CN106086978A - A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying - Google Patents

A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying Download PDF

Info

Publication number
CN106086978A
CN106086978A CN201610416437.2A CN201610416437A CN106086978A CN 106086978 A CN106086978 A CN 106086978A CN 201610416437 A CN201610416437 A CN 201610416437A CN 106086978 A CN106086978 A CN 106086978A
Authority
CN
China
Prior art keywords
graphene
sdbs
electrode
ppy
palladium catalyst
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.)
Pending
Application number
CN201610416437.2A
Other languages
Chinese (zh)
Inventor
孙治荣
张进伟
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.)
Beijing University of Technology
Original Assignee
Beijing University of Technology
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 Beijing University of Technology filed Critical Beijing University of Technology
Priority to CN201610416437.2A priority Critical patent/CN106086978A/en
Publication of CN106086978A publication Critical patent/CN106086978A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D9/00Electrolytic coating other than with metals
    • C25D9/02Electrolytic coating other than with metals with organic materials
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F1/46114Electrodes in particulate form or with conductive and/or non conductive particles between them
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4676Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C28/00Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
    • C23C28/30Coatings combining at least one metallic layer and at least one inorganic non-metallic layer
    • C23C28/32Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one pure metallic layer
    • C23C28/322Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one pure metallic layer only coatings of metal elements only
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C28/00Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
    • C23C28/30Coatings combining at least one metallic layer and at least one inorganic non-metallic layer
    • C23C28/34Coatings combining at least one metallic layer and at least one inorganic non-metallic layer including at least one inorganic non-metallic material layer, e.g. metal carbide, nitride, boride, silicide layer and their mixtures, enamels, phosphates and sulphates
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/50Electroplating: Baths therefor from solutions of platinum group metals
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Inert Electrodes (AREA)
  • Catalysts (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The preparation method of a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying, belongs to technical field of electrochemical water treatment.The present invention is with titanium net as matrix, after electroxidation polymerization in its surface forms polypyrrole, is taken in isopropanol the uniform drop coating of graphene dispersing solution after dispersion on its surface, and as negative electrode after fully drying, platinized platinum is as anode, with palladium bichloride (PdCl2) solution is electrolyte, galvanostatic deposition prepares Pd/Graphene/PPy SDBS/Ti electrode.Compared with the Pd/PPy SDBS/Ti electrode without graphene modified of preparation under equal conditions, Pd/Graphene/PPy SDBS/Ti electrode has higher catalysis activity.

Description

A kind of preparation of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying Method
Technical field
The invention belongs to technical field of electrochemical water treatment, relate to a kind of supported palladium based on Graphene/polypyrrole modifying The preparation method of catalyst electrode, is mainly used in the electrochemical reduction dechlorination of chlorinatedorganic in water.
Background technology
Chlorinatedorganic produces material as one and intermediate product has extensively at aspects such as agricultural chemicals, dyestuff, organic syntheses General application is simultaneously discharged in environment.But, major part chlorinatedorganic is all toxic and be considered to have " carcinogenic, teratogenesis, Mutagenesis " effect, and be difficult to degrade, it is the persistence organic pollutant of a quasi-representative.Therefore, chlorinatedorganic in water is carried out The research removed is very necessary.Electrochemical techniques are as a kind of environmentally-friendly technique, in environmental improvement particularly waste water The removal aspect of bio-refractory organic matter has good application prospect.
One of key of electrochemical treatments chlorinatedorganic is electrode, and the quality of electrode material directly affects organic dirt The degradation effect of dye thing.Palladium, because having good reactive hydrogen storage capacity thus promoting dechlorination reaction, becomes catalyst research Emphasis.Material with carbon element has a wide range of applications in catalytic field, when material with carbon element is as catalyst carrier, and the structure of carbon carrier The performance of catalyst is had a significant impact.Researchers find, your gold the both sides of graphene planes structure all can support The high conductivity of genus particle, especially Graphene and huge specific surface area so that it is be particularly suitable as catalyst carrier.Cause This, it is that disposal organo-chlorine pollutant is more high that the loaded palladium catalyst electrode of graphene modified carries out electro-catalysis reduction dechlorination Effect, the method for low consumption.
The present invention modifies using Graphene and polypyrrole as intermediate layer, using palladium as catalyst, is devoted to prepare efficiently Electro-catalysis reduction dechlorination electrode.
Content of the invention
It is an object of the invention to solve the problems of the prior art, provide a kind of prepare simplicity, catalysis activity strong with Titanium net is the loaded palladium catalyst electrode (Pd/Graphene/PPy-SDBS/Ti) based on Graphene/polypyrrole modifying of matrix Preparation method.
The preparation method of above-mentioned Pd/Graphene/PPy-SDBS/Ti electrode and process, comprise the following steps:
(1) titanium net is inserted successively in sodium carbonate liquor (preferred concentration 0.3mol/L) and embathe oil removing, at oxalic acid solution Boiling removal oxide on surface in (preferred concentration 0.1mol/L), then being rinsed well by redistilled water, nitrogen dries up standby;
(2) take neopelex (SDBS) to join in sulfuric acid (preferred concentration 0.3mol/L) and be sufficiently stirred for, molten Adding the pyrroles (Py) having distilled fully to dissolve as deposition liquid after solution, SDBS concentration is preferably 1g/L, and pyrrole concentrations is preferably 0.1mol/L;The titanium net handled well with step (1) is as anode, and with platinized platinum as negative electrode, galvanostatic deposition prepares PPy-SDBS/Ti electricity Pole, constant current sinks galvanostatic deposition 5min under preferred 5mA electric current;
(3) Graphene is joined in isopropanol, Graphene mass concentration 0.02%~0.1% (preferably 0.04%) is super Sound makes it fully dispersed, and then the isopropanol dispersion liquid of drop coating Graphene is to PPy-SDBS/Ti electrode surface, horizontal positioned, fills Divide and dry, obtain Graphene/PPy-SDBS/Ti standby, wherein preferably every 8cm2The corresponding drop coating of PPy-SDBS/Ti electrode surface The isopropanol dispersion liquid of 50-70 μ L Graphene;
(4) take in palladium bichloride powder addition hydrochloric acid and be completely dissolved, prepare palladium chloride solution standby, wherein preferably employ every 1g The corresponding hydrochloric acid solution 100ml adding 3mol/L of palladium bichloride correspondence are diluted with water the palladium chloride solution obtaining 4g/L;
(5) the Graphene/PPy-SDBS/Ti electrode prepared with step (3) is as negative electrode, and platinized platinum is anode, with step (4) The palladium chloride solution of preparation is electrolyte, and galvanostatic deposition current density is 1.875~4.375mA/cm2, sedimentation time is 35 ~55min, galvanostatic deposition prepares Pd/Graphene/PPy-SDBS/Ti electrode.
Use the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying prepared by the present invention as negative electrode, be used for The electrochemical reduction dechlorination of chlorinatedorganic in water has excellent performance.
Compared with prior art, the method have the advantages that
1st, the present invention is with titanium net as matrix, utilizes the high stability such as its high-low temperature resistant, corrosion-resistant, the high intensity of resistance to strong acid special For it, the stability of point, beneficially holding electrode, realizes that the electrochemical reduction dechlorination to chlorinatedorganic provides basis.
2nd, the present invention deposits polypyrrole at titanium net surface, not only increases the specific surface area of electrode, and is follow-up graphite The attachment of alkene is fixing provides condition.
3rd, the present invention is using Graphene as modification, makes full use of the characteristic of its high-specific surface area, high conductivity and stability, Improve the specific surface area of electrode, thus provide more attachment site for palladium catalyst, be conducive to strengthening the catalysis of electrode Activity.
4th, the present invention disperses graphene in organic solvent (isopropanol), and beneficially Graphene is dispersed.Afterwards Use drop-coating by graphene modified in electrode surface, simple to operate.
5th, the present invention uses the method for drop coating and electrochemical deposition to prepare Pd/Graphene/PPy-SDBS/Ti electrode, tool There is higher catalysis activity.
Brief description
Fig. 1 is the scanning electron microscopic picture of PPy-SDBS/Ti.
Fig. 2 is the scanning electron microscopic picture of Graphene/PPy-SDBS/Ti electrode.
Fig. 3 is the scanning electron microscopic picture of Pd/Graphene/PPy-SDBS/Ti electrode, is as can be seen from the figure tied by sheet Structure forms flower ball-shaped structure.
Fig. 4 is the Pd/PPy-of the Pd/Graphene/PPy-SDBS/Ti electrode of embodiment the 1st, embodiment 2 and comparative example The cyclic voltammetry scan curve of SDBS/Ti electrode.
Detailed description of the invention
Example below and comparative example will the present invention is further illustrated in conjunction with accompanying drawing, but the present invention be not limited to Lower embodiment.
Embodiment 1:
(1) sodium carbonate liquor titanium net of 2cm × 2cm being inserted successively 0.3mol/L embathes oil removing, at 0.1mol/L Oxalic acid solution in boil holding 30min remove oxide on surface, then rinsed well by redistilled water, nitrogen dries up standby With;
(2) take neopelex (SDBS) to join in the sulfuric acid of 0.3mol/L and be sufficiently stirred for, add after dissolving The pyrroles (Py) having distilled fully is dissolved as deposition liquid, and SDBS concentration is 1g/L, and pyrrole concentrations is 0.1mol/L.With step (1) the titanium net handled well is anode, with platinized platinum as negative electrode, and galvanostatic deposition 5min under 5mA electric current, preparation PPy-SDBS/Ti electricity Pole.As seen from Figure 1, PPy film is defined at electrode surface;
(3) Graphene of different quality is joined in isopropanol, Graphene mass concentration 0.04%, ultrasonic make it abundant Dispersion, then drop coating 60 μ L dispersion liquid is to PPy-SDBS/Ti electrode surface, horizontal positioned, fully dries, obtains Graphene/ PPy-SDBS/Ti is standby.From Figure 2 it can be seen that Graphene has been attached to electrode surface;
(4) the corresponding hydrochloric acid solution 100ml adding 3mol/L of every 1g palladium bichloride correspondence are diluted with water the chlorine obtaining 4g/L Change palladium solution for standby;
(5) the Graphene/PPy-SDBS/Ti electrode prepared with step (3) is as negative electrode, and platinized platinum is anode, with step (4) The palladium chloride solution of preparation is electrolyte, and galvanostatic deposition current density is 3.125mA/cm2, sedimentation time is 45min, permanent electricity Stream deposition prepares Pd/Graphene/PPy-SDBS/Ti electrode.As seen from Figure 3, palladium has deposited to electrode surface;
(6) the Pd/Graphene/PPy-SDBS/Ti electrode obtaining with step (5) is as working electrode, Pt piece for electrode, Hg/Hg2SO4For reference electrode, at the H of 0.5mol/L2SO4Being circulated voltammetric scan in solution, sweep speed is 50mV/ Min, sweep limits is-700mV~700mV.
Embodiment 2:
(1) sodium carbonate liquor titanium net of 2cm × 2cm being inserted successively 0.3mol/L embathes oil removing, at 0.1mol/L Oxalic acid solution in boil holding 30min remove oxide on surface, then rinsed well by redistilled water, nitrogen dries up standby With;
(2) take neopelex (SDBS) to join in the sulfuric acid of 0.3mol/L and be sufficiently stirred for, add after dissolving The pyrroles (Py) having distilled fully is dissolved as deposition liquid, and SDBS concentration is 1g/L, and pyrrole concentrations is 0.1mol/L.With step (1) the titanium net handled well is anode, with platinized platinum as negative electrode, and galvanostatic deposition 5min under 5mA electric current, preparation PPy-SDBS/Ti electricity Pole;
(3) Graphene of different quality is joined in isopropanol, Graphene mass concentration 0.06%, ultrasonic make it abundant Dispersion, then drop coating 60 μ L dispersion liquid is to PPy-SDBS/Ti electrode surface, horizontal positioned, fully dries, obtains Graphene/ PPy-SDBS/Ti is standby;
(4) the corresponding hydrochloric acid solution 100ml adding 3mol/L of every 1g palladium bichloride correspondence are diluted with water the chlorine obtaining 4g/L Change palladium solution for standby;
(5) the Graphene/PPy-SDBS/Ti electrode prepared with step (3) is as negative electrode, and platinized platinum is anode, with step (4) The palladium chloride solution of preparation is electrolyte, and galvanostatic deposition current density is 2.5mA/cm2, sedimentation time is 45min, constant current Deposition prepares Pd/Graphene/PPy-SDBS/Ti electrode.
(6) the Pd/Graphene/PPy-SDBS/Ti electrode obtaining with step (5) is as working electrode, Pt piece for electrode, Hg/Hg2SO4For reference electrode, at the H of 0.5mol/L2SO4Being circulated voltammetric scan in solution, sweep speed is 50mV/ Min, sweep limits is-700mV~700mV.
Comparative example:
(1) sodium carbonate liquor titanium net of 2cm × 2cm being inserted successively 0.3mol/L embathes oil removing, at 0.1mol/L Oxalic acid solution in boil holding 30min remove oxide on surface, then rinsed well by redistilled water, nitrogen dries up standby With;
(2) take neopelex (SDBS) to join in the sulfuric acid of 0.3mol/L and be sufficiently stirred for, add after dissolving The pyrroles (Py) having distilled fully is dissolved as deposition liquid, and SDBS concentration is 1g/L, and pyrrole concentrations is 0.1mol/L.With step (1) the titanium net handled well is anode, with platinized platinum as negative electrode, and galvanostatic deposition 5min under 5mA electric current, preparation PPy-SDBS/Ti electricity Pole;
(3) the corresponding hydrochloric acid solution 100ml adding 3mol/L of every 1g palladium bichloride correspondence is used to be diluted with water and obtain 4g/L Palladium chloride solution;
(4) the PPy-SDBS/Ti electrode prepared with step (3) is as negative electrode, and platinized platinum is anode, the chlorine prepared with step (4) Changing palladium solution is electrolyte, and galvanostatic deposition current density is 3.125mA/cm2, sedimentation time is 45min, galvanostatic deposition system Obtain Pd/PPy-SDBS/Ti electrode.
(5) the Pd/PPy-SDBS/Ti electrode obtaining with step (5) is as working electrode, and Pt piece is for electrode, Hg/Hg2SO4 For reference electrode, at the H of 0.5mol/L2SO4Being circulated voltammetric scan in solution, sweep speed is 50mV/min, sweep limits For-700mV~700mV.From fig. 4, it can be seen that embodiment 1 all has higher peak point current with embodiment 2 compared with comparative example, electricity Polarity can be higher.

Claims (7)

1. the preparation method based on the loaded palladium catalyst electrode of Graphene/polypyrrole modifying, it is characterised in that include with Lower step:
(1) insert titanium net in sodium carbonate liquor successively and embathe oil removing, in oxalic acid solution, boil removal oxide on surface, then Being rinsed well by redistilled water, nitrogen dries up standby;
(2) take neopelex (SDBS) to join in sulfuric acid and be sufficiently stirred for, after dissolving, add the pyrroles having distilled (Py) fully dissolving as deposition liquid, the titanium net handled well with step (1) is as anode, with platinized platinum as negative electrode, and galvanostatic deposition system Standby PPy-SDBS/Ti electrode;
(3) Graphene is joined in isopropanol, Graphene (Graphene) mass concentration 0.02%~0.1%, ultrasonic make it Fully dispersed, then the isopropanol dispersion liquid of drop coating Graphene is to PPy-SDBS/Ti electrode surface, horizontal positioned, fully dries, Obtain Graphene/PPy-SDBS/Ti standby;
(4) take in palladium bichloride powder addition hydrochloric acid and be completely dissolved, prepare palladium chloride solution standby;
(5) the Graphene/PPy-SDBS/Ti electrode prepared with step (3) is as negative electrode, and platinized platinum is anode, prepares with step (4) Palladium chloride solution be electrolyte, galvanostatic deposition current density is 1.875~4.375mA/cm2, sedimentation time is 35~ 55min, galvanostatic deposition prepares Pd/Graphene/PPy-SDBS/Ti electrode.
2. the preparation side according to a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in claim 1 Method, it is characterised in that step (2) sulfuric acid concentration 0.3mol/L, SDBS concentration is 1g/L, and pyrrole concentrations is 0.1mol/L;Permanent electricity Stream sinks for galvanostatic deposition 5min under 5mA electric current.
3. the preparation side according to a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in claim 1 Method, it is characterised in that step (3) Graphene mass concentration is 0.04%.
4. the preparation side according to a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in claim 1 Method, it is characterised in that the every 8cm of step (3)2The isopropanol of the corresponding drop coating 50-70 μ l Graphene of PPy-SDBS/Ti electrode surface divides Dissipate liquid.
5. the preparation side according to a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in claim 1 Method, it is characterised in that prepared by step (4) palladium chloride solution: use the corresponding hydrochloric acid solution adding 3mol/L of every 1g palladium bichloride 100ml correspondence are diluted with water the palladium chloride solution obtaining 4g/L.
6. according to the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in any one of claim 1-5.
7. according to a kind of loaded palladium catalyst electrode based on Graphene/polypyrrole modifying described in claim 1 in water The application of the electrochemical reduction dechlorination of chlorinatedorganic.
CN201610416437.2A 2016-06-14 2016-06-14 A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying Pending CN106086978A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610416437.2A CN106086978A (en) 2016-06-14 2016-06-14 A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610416437.2A CN106086978A (en) 2016-06-14 2016-06-14 A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying

Publications (1)

Publication Number Publication Date
CN106086978A true CN106086978A (en) 2016-11-09

Family

ID=57846137

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610416437.2A Pending CN106086978A (en) 2016-06-14 2016-06-14 A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying

Country Status (1)

Country Link
CN (1) CN106086978A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107475761A (en) * 2017-08-22 2017-12-15 哈尔滨工程大学 The electropolymerization liquid and electropolymerization method of the sodium dodecyl benzene sulfonate-doped film of poly pyrrole of Mg alloy surface
CN108262071A (en) * 2018-01-25 2018-07-10 河南科技大学 The preparation method of the three-dimensional porous polypyrrole modifying Ti electrode of catalyst carrier
CN112981497A (en) * 2021-02-05 2021-06-18 浙江大学 Preparation method and application of porous MXene hydrogel based on electrocoagulation process
CN113077919A (en) * 2021-03-25 2021-07-06 徐州医科大学 Metal Pd-loaded graphene/polypyrrole composite material and preparation method and application thereof
CN113981490A (en) * 2021-11-05 2022-01-28 浙江师范大学行知学院 Composite material containing palladium metal organic framework compound modified foam nickel and preparation method and application thereof
CN117230483A (en) * 2023-11-13 2023-12-15 河南工学院 Palladium-modified polyaniline/carbon nanotube composite electrode material, and preparation method and application thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060254929A1 (en) * 2004-08-09 2006-11-16 Sugimoto Mikio Method for producing water containing metal ion and water treatment method using said production method, and tool for producing water containing metal ion and water treatment device using said production tool
CN101811755A (en) * 2009-11-27 2010-08-25 北京工业大学 Method for preparing sodium dodecyl benzene sulfonate doped titanium catalyzed electrode
CN102061483A (en) * 2010-11-05 2011-05-18 北京工业大学 Method for preparing palladium-nickel duplex metal catalytic electrode by using sodium dodecyl benzene sulfonate as aid
CN104005075A (en) * 2014-06-04 2014-08-27 北京工业大学 Method for preparing carbon nano-tube modified palladium-loaded electrode through electrophoresis-chemical deposition
CN105225766A (en) * 2015-07-30 2016-01-06 国家纳米科学中心 A kind of preparation method of transparent graphene conductive film
CN105251489A (en) * 2015-09-13 2016-01-20 中南大学 Preparation method for iron-based non-noble metal oxygen evolution catalysts
CN105642278A (en) * 2016-01-20 2016-06-08 广东南海普锐斯科技有限公司 Pd/graphene electrocatalyst and preparation method and application thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060254929A1 (en) * 2004-08-09 2006-11-16 Sugimoto Mikio Method for producing water containing metal ion and water treatment method using said production method, and tool for producing water containing metal ion and water treatment device using said production tool
CN101811755A (en) * 2009-11-27 2010-08-25 北京工业大学 Method for preparing sodium dodecyl benzene sulfonate doped titanium catalyzed electrode
CN102061483A (en) * 2010-11-05 2011-05-18 北京工业大学 Method for preparing palladium-nickel duplex metal catalytic electrode by using sodium dodecyl benzene sulfonate as aid
CN104005075A (en) * 2014-06-04 2014-08-27 北京工业大学 Method for preparing carbon nano-tube modified palladium-loaded electrode through electrophoresis-chemical deposition
CN105225766A (en) * 2015-07-30 2016-01-06 国家纳米科学中心 A kind of preparation method of transparent graphene conductive film
CN105251489A (en) * 2015-09-13 2016-01-20 中南大学 Preparation method for iron-based non-noble metal oxygen evolution catalysts
CN105642278A (en) * 2016-01-20 2016-06-08 广东南海普锐斯科技有限公司 Pd/graphene electrocatalyst and preparation method and application thereof

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107475761A (en) * 2017-08-22 2017-12-15 哈尔滨工程大学 The electropolymerization liquid and electropolymerization method of the sodium dodecyl benzene sulfonate-doped film of poly pyrrole of Mg alloy surface
CN108262071A (en) * 2018-01-25 2018-07-10 河南科技大学 The preparation method of the three-dimensional porous polypyrrole modifying Ti electrode of catalyst carrier
CN108262071B (en) * 2018-01-25 2021-01-29 河南科技大学 Preparation method of three-dimensional porous polypyrrole modified titanium electrode for catalyst carrier
CN112981497A (en) * 2021-02-05 2021-06-18 浙江大学 Preparation method and application of porous MXene hydrogel based on electrocoagulation process
CN113077919A (en) * 2021-03-25 2021-07-06 徐州医科大学 Metal Pd-loaded graphene/polypyrrole composite material and preparation method and application thereof
CN113981490A (en) * 2021-11-05 2022-01-28 浙江师范大学行知学院 Composite material containing palladium metal organic framework compound modified foam nickel and preparation method and application thereof
CN113981490B (en) * 2021-11-05 2022-11-15 浙江师范大学行知学院 Composite material of palladium-containing metal organic framework compound modified foam nickel and preparation method and application thereof
CN117230483A (en) * 2023-11-13 2023-12-15 河南工学院 Palladium-modified polyaniline/carbon nanotube composite electrode material, and preparation method and application thereof
CN117230483B (en) * 2023-11-13 2024-02-06 河南工学院 Palladium-modified polyaniline/carbon nanotube composite electrode material, and preparation method and application thereof

Similar Documents

Publication Publication Date Title
CN106086978A (en) A kind of preparation method of the loaded palladium catalyst electrode based on Graphene/polypyrrole modifying
CN103343342B (en) The method of a kind of polypyrrole-multi-walled carbon nano-tubes synergistically modified year palladium combined electrode and application
CN108686685B (en) Copper nanoparticle/black phosphorus nanosheet composite material and preparation method and application thereof
Yue et al. Graphene–poly (5-aminoindole) composite film as Pt catalyst support for methanol electrooxidation in alkaline medium
Zhou et al. Electrochemical fabrication of novel platinum-poly (5-nitroindole) composite catalyst and its application for methanol oxidation in alkaline medium
CN107010670A (en) A kind of MoSxOy/ carbon nano-composite material, its preparation method and its application
CN101728541B (en) Method for preparing carbon nano tube loaded cobalt-platinum alloy catalyst
CN106876722B (en) A kind of Carbon dioxide electrochemical reduction gas-diffusion electrode and its preparation and application
CN110040820B (en) Titanium-based tin antimony oxide electrode modified by titanium dioxide net structure and preparation method thereof
CN105111507A (en) Preparation method and application of bacterial cellulose/polyaniline/carbon nanotube conducting film material
CN108179433B (en) Ordered mesopore carbon loads nanometer iridium base electrocatalytic hydrogen evolution electrode and its preparation and application
Wang et al. Graphitic carbon nitride/multiwalled carbon nanotubes composite as Pt-free counter electrode for high-efficiency dye-sensitized solar cells
CN106044963B (en) A kind of preparation method of titanium-based Polyaniline Doped brown lead oxide combination electrode material
CN109745865A (en) It is a kind of based on graphite/composite titania material Kynoar electro-catalysis ultrafiltration membrane
CN101235517A (en) Method for preparing Pd-polypyrrole modifying foam nickel catalysis electrode
Ramalingam et al. Efficient PEDOT electrode architecture for continuous redox-flow desalination
CN101630594B (en) Preparation method of composite membrane counter electrode used for dye-sensitized solar cells
CN104005046B (en) A kind of electrophoresis pulse deposits the method preparing carbon nano tube modified load palladium electrode
CN106947990A (en) A kind of electrophoresis pulse deposition prepares the method that graphene modified carries palladium electrode
CN103343378B (en) The preparation method of the high stability catalysis electrode that a kind of carbon nano tube-doped Nafion membrane is modified and application
Guo et al. An In2. 77S4@ conductive carbon composite with superior electrocatalytic activity for dye-sensitized solar cells
Wu et al. An asymmetric Zn//Ag doped polyaniline microparticle suspension flow battery with high discharge capacity
CN101811755B (en) Method for preparing sodium dodecyl benzene sulfonate doped titanium catalyzed electrode
CN104928713B (en) The preparation method and its usage of the Ni-based production hydrogen electrode of conducting polymer cladding
CN1995462B (en) Polypyrrole electrolytic synthesis method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20161109