | |
CN108642524A (zh) | 一种铝-碳复合阴极铝电解槽阴极 | |
Guangchun et al. | Activated Carbon Anode for Aluminum Extraction Cell |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C06 | Publication | ||
PB01 | Publication | ||
C13 | Decision | ||
GR02 | Examined patent application | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |