CN115947602B - ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof - Google Patents

ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof Download PDF

Info

Publication number
CN115947602B
CN115947602B CN202211232277.8A CN202211232277A CN115947602B CN 115947602 B CN115947602 B CN 115947602B CN 202211232277 A CN202211232277 A CN 202211232277A CN 115947602 B CN115947602 B CN 115947602B
Authority
CN
China
Prior art keywords
zrb
inert anode
anode
ceramic
metal
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.)
Active
Application number
CN202211232277.8A
Other languages
Chinese (zh)
Other versions
CN115947602A (en
Inventor
何汉兵
曾婧
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Central South University
Original Assignee
Central South University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Central South University filed Critical Central South University
Priority to CN202211232277.8A priority Critical patent/CN115947602B/en
Publication of CN115947602A publication Critical patent/CN115947602A/en
Application granted granted Critical
Publication of CN115947602B publication Critical patent/CN115947602B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Abstract

The invention discloses a ZrB 2 A base metal ceramic inert anode, a preparation method and application thereof; the method utilizes ceramic component ZrB with better conductivity 2 (conductivity 1X 10) 4 S/cm‑1.2×10 5 S/cm) is a ceramic phase, cu (Ni) with better toughness is used as a metal phase to prepare the metal ceramic inert anode, the good conductivity of the metal ceramic inert anode is maintained, the molten salt corrosion resistance of the inert anode is improved, and the cathode raw aluminum also has higher purity.

Description

ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof
Technical Field
The invention relates to a ZrB 2 A base high-conductivity high-temperature-resistant molten salt corrosion-resistant metal ceramic inert anode and a preparation method and application thereof belong to the technical field of aluminum electrolysis.
Background
ZrB 2 Due to its good conductivity (conductivity 1X 10 4 S/cm-1.2×10 5 S/cm) and resistance to corrosion by high temperature molten salts are now of increasing interest. Inert metal ceramicIn order to achieve the balance of compactness, mechanical property, conductivity and high-temperature molten salt corrosion resistance, ceramic components are often added into the anode to withstand high-temperature molten salt corrosion, and then high-content metal components are added to improve the conductivity of the metal ceramic, so that the metal ceramic inert anode is preferentially corroded in the electrolysis process, a large number of micropores are formed in the surface of the metal ceramic inert anode, a permeation channel is provided for high-temperature molten salt electrolyte, and the corrosion of the metal ceramic inert anode is serious. Although coating the surface of the metal phase with a certain amount of spinel oxide powder may be used to avoid preferential corrosion of the metal phase in the high temperature molten salt compared to the ceramic phase (201110146867.4); or controlling certain electrolytic corrosion conditions to ensure that the metal ceramic inert anode reaches dynamic corrosion balance (201210066342.4) of the surface compact spinel type oxide ceramic corrosion and the continuous formation of a new compact spinel type oxide ceramic layer inside the metal ceramic inert anode, but has little effect on large-scale aluminum electrolysis.
Disclosure of Invention
Aiming at the defects of the prior aluminum electrolysis inert anode, the invention aims to provide a ZrB 2 A base metal ceramic inert anode, a preparation method and application thereof.
Due to ZrB 2 The conductivity of the ceramic is 1 multiplied by 10 4 S/cm-1.2×10 5 S/cm, compared with common aluminum electrolysis inert anode NiFe 2 O 4 The electrical conductivity of NiO-Cu/Ni is 10-100S/cm, which is improved by three orders of magnitude; zrB 2 The high conductivity of the ceramic can greatly reduce the Cu/Ni metal content in the cermet, and a large number of holes are not generated on the surface of the anode due to preferential corrosion of a large number of Cu/Ni metals in the aluminum electrolysis process, so that the electrolyte can be quickly permeated to cause premature failure of the anode. And ZrB 2 The ceramic can also resist high temperature molten salt corrosion, thus ZrB 2 The metal ceramic can reach the balance of the conductivity and the high-temperature molten salt corrosion resistance of the metal ceramic inert anode.
In order to achieve the technical purpose, the invention aims at being realized by the following technical means.
ZrB (ZrB) 2 Base metal ceramicCeramic inert anode: comprises ZrB 2 A major ceramic component, and a Cu and/or Ni metal phase with better toughness.
Further, the ZrB 2 An inert anode of metal ceramic, wherein the proportion of each component comprises ZrB 2 90-95% of metal phase and 5-10% of metal phase.
ZrB according to the invention 2 The preparation method of the metal ceramic-based inert anode comprises the following steps: firstly weighing ZrB 2 Ball-milling and mixing Cu and/or Ni powder in a ball-milling medium containing a dispersing agent and a binder, and (3) drying the mixed powder, pressing and forming the mixed powder into a green body, and finally sintering the green body in a protective atmosphere to obtain the finished product.
Further, the dispersing agent is at least one of water, ethanol and methanol; the binder is at least one of polyvinyl alcohol and polyethylene glycol.
Further: the grinding ball material comprises: steel balls or zirconium balls; the diameter is 1-5cm; ball material ratio is 1:1-1:2, ball milling and mixing are carried out for 120-150min.
Further, the mixed powder is dried and then is formed by bidirectional compression molding under the pressure of 100-300MPaIs a green body of (c).
Further, the sintering temperature is 1150-1400 ℃ and the sintering time is 2-6h.
The invention also provides the ZrB 2 The application method of the metal ceramic-based inert anode is used for aluminum electrolysis or rare earth electrolysis.
Further, the electrolyte comprises the following components in percentage by mass during electrolysis: na (Na) 3 AlF 6 And/or K 3 AlF 6 60~80%,AlF 3 5~30%,CaF 2 ≤10%,Al 2 O 3 3~5%。
Further, the condition parameters at the time of electrolysis range: (1) depth of immersion of anode into electrolyte: 1-4cm; (2) cathode aluminum: the height is 1.5-3.5cm; (3) anode bottom current density: 0.8-1.1A/cm 2 The method comprises the steps of carrying out a first treatment on the surface of the (4) pole pitch: 2-4cm; (5) electrolyte level: 5-9cm; (6) electrolysis temperature:800-960 ℃. The electrolysis time is not less than 10 hours.
ZrB of the invention 2 The base high-conductivity high-temperature-resistant molten salt corrosion-resistant metal ceramic inert anode is ZrB with better conductivity 2 The ceramic component takes Cu (Ni) with better toughness as a metal phase, improves the conductivity of the metal ceramic inert anode and improves the molten salt corrosion resistance of the inert anode.
The technical principle of the invention has the beneficial technical effects compared with the prior art:
principle of: a large number of researches show that the ZrB with good conductivity is prepared at the temperature and the current density of the invention 2 The ceramic is a metal ceramic inert anode prepared by ceramic phase, and then is put into proper electrolyte for electrolytic corrosion, and because the metal components in the metal ceramic inert anode are less, zrB is simultaneously carried out 2 The ceramic has good conductivity, and ZrB is used in the aluminium electrolysis process 2 The metal-based cermet inert anode will be compared with NiFe 2 O 4 The NiO metal ceramic inert anode has improved conductivity and molten salt corrosion resistance, can effectively slow down the anode corrosion speed, and meanwhile, has fewer anode components dissolved in electrolyte and less amount of elemental metal generated in cathode discharge, thereby keeping the original cathode aluminum of the anode to have higher purity.
If it is less than 90% ZrB 2 The anode has poor conductivity, high cell voltage and high energy consumption in the electrolysis process.
If more kinds of metals are doped, the effect is not improved, and the impurities in the original aluminum are more, which is unfavorable for the purity of the original aluminum.
The beneficial effects are that: (1) The technical proposal of the invention can simultaneously improve the conductivity and corrosion resistance of the metal ceramic inert anode for aluminum electrolysis and the purity of the original aluminum, and solves the problems of NiFe at present 2 O 4 The problems of reduced conductivity, improved resistance to molten salt corrosion of the anode, and the like caused by preferential corrosion of metal due to excessive Cu (Ni) metal content of the NiO-Cu (Ni) cermet inert anode in the aluminum electrolysis process. (2) The technical scheme of the invention has simple and convenient process and is easy to popularize and apply.
Detailed Description
The following examples are presented to further illustrate the invention and are not intended to limit the scope of the invention as claimed.
Example 1
Firstly weighing ZrB according to a proportion 2 And Cu or/and Ni powder, ball milling and mixing for 120min in a ball milling medium containing dispersant absolute ethyl alcohol and binder polyethylene glycol, wherein the diameter range is 1-3cm; ball-material ratio 1:1, and the mixed powder is formed by bidirectional compression molding under 200MPa pressure after being driedFinally, the green body is placed in an electric furnace, and the green body is placed in N 2 Sintering for 3h at 1400 ℃ according to a certain heating system in the atmosphere to obtain a ceramic inert anode sample 5 (20 Ni-Cu)/95 ZrB with a regular shape 2
5(20Ni-Cu)/95ZrB 2 (20% Ni and 80% Cu constitute the metallic phase, 5% metallic phase and 95% ZrB) 2 Constituting a ceramic inert anode) and 5 (20 Ni-Cu)/95 (NiFe 2 O 4 -10 NiO) (20% Ni and 80% Cu constitute the metallic phase, 90% NiFe 2 O 4 And 10% NiO constitute the ceramic phase, 5% of the metal phase and 95% of the ceramic phase constitute the ceramic inert anode) and 5 (20 Ni-Cu)/95 (NiFe) 2 O 4 -10NiO-10ZrB 2 ) (20% Ni and 80% Cu constitute the metallic phase, 80% NiFe) 2 O 4 And 10% NiO and 10% ZrB 2 Constitute a ceramic phase, 5% of the metal phase and 95% of the ceramic phase constitute a ceramic inert anode) the ceramic inert anode, the conductivity at 960 ℃ being 168.2S/cm, 52.5S/cm and 75.6S/c, respectively; at electrolyte 78.07% Na 3 AlF 6 -9.5%AlF 3 -5.0%CaF 2 -7.43%Al 2 O 3 Medium (primary crystal temperature 947 ℃, superheat degree 13 ℃) and current density of 0.98A/cm 2 ) Electrolysis for 120h (electrolysis temperature 960 ℃); depth of anode immersed in electrolyte: 2cm, cathode aluminum: height 2.5cm, pole pitch: 3cm, electrolyte level: after 5cm, it was found that 5 (20 Ni-Cu)/95 ZrB 2 The anode corrosion rate was 0.64 cm/year -1 ,5(20Ni-Cu)/95(NiFe 2 O 4 -10 NiO) with a corrosion rate of 1.23 cm-year -1 ,5(20Ni-Cu)/95(NiFe 2 O 4 -10NiO-10ZrB 2 ) The corrosion rate is 0.96 cm-year -1 . The purity of the raw aluminum is 99.5wt%, 98.8wt% and 99.1wt%, respectively. Description ZrB 2 The metal ceramic can improve the high-temperature conductivity and high-temperature molten salt corrosion resistance of the metal ceramic inert anode. W (W) loss =(W b ×C b +W a ×C a )×10 -6 ×365×24/(s Anode ×ρ Anode ×t)(1)
W in (1) loss Defined as the annual rate of corrosion of the anode (cm. Year) -1 ),W b C is the total electrolyte (g) b W for impurity concentration (ppm) into electrolyte a C is the total amount (g) of cathode aluminum a To enter the concentration (ppm) of impurities in the cathode aluminum liquid, the sAnode is the surface area (cm) of the anode immersed during electrolysis 2 ) ρanode is the volume density (g/cm) of the anode 3 ) T is the electrolysis time (h).
Example 2:
10(20Ni-Cu)/90ZrB 2 the preparation method is the same as in example 1
10(20Ni-Cu)/90ZrB 2 And 10 (20 Ni-Cu)/90 (NiFe) 2 O 4 -10 NiO) cermet inert anode having conductivities at 183.7S/cm and 69.2S/cm, respectively, at 910 ℃; at low temperature electrolyte 23.4K 3 AlF 6 -54.6Na 3 AlF 6 -22.5%AlF 3 -5.0%Al 2 O 3 Middle (primary crystal temperature 890 ℃, superheat 20 ℃ and current density 1.0A/cm) 2 ) Electrolysis for 120h (electrolysis temperature 910 ℃); depth of anode immersed in electrolyte: 2cm, cathode aluminum: height 2.5cm, pole pitch: 3cm, electrolyte level: after 5cm, it was found that 10 (20 Ni-Cu)/90 ZrB 2 The anode corrosion rate was 0.71 cm/year -1 ,10(20Ni-Cu)/90(NiFe 2 O 4 -10 NiO) with a corrosion rate of 1.48 cm-year -1 . The purity of the raw aluminum was 99.3wt% and 98.7wt%, respectively. Description ZrB 2 The metal ceramic can improve the high-temperature conductivity and high-temperature molten salt corrosion resistance of the metal ceramic inert anode.

Claims (9)

1. ZrB (ZrB) 2 The metal ceramic-based inert anode is characterized in that: comprises ZrB 2 A ceramic component mainly, and a Cu and/or Ni metal phase with better toughness; the ratio of each component comprises ZrB 2 90% -95% of metal phase and 5% -10% of metal phase.
2. ZrB according to claim 1 2 The preparation method of the metal ceramic-based inert anode is characterized by comprising the following steps of: the method comprises the following steps: firstly weighing ZrB 2 Ball-milling and mixing Cu and/or Ni powder in a ball-milling medium containing a dispersing agent and a binder, and (3) drying the mixed powder, pressing and forming the mixed powder into a green body, and finally sintering the green body in a protective atmosphere to obtain the finished product.
3. The preparation method according to claim 2, characterized in that: the dispersing agent is at least one of water, ethanol and methanol; the binder is at least one of polyvinyl alcohol and polyethylene glycol.
4. The preparation method according to claim 2, characterized in that: the grinding ball material comprises: steel balls or zirconium balls; the diameter is 1-5cm; ball material ratio is 1:1-1:2, ball milling and mixing are carried out for 120-150min.
5. The preparation method according to claim 2, characterized in that: and drying the mixed powder, and performing bidirectional compression molding under the pressure of 100-300MPa to obtain a green body with phi 20mm multiplied by 40 mm.
6. The preparation method according to claim 2, characterized in that: the sintering temperature is 1150-1400 ℃ and the sintering time is 2-6h.
7. ZrB according to claim 1 2 An inert anode based on cermet or ZrB prepared by the method of any one of claims 2-6 2 The application method of the metal ceramic-based inert anode is characterized by comprising the following steps of: is used for aluminum electrolysis or rare earth electrolysis.
8. The application method according to claim 7, wherein the electrolyte comprises the following components in percentage by mass during electrolysis: na (Na) 3 AlF 6 And/or K 3 AlF 6 60~80%,AlF 3 5~30%,CaF 2 ≤10%,Al 2 O 3 3~5%。
9. The method of claim 7, wherein the range of parameters of the electrolysis conditions is: (1) depth of immersion of anode into electrolyte: 1-4cm; (2) cathode aluminum; (3) anode bottom current density: 0.8-1.1A/cm 2 The method comprises the steps of carrying out a first treatment on the surface of the (4) pole pitch: 2-4cm; (5) electrolyte level: 5-9cm; (6) electrolysis temperature: 800-960 ℃.
CN202211232277.8A 2022-10-10 2022-10-10 ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof Active CN115947602B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202211232277.8A CN115947602B (en) 2022-10-10 2022-10-10 ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202211232277.8A CN115947602B (en) 2022-10-10 2022-10-10 ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof

Publications (2)

Publication Number Publication Date
CN115947602A CN115947602A (en) 2023-04-11
CN115947602B true CN115947602B (en) 2023-11-07

Family

ID=87295867

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202211232277.8A Active CN115947602B (en) 2022-10-10 2022-10-10 ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof

Country Status (1)

Country Link
CN (1) CN115947602B (en)

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3088906A (en) * 1959-12-07 1963-05-07 Norton Co Cathode bar for aluminum reduction cell
JPS6256545A (en) * 1985-09-06 1987-03-12 Asahi Glass Co Ltd Zrb2-cu type sintered body
JPH05263285A (en) * 1992-03-17 1993-10-12 Nippon Light Metal Co Ltd Electrode for electrolyzing aluminum
US5870663A (en) * 1996-08-02 1999-02-09 The Texas A&M University System Manufacture and use of ZrB2 /CU composite electrodes
US5933701A (en) * 1996-08-02 1999-08-03 Texas A & M University System Manufacture and use of ZrB2 /Cu or TiB2 /Cu composite electrodes
CN1940103A (en) * 2005-09-30 2007-04-04 中南大学 Cu.TiB nano-diffusion alloy and its production
WO2009112192A2 (en) * 2008-03-14 2009-09-17 Esk Ceramics Gmbh & Co. Kg Composite material based on transition metal borides, method for the production thereof, and use thereof
WO2010015789A2 (en) * 2008-08-08 2010-02-11 Drazenovic Beatrice Semiconductor ceramic
RO125862A2 (en) * 2009-02-25 2010-11-30 Institutul De Chimie Fizică "Ilie Murgulescu" Process for electrolytic making of aluminium and inert anodes and electrolyte compositions
CN102216208A (en) * 2008-11-17 2011-10-12 钴碳化钨硬质合金公司 Readily-densified titanium diboride and process for making same
CN102689907A (en) * 2012-05-30 2012-09-26 深圳市新星轻合金材料股份有限公司 Preparing method and application of transition metal boride
RU2012107070A (en) * 2009-07-28 2013-09-10 Алкоа Инк. COMPOSITION FOR PRODUCING A WETABLE CATHODE FOR Smelting
CN103304239A (en) * 2013-06-27 2013-09-18 中国铝业股份有限公司 TiB2-based metal ceramic material for aluminium cell and preparation method of material
CN104018019A (en) * 2014-05-26 2014-09-03 郑州大学 ZrB2/Cu composite material preparation method
CN105506674A (en) * 2016-03-01 2016-04-20 中南大学 Method for improving corrosion resistance of metal ceramic inert anode
CA2983583A1 (en) * 2015-04-23 2016-10-27 Obshchestvo S Ogranichennoy Otvetstvennost'yu "Obedinennaya Kompaniya Rusal Inzhenerno-Tekhnologicheskiy Tsentr" Aluminum reduction cell electrode (variants)
CN106278281A (en) * 2016-08-16 2017-01-04 东北大学 A kind of boronation titanio composite cathode material and preparation method thereof
CN108118177A (en) * 2017-12-21 2018-06-05 湖北工业大学 A kind of in-situ synthesis of boride zirconium enhancing Cu-base composites and its preparation method and application
CN108611515A (en) * 2018-05-09 2018-10-02 台州学院 A kind of preparation method of spot-wedling electrode nano-granular zirconium carbide-rodlike zirconium boride dispersed and strengthened copper-based composite material
CN113186569A (en) * 2021-04-30 2021-07-30 中南大学 High-corrosion-resistance metal ceramic inert anode material for aluminum electrolysis and preparation method thereof

Patent Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3088906A (en) * 1959-12-07 1963-05-07 Norton Co Cathode bar for aluminum reduction cell
JPS6256545A (en) * 1985-09-06 1987-03-12 Asahi Glass Co Ltd Zrb2-cu type sintered body
JPH05263285A (en) * 1992-03-17 1993-10-12 Nippon Light Metal Co Ltd Electrode for electrolyzing aluminum
US5870663A (en) * 1996-08-02 1999-02-09 The Texas A&M University System Manufacture and use of ZrB2 /CU composite electrodes
US5933701A (en) * 1996-08-02 1999-08-03 Texas A & M University System Manufacture and use of ZrB2 /Cu or TiB2 /Cu composite electrodes
CN1940103A (en) * 2005-09-30 2007-04-04 中南大学 Cu.TiB nano-diffusion alloy and its production
WO2009112192A2 (en) * 2008-03-14 2009-09-17 Esk Ceramics Gmbh & Co. Kg Composite material based on transition metal borides, method for the production thereof, and use thereof
WO2010015789A2 (en) * 2008-08-08 2010-02-11 Drazenovic Beatrice Semiconductor ceramic
CN102216208A (en) * 2008-11-17 2011-10-12 钴碳化钨硬质合金公司 Readily-densified titanium diboride and process for making same
RO125862A2 (en) * 2009-02-25 2010-11-30 Institutul De Chimie Fizică "Ilie Murgulescu" Process for electrolytic making of aluminium and inert anodes and electrolyte compositions
RU2012107070A (en) * 2009-07-28 2013-09-10 Алкоа Инк. COMPOSITION FOR PRODUCING A WETABLE CATHODE FOR Smelting
CN102689907A (en) * 2012-05-30 2012-09-26 深圳市新星轻合金材料股份有限公司 Preparing method and application of transition metal boride
CN103304239A (en) * 2013-06-27 2013-09-18 中国铝业股份有限公司 TiB2-based metal ceramic material for aluminium cell and preparation method of material
CN104018019A (en) * 2014-05-26 2014-09-03 郑州大学 ZrB2/Cu composite material preparation method
CA2983583A1 (en) * 2015-04-23 2016-10-27 Obshchestvo S Ogranichennoy Otvetstvennost'yu "Obedinennaya Kompaniya Rusal Inzhenerno-Tekhnologicheskiy Tsentr" Aluminum reduction cell electrode (variants)
CN107429414A (en) * 2015-04-23 2017-12-01 俄铝工程技术中心有限责任公司 Electrode of aluminum electrolysis cell (variant)
CN105506674A (en) * 2016-03-01 2016-04-20 中南大学 Method for improving corrosion resistance of metal ceramic inert anode
CN106278281A (en) * 2016-08-16 2017-01-04 东北大学 A kind of boronation titanio composite cathode material and preparation method thereof
CN108118177A (en) * 2017-12-21 2018-06-05 湖北工业大学 A kind of in-situ synthesis of boride zirconium enhancing Cu-base composites and its preparation method and application
CN108611515A (en) * 2018-05-09 2018-10-02 台州学院 A kind of preparation method of spot-wedling electrode nano-granular zirconium carbide-rodlike zirconium boride dispersed and strengthened copper-based composite material
CN113186569A (en) * 2021-04-30 2021-07-30 中南大学 High-corrosion-resistance metal ceramic inert anode material for aluminum electrolysis and preparation method thereof

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
Preparation of ZrB2-based nanocomposites with limited grain growth by means of low-temperature hot-pressing using Cu additive;Rujie He et al.;International Journal of Materials Research;第104卷(第10期);第1034-1035页 *
Processing and properties of ZrB2-Cu composites sintered by Hot-pressing sintering;Wei Shang et al.;Key Engineering Materials;447-450 *
化学镀铜制备ZrB2-Cu复合粉末的工艺研究;朱时珍 等;稀有金属材料与工程;第42卷;614-617 *
硼化物陶瓷及其复合材料的研究进展;贾成科;张鑫;彭浩然;谢旭霞;任先京;;热喷涂技术(第01期);全文 *

Also Published As

Publication number Publication date
CN115947602A (en) 2023-04-11

Similar Documents

Publication Publication Date Title
CN108793987B (en) Lithium ion conductive oxide solid electrolyte and preparation method thereof
CN107234241B (en) A kind of micrometer level porous tungsten and preparation method thereof
CN103746134B (en) A kind of electrolyte for solid oxide fuel cell and preparation method thereof
Li et al. Preparation of double-doped BaCeO3 and its application in the synthesis of ammonia at atmospheric pressure
CN102586853B (en) Method for improving high-temperature fused salt corrosion resistance of metal ceramic inert anode
CN108103524A (en) A kind of electrolytic tank of solid oxide and preparation method thereof
CN103556184A (en) Preparation method of all-wet nano NiFe2O4-NiO-Cu-Ni metal ceramic inert anode
CN104388972A (en) Cathode material used for solid oxide electrolytic cell and application of cathode material
CN108682867A (en) A kind of magnesium-air cell anode band and its preparation method and application
CN110931730B (en) Titanium niobate negative electrode material and preparation method and application thereof
Zhang et al. Microstructure and ion conductivity of Al‐LLZO solid electrolyte prepared by molten salt and cold sintering process
CN115947602B (en) ZrB (ZrB) 2 Metal ceramic-based inert anode and preparation method and application thereof
CN103165930A (en) Method for improving sintering performance of electrolyte of proton conductor solid oxide fuel cell (SOFC)
CN108409315B (en) Nickel ferrite based ceramic inert anode material for aluminum electrolysis and preparation method thereof
CN101552344B (en) Method for preparing composite oxides mischcrystal jelly glue with gadolinium oxide adulterating cerium oxide
CN105655618B (en) One kind melts mixed type intermediate temperature solid oxide fuel cell electrolyte admittedly
CN107611461A (en) A kind of preparation method of SOFC
CN109742431B (en) Cerium oxide matrix doped dysprosium oxide composite electrolyte material and preparation method thereof
CN107841765B (en) A kind of Zinc electrolysis anode material and preparation method thereof
CN114497714B (en) Preparation method of garnet type solid electrolyte with high ion conductivity
CN115763916A (en) Ga and Mg co-doped apatite lanthanum silicate solid electrolyte material and preparation method thereof
CN114243095A (en) K-beta' -Al2O3Solid electrolyte, preparation method thereof and potassium battery
CN113430577A (en) NiFe for aluminum electrolysis2O4Inert anode material of base cermet and its prepn
CN110229003B (en) Preparation method and application of LiNiLaZrO solid electrolyte
CN115403358B (en) Transition metal ion and Eu 3+ Co-doped solid electrolyte ceramic material and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant