CN107012475A - A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition - Google Patents

A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition Download PDF

Info

Publication number
CN107012475A
CN107012475A CN201710272307.0A CN201710272307A CN107012475A CN 107012475 A CN107012475 A CN 107012475A CN 201710272307 A CN201710272307 A CN 201710272307A CN 107012475 A CN107012475 A CN 107012475A
Authority
CN
China
Prior art keywords
bipolar membrane
water decomposition
type semiconductor
hydrogen
application
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.)
Granted
Application number
CN201710272307.0A
Other languages
Chinese (zh)
Other versions
CN107012475B (en
Inventor
刘宪
韩艳娇
宋秀丽
杨慧敏
代红艳
梁镇海
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.)
Taiyuan Normal University
Original Assignee
Taiyuan Normal 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 Taiyuan Normal University filed Critical Taiyuan Normal University
Priority to CN201710272307.0A priority Critical patent/CN107012475B/en
Publication of CN107012475A publication Critical patent/CN107012475A/en
Application granted granted Critical
Publication of CN107012475B publication Critical patent/CN107012475B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70Assemblies comprising two or more cells
    • C25B9/73Assemblies comprising two or more cells of the filter-press type
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/50Processes
    • C25B1/55Photoelectrolysis
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B11/00Electrodes; Manufacture thereof not otherwise provided for
    • C25B11/04Electrodes; Manufacture thereof not otherwise provided for characterised by the material
    • C25B11/051Electrodes formed of electrocatalysts on a substrate or carrier
    • C25B11/073Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • C25B9/23Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms comprising ion-exchange membranes in or on which electrode material is embedded
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition, the application is using the cation-exchange membrane of area load P-type semiconductor photocatalyst powder and the anion-exchange membrane of area load N-type semiconductor photocatalyst powder as Bipolar Membrane, and constitute cathode chamber and anode chamber's barrier film, it regard P-type semiconductor photocatalyst powder material as negative electrode, it regard N-type semiconductor photocatalyst powder material as anode, prepare 0.5 ~ 1.0 M catholyte and anolyte respectively afterwards, light source is used as using xenon lamp, applied voltage is under 0.5 ~ 2.0 V is acted on, it is carried out continuously photoelectrocatalysis water decomposition hydrogen manufacturing.The catalyst of powdered form is attached to Bipolar Membrane two sides by the present invention, for photoelectrocatalysis water decomposition hydrogen manufacturing, hydrogen generation efficiency is up to 90 ~ 99.8%, hydrogen purity is up to 90% ~ 99.99%, continuous operation 10 ~ 48 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize efficient, the continuous operation of semiconductor powder state photochemical catalyst hydrogen production by water decomposition.

Description

A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition
Technical field
It is a kind of load powdered form specifically the present invention relates to a kind of application of powdered form catalyst in water decomposition The technical scheme that the Bipolar Membrane of catalyst is applied in water decomposition hydrogen manufacturing.
Background technology
Semiconductor photoelectrocatalysielectrode technology is a kind of effective technology means for converting solar energy into chemical energy, to solving the energy In short supply, reduction pollution pressure is significant.By the exploration and accumulation of scientists from all over the world for many years, the research in the field Greater advance is achieved, but on the whole, using solar photoelectric catalytic efficiency still than relatively low.One of main cause is Because photo-generate electron-hole fails to efficiently separate, it is combined again, causes photoelectric catalytically active to decline.Domestic and foreign scholars are used Various methods separate photo-generate electron-hole, such as:Fan etc. is by TiO2It is combined with BiOCl catalyst, makes BiOCl conduction bands Electro transfer is to TiO2On conduction band, TiO2The hole of valence band is transferred in BiOCl valence band, so as to effectively separate electron-hole (CrystEngComm, 2014, 16: 820-825);Zhang etc. is prepared for BiOCl nucleocapsid structure photochemical catalysts, this structure Photo-generate electron-hole can be efficiently separated, so as to improve photocatalytic activity(CrystEngComm, 2012, 14: 700- 707).It can be seen that, it is still that key in the urgent need to address during photoelectrocatalysis is asked to improve photo-generate electron-hole separative efficiency Topic.
In photoelectrocatalysis actual application, semiconductor powder state catalyst has what hardly possible after easily reunion and reaction was reclaimed Problem.Therefore, the immobilization of photochemical catalyst is to the practical extremely important of photocatalysis technology.For example, Noorjahan etc. utilizes spray TiO has been made in the technology of splashing2- HZSM-5 laminated films, degraded of this film to poisonous phenol and organic acid in waste water has very high Activity(Appl. Catal., B: Environmental, 2004, 47: 209-213);Garc í a etc. are with glass microsphere For carrier, supported titanium is prepared for using dip-coating method2Photochemical catalyst is used for degrade simulating pollution thing and municipal sewage treatment Sewage (the Appl. Catal., B of factory: Environmental, 2011, 103:294-301), good result is achieved. It can be seen that, in order to really realize the practical of photocatalysis technology, the immobilization of photochemical catalyst seems particularly important, await into One step research.
The method of traditional photoelectrocatalysis water decomposition hydrogen manufacturing is by N-type semiconductor light anode and P-type semiconductor photocathode string Yin, yang pole room is split using the gas separation membrane of printing opacity connection, centre.But with the lasting progress of reaction, anode chamber by In oxygen evolution reaction can gradually souring, cathode chamber can gradually become alkali due to evolving hydrogen reaction, and most of anode material prefers neutrality Or slight alkali environment, most of cathode material prefers slant acidity environment, therefore greatly limit the continuous of water decomposition reaction Carry out.
P-type semiconductor photocatalyst powder and N-type semiconductor photocatalyst powder are individually fixed in double by present invention proposition The surface of pole film both sides, and as the barrier film of yin, yang pole room, photoelectrocatalysis water decomposition hydrogen manufacturing is carried out, it is to be examined based on following Consider:1. under photoelectric action, water decomposition generation H occurs for Bipolar Membrane intermediate layer+ And OH-Ion, H+Ion permeable cation Exchange membrane enters cathode chamber, and generation evolving hydrogen reaction is consumed at negative electrode, OH-Ion permeable anion-exchange membrane enters anode Room, and generation oxygen evolution reaction is consumed at anode.Therefore, the stabilization of cathode chamber and anode chamber pH can be kept in theory, this Be conducive to the steady operation of semiconductor light-catalyst powder, reaction is continued progress.2. it is fixed with semiconductor using surface Oxygen anodic evolution reaction and cathode hydrogen evolution can be reacted effective by the Bipolar Membrane of photocatalyst powder as the barrier film of yin, yang pole room Ground Split is in two pole rooms, it is to avoid hydrogen, the oxygen generated intersects, further in conjunction with generation hydrone, not only increases water decomposition effect Rate, and the higher hydrogen of purity is made.3. consider from thermodynamics, the H of Bipolar Membrane water decomposition generation+More hold than hydrone Easily reduce, and OH-It is easier occur oxidation reaction than hydrone, further increases water decomposition efficiency.
The content of the invention
Problem of the invention is that in the prior art semiconductor light-catalyst powder easily reunite and reaction after it is difficult reclaim ask Topic, the problem of semiconductor light-catalyst photo-generate electron-hole low separation efficiency, semiconductor light-catalyst can not stablize, efficiently, hold The problem of continuous work, and a kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition is provided.
In order to solve the above problems, a kind of Bipolar Membrane surface powder state photochemical catalyst provided by the present invention is in water decomposition Application, the application is with the cation-exchange membrane of area load P-type semiconductor photocatalyst powder and area load N-type half The anion-exchange membrane of conductor photocatalyst powder is Bipolar Membrane, and constitutes cathode chamber and anode chamber's barrier film, by P-type semiconductor light Catalyst powder powder material is as negative electrode, using N-type semiconductor photocatalyst powder material as anode, after prepare 0.5 ~ 1.0 respectively M catholyte and anolyte, using xenon lamp as light source, applied voltage is under 0.5 ~ 2.0 V is acted on, to be carried out continuously Photoelectrocatalysis water decomposition hydrogen manufacturing.
The additional technical feature of such scheme is as follows.
The P-type semiconductor photocatalyst powder is Ag2O、NiO、Cu2One kind or its combination in O, CoO and SnO.
The N-type semiconductor photocatalyst powder is ZnO, TiO2、Fe2O3, CdS and SnO2In one kind or its combination.
The catholyte is H2SO4And HClO4One kind in solution, during anolyte is KOH and NaOH solution It is a kind of.
The Bipolar Membrane is composited by cation-exchange membrane, anion-exchange membrane.
A kind of application of above-mentioned the provided Bipolar Membrane surface powder state photochemical catalyst of the present invention in water decomposition is provided, with Prior art is compared, the light-catalysed Bipolar Membrane of area load powdered form of the present invention as cathode chamber and anode chamber every Film, the barrier film carries out photoelectrocatalysis water decomposition hydrogen under sunshine and electric field action, efficiently solves conductor photocatalysis After agent powder is easily reunited and reacted the problem of difficult recovery;Meanwhile, utilize the fixation anionic group in cation-exchange membrane and the moon Fixed cation group efficiently separates hole-electron respectively to hole and the sucking action of electronics in amberplex, solves The problem of photo-generate electron-hole low separation efficiency during semiconductor photoelectrocatalysielectrode of having determined;Importantly, boundary in Bipolar Membrane Water decomposition generation H occurs for surface layer+And OH-Ion, maintains yin, yang pole room pH stabilization, is conducive to semiconductor light-catalyst powder Stable, efficient, continuous firing.This invention carries out photoelectrocatalysis water decomposition hydrogen manufacturing, and hydrogen generation efficiency is up to 90 ~ 99.8%, hydrogen purity Up to 90 ~ 99.99%, continuously run 10 ~ 48 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize semiconductor powder Efficient, the continuous operation of state photochemical catalyst hydrogen production by water decomposition.
In summary, its advantage embodies a concentrated reflection of as follows with good effect.
The problem of present invention solves difficult recovery after semiconductor light-catalyst powder is easily reunited and reacted.
The present invention utilizes the fixation anionic group in cation-exchange membrane and cation fixed in anion-exchange membrane To hole and the sucking action of electronics, hole-electron is efficiently separated respectively for group, during solving semiconductor photoelectrocatalysielectrode The problem of photo-generate electron-hole low separation efficiency.
Using Bipolar Membrane intermediate layer water decomposition generation H occurs for the present invention+And OH-Ion, maintains yin, yang pole room pH Stabilization, solve semiconductor light-catalyst can not stablize, efficiently, continuous firing the problem of.
The present invention is combined Photocatalitic Technique of Semiconductor with Bipolar Membrane water decomposition technology, concerted catalysis water decomposition hydrogen manufacturing, production Hydrogen efficiency is up to 90 ~ 99.8%, and hydrogen purity is up to 90% ~ 99.99%, continuously runs 10 ~ 48 hours, tank voltage, hydrogen generation efficiency base This holding is constant, realizes efficient, the continuous operation of semiconductor powder state photochemical catalyst hydrogen production by water decomposition.
Brief description of the drawings
Fig. 1 is the schematic diagram that Bipolar Membrane both side surface of the present invention loads powdery photocatalyst.In figure:1- anion exchanges Film;2- cation-exchange membranes;3-P type semiconductor light-catalyst powder;4-N type semiconductor light-catalyst powder;Cation exchange Film and anion-exchange membrane, which are combined, obtains Bipolar Membrane.
Fig. 2 is the sodium carboxymethylcellulose crosslinking schematic diagram that the present invention prepares cation-exchange membrane.
Fig. 3 is the chitosan and glutaraldehyde cross-linking schematic diagram that the present invention prepares anion-exchange membrane.
Fig. 4 is the Cross Section Morphology figure of Bipolar Membrane in the present invention, and lower left corner illustration, which presents Bipolar Membrane, has good printing opacity Performance, is conducive to preferably absorbing sunshine;Upper right corner illustration is that Bipolar Membrane soaks the picture after 48 hours, table in distilled water Bright Bipolar Membrane is water insoluble, is conducive to it stably to work in aqueous.
Fig. 5 is the device that the present invention carries out photoelectrocatalysis experiment using the Bipolar Membrane of area load semiconductor catalyst powder Schematic diagram.
During Fig. 6 is the embodiment of the present invention 1, the both sides of preparation load powdery photocatalyst Bipolar Membrane and urged with unsupported respectively The contact angle of agent powder Bipolar Membrane.In figure, the cation-exchange membrane surface contact angle of (a)-unsupported catalyst fines;(b)- The anion-exchange membrane surface contact angle of unsupported catalyst fines Bipolar Membrane;(c)-area load Cu2O powder photocatalysts Cation-exchange membrane surface contact angle;(d)-area load TiO2The anion-exchange membrane surface contact angle of powder photocatalyst. Loading powdery photocatalyst Bipolar Membrane has smaller contact angle, shows that its hydrophily more preferably, promotes boundary in Bipolar Membrane Surface layer water decomposition, is conducive to the pH gradient for maintaining yin, yang pole room stable.
During Fig. 7 is the embodiment of the present invention 1, the voltage drop (IR) of load powdery photocatalyst Bipolar Membrane changes over time song Line chart.
During Fig. 8 is the embodiment of the present invention 1, the tank voltage for loading powdery photocatalyst Bipolar Membrane is bent with current density change Line chart.
During Fig. 9 is the embodiment of the present invention 1, the AC impedance curve map of powdery photocatalyst Bipolar Membrane is loaded.
During Figure 10 is the embodiment of the present invention 1, yin, yang pole room pH change curves.
During Figure 11 is the embodiment of the present invention 1, the energy expenditure figure of photoelectrocatalysis water decomposition hydrogen manufacturing.
During Figure 12 is the embodiment of the present invention 1, the production of photoelectrocatalysis water decomposition hydrogen manufacturing is carried out using supported catalyst Bipolar Membrane Hydrogen efficiency figure.
During Figure 13 is the embodiment of the present invention 1, photoelectrocatalysis water decomposition hydrogen manufacturing is carried out using unsupported catalyst Bipolar Membrane Hydrogen generation efficiency figure.
Embodiment
The embodiment to the present invention is further illustrated below.
Embodiment 1
Cathode chamber and the barrier film of anode chamber are used as using the light-catalysed Bipolar Membrane of area load powdered form(Wherein, Bipolar Membrane is constituted Cation-exchange membrane area load Ag2O semiconductor light-catalyst powder, constitutes the anion-exchange membrane area load of Bipolar Membrane TiO2Semiconductor light-catalyst powder), by Ag2O semiconductor light-catalysts dusty material is as negative electrode, by TiO2Semiconductor light is urged Agent dusty material is used as anode, 0.5 M H2SO4Solution is used as anode electrolysis as catholyte, 1.0 M KOH solution Liquid;Using xenon lamp as simulated solar radiant, applied voltage is under 1.0 V are acted on, to be carried out continuously photoelectrocatalysis water decomposition system Hydrogen.
Hydrogen generation efficiency result is bipolar using supported catalyst under same current density as shown in accompanying drawing 12 and accompanying drawing 13 Film has bigger hydrogen generation efficiency than unsupported catalyst Bipolar Membrane as barrier film, and especially under illumination condition, hydrogen generation efficiency is more Height, when current density is 90 mA cm-2When, hydrogen generation efficiency is up to 98.7%;Simultaneously using the method for chromatography of gases on-line checking, The purity for measuring hydrogen is 99.8%.After continuous operation 15 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and are realized and are partly led Efficient, the continuous operation of body powdery photocatalyst hydrogen production by water decomposition.
Embodiment 2
Cathode chamber and the barrier film of anode chamber are used as using the light-catalysed Bipolar Membrane of area load powdered form(Wherein, Bipolar Membrane is constituted Cation-exchange membrane area load Ag2O semiconductor light-catalyst powder, constitutes the anion-exchange membrane area load of Bipolar Membrane Fe2O3Semiconductor light-catalyst powder), by Ag2O semiconductor light-catalysts dusty material is as negative electrode, by Fe2O3Semiconductor light is urged Agent dusty material is used as anode, 0.5 M H2SO4Solution is used as anode electrolysis as catholyte, 0.5 M KOH solution Liquid;Using xenon lamp as simulated solar radiant, applied voltage is under 0.8 V is acted on, to be carried out continuously photoelectrocatalysis water decomposition system Hydrogen.
Result of study is shown, under same current density, more bipolar than unsupported catalyst using supported catalyst Bipolar Membrane Film has bigger hydrogen generation efficiency as barrier film, and especially under illumination condition, hydrogen generation efficiency is higher, when current density is 90 mA cm-2When, hydrogen generation efficiency is up to 99.1%;Simultaneously using the method for chromatography of gases on-line checking, the purity for measuring hydrogen is 99.9%. After continuous operation 10 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize semiconductor powder state photochemical catalyst decomposition water Efficient, the continuous operation of hydrogen manufacturing.
Embodiment 3
Cathode chamber and the barrier film of anode chamber are used as using the light-catalysed Bipolar Membrane of area load powdered form(Wherein, Bipolar Membrane is constituted Cation-exchange membrane area load CoO semiconductor light-catalyst powder, constitutes the anion-exchange membrane area load ZnO of Bipolar Membrane Semiconductor light-catalyst powder), using CoO semiconductor light-catalysts dusty material as negative electrode, by ZnO semiconductor light-catalyst powder Powder material is used as anode, 1.0 M H2SO4Solution is used as anolyte as catholyte, 1.0 M KOH solution;Adopt With xenon lamp as simulated solar radiant, applied voltage is under 1.0 V are acted on, to be carried out continuously photoelectrocatalysis water decomposition hydrogen manufacturing.
Result of study is shown, under same current density, more bipolar than unsupported catalyst using supported catalyst Bipolar Membrane Film has bigger hydrogen generation efficiency as barrier film, and especially under illumination condition, hydrogen generation efficiency is higher, when current density is 90 mA cm-2When, hydrogen generation efficiency is up to 99.3%;Simultaneously using the method for chromatography of gases on-line checking, the purity for measuring hydrogen is 99.7%. After continuous operation 18 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize semiconductor powder state photochemical catalyst decomposition water Efficient, the continuous operation of hydrogen manufacturing.
Embodiment 4
Cathode chamber and the barrier film of anode chamber are used as using the light-catalysed Bipolar Membrane of area load powdered form(Wherein, Bipolar Membrane is constituted Cation-exchange membrane area load Cu2O semiconductor light-catalyst powder, constitutes the anion-exchange membrane area load of Bipolar Membrane CdS semiconductor light-catalyst powder), by Cu2O semiconductor light-catalysts dusty material is as negative electrode, by CdS conductor photocatalysis Agent dusty material is used as anode, 0.5 M HClO4Solution is used as anode electrolysis as catholyte, 0.5 M NaOH solution Liquid;Using xenon lamp as simulated solar radiant, applied voltage is under 1.5 V are acted on, to be carried out continuously photoelectrocatalysis water decomposition system Hydrogen.
Result of study is shown, under same current density, more bipolar than unsupported catalyst using supported catalyst Bipolar Membrane Film has bigger hydrogen generation efficiency as barrier film, and especially under illumination condition, hydrogen generation efficiency is higher, when current density is 90 mA cm-2When, hydrogen generation efficiency is up to 99.5%;Simultaneously using the method for chromatography of gases on-line checking, the purity for measuring hydrogen is 99.6%. After continuous operation 16 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize semiconductor powder state photochemical catalyst decomposition water Efficient, the continuous operation of hydrogen manufacturing.
Embodiment 5
Cathode chamber and the barrier film of anode chamber are used as using the light-catalysed Bipolar Membrane of area load powdered form(Wherein, Bipolar Membrane is constituted Cation-exchange membrane area load NiO semiconductor light-catalyst powder, constitutes the anion-exchange membrane area load of Bipolar Membrane SnO2Semiconductor light-catalyst powder), using NiO semiconductor light-catalysts dusty material as negative electrode, by SnO2Conductor photocatalysis Agent dusty material is used as anode, 1.0 M HClO4Solution is used as anode electrolysis as catholyte, 1.0 M NaOH solution Liquid;Using xenon lamp as simulated solar radiant, applied voltage is under 2.0 V are acted on, to be carried out continuously photoelectrocatalysis water decomposition system Hydrogen.
Result of study is shown, under same current density, more bipolar than unsupported catalyst using supported catalyst Bipolar Membrane Film has bigger hydrogen generation efficiency as barrier film, and especially under illumination condition, hydrogen generation efficiency is higher, when current density is 90 mA cm-2When, hydrogen generation efficiency is up to 99.6%;Simultaneously using the method for chromatography of gases on-line checking, the purity for measuring hydrogen is 99.9%. After continuous operation 20 hours, tank voltage, hydrogen generation efficiency are held essentially constant, and realize semiconductor powder state photochemical catalyst decomposition water Efficient, the continuous operation of hydrogen manufacturing.
A kind of embodiment 1 ~ 5 described in the invention described above, the Bipolar Membrane area load powdered form catalyst provided exists Application in water decomposition, the preparation method of the Bipolar Membrane area load powdery photocatalyst of its application is as follows:
(1)Carboxymethyl cellulose or the cellulose acetate aqueous solution that preparation mass fraction is 2.0 ~ 5.0%, and 2.0 ~ 5.0% Polyvinyl alcohol or aqueous povidone solution, after mixing and are stirred continuously to form jelly, standing and defoaming 30 ~ 60 minutes, It is cast on clean band frame glass plate, room temperature obtains the cation-exchange membrane that thickness is 30 ~ 60 μm after air-drying.
(2)Weigh 0.5 ~ 2.0g P-type semiconductor photocatalyst powders, be scattered under ultrasonic oscillation 100 mL water or In absolute ethyl alcohol, continue concussion and be uniformly dispersed for 2.0 hours, the cation-exchange membrane surface of above-mentioned preparation is poured into, using metal Ion carries out crosslinking 5 ~ 15 minutes, and after 30 ~ 60 °C of drying, P-type semiconductor photocatalyst powder is attached to cation-exchange membrane table Face.
(3)By step(2)In cation-exchange membrane top and bottom overturn, be close to the surface of supported catalyst and soaked Glass plate on, another surface(The surface of i.e. unsupported catalyst)Upward.
(4)The aqueous solution of chitosan, polyimides or benzimidazole that preparation mass fraction is 2.0 ~ 5.0%, and 2.0 ~ 5.0% polyvinyl alcohol or aqueous povidone solution, after mixing and is stirred continuously to form jelly, standing and defoaming 30 ~ 60 Minute, it is cast in step(3)In cation-exchange membrane surface, room temperature air-dry after obtain thickness be 30 ~ 60 μm anion hand over Change film.
(5)Weigh 0.5 ~ 2.0g N-type semiconductor photocatalyst powders, be scattered under ultrasonic oscillation 100 mL water or In absolute ethyl alcohol, continue concussion and be uniformly dispersed for 2.0 hours, the anion-exchange membrane surface of above-mentioned preparation is poured into, using aldehydes Crosslinking agent carries out crosslinking 5 ~ 15 minutes, and after 30 ~ 60 °C of drying, N-type semiconductor photocatalyst powder is attached to anion-exchange membrane Surface.
Wherein, described described P-type semiconductor photocatalyst powder is Ag2O、NiO、Cu2One kind in O, CoO and SnO Or its combination;Described metal ion is Fe3+、Sn2+And Ti4+In one kind;Described N-type semiconductor photocatalyst powder is ZnO、TiO2、Fe2O3, CdS and SnO2In one kind or its combination;Described aldehyde crosslinking agent is in glutaraldehyde and butanedial It is a kind of;Described Bipolar Membrane is composited by cation-exchange membrane, anion-exchange membrane.
The Bipolar Membrane area load powdery photocatalyst of above-mentioned preparation, is by P-type semiconductor photocatalyst powder and N-type Semiconductor light-catalyst powder is carried on the both side surface of Bipolar Membrane respectively, and this film translucency is good and can effectively absorb the sun Anionic group and cation group are fixed in light, Bipolar Membrane has sucking action to hole and electronics respectively, can be by hole-electricity Son is efficiently separated;Water decomposition generation H occurs for Bipolar Membrane intermediate layer+And OH-Ion, maintains yin, yang pole room pH stabilization, Photocatalitic Technique of Semiconductor being combined with Bipolar Membrane water decomposition technology, concerted catalysis water decomposition hydrogen manufacturing, hydrogen generation efficiency is up to 90 ~ 99.8%, hydrogen purity is up to 90% ~ 99.99%, continuously runs 10 ~ 48 hours, tank voltage, hydrogen generation efficiency are held essentially constant, real Efficient, the continuous operation of semiconductor powder state photochemical catalyst water decomposition hydrogen manufacturing are showed.

Claims (5)

1. a kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition, the application is with area load p-type half The cation-exchange membrane of conductor photocatalyst powder and the anion-exchange membrane of area load N-type semiconductor photocatalyst powder are Bipolar Membrane, and cathode chamber and anode chamber's barrier film are constituted, using P-type semiconductor photocatalyst powder as negative electrode, by N-type semiconductor light Catalyst fines as anode, after prepare 0.5 ~ 1.0 M catholyte and anolyte respectively, light is used as using xenon lamp Source, applied voltage is under 0.5 ~ 2.0 V is acted on, to be carried out continuously photoelectrocatalysis water decomposition hydrogen manufacturing.
2. application of the Bipolar Membrane surface powder state photochemical catalyst as claimed in claim 1 in water decomposition, the P-type semiconductor Photocatalyst powder is Ag2O、NiO、Cu2One kind or its combination in O, CoO and SnO.
3. application of the Bipolar Membrane surface powder state photochemical catalyst as claimed in claim 1 in water decomposition, the N-type semiconductor Photocatalyst powder is ZnO, TiO2、Fe2O3, CdS and SnO2In one kind or its combination.
4. application of the Bipolar Membrane surface powder state photochemical catalyst as claimed in claim 1 in water decomposition, the catholyte Liquid is H2SO4And HClO4One kind in solution, anolyte is one kind in KOH and NaOH solution.
5. application of the Bipolar Membrane surface powder state photochemical catalyst as claimed in claim 1 in water decomposition, the Bipolar Membrane is It is composited by cation-exchange membrane, anion-exchange membrane.
CN201710272307.0A 2017-04-24 2017-04-24 A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition Active CN107012475B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710272307.0A CN107012475B (en) 2017-04-24 2017-04-24 A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710272307.0A CN107012475B (en) 2017-04-24 2017-04-24 A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition

Publications (2)

Publication Number Publication Date
CN107012475A true CN107012475A (en) 2017-08-04
CN107012475B CN107012475B (en) 2018-11-30

Family

ID=59448421

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710272307.0A Active CN107012475B (en) 2017-04-24 2017-04-24 A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition

Country Status (1)

Country Link
CN (1) CN107012475B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107779909A (en) * 2017-11-07 2018-03-09 太原师范学院 A kind of application of photoelectrocatalysis film
CN109082677A (en) * 2018-09-11 2018-12-25 太原师范学院 A kind of application of the Bipolar Membrane of area load graphite alkene in photoelectrocatalysis water decomposition
CN110079816A (en) * 2019-04-30 2019-08-02 太原师范学院 A kind of device and method of photoelectrocatalysis fixed nitrogen synthesis ammonia
CN111101142A (en) * 2018-10-26 2020-05-05 中国科学院金属研究所 Construction method of graphical integrated high-efficiency photocatalytic decomposition water system
CN114318388A (en) * 2022-01-25 2022-04-12 山西大学 Photoelectrocatalysis olefin hydrogenation device and application thereof
CN114672819A (en) * 2022-03-10 2022-06-28 东南大学 Method and system for preparing hydrogen by coupling photoelectrocatalysis PET plastic oxidation with water decomposition

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103159331A (en) * 2013-04-10 2013-06-19 重庆大学 Method and device for simultaneously carrying out wastewater treatment and power generation by using photocatalysis associated microbial fuel cell technology
CN105483747A (en) * 2016-01-22 2016-04-13 清华大学 Hydrogen production method and device through electrolysis of water

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103159331A (en) * 2013-04-10 2013-06-19 重庆大学 Method and device for simultaneously carrying out wastewater treatment and power generation by using photocatalysis associated microbial fuel cell technology
CN105483747A (en) * 2016-01-22 2016-04-13 清华大学 Hydrogen production method and device through electrolysis of water

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DAVID A. VERMAAS ET AL.: "Photo-assisted water splitting with bipolar membrane induced pH gradients for practical solar fuel devices", 《JOURNAL OF MATERIALS CHEMISTRY A》 *
JOHN A. TURNER: "A Nickel Finish Protects Silicon Photoanodes for Water Splitting", 《SCIENCE 》 *

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107779909A (en) * 2017-11-07 2018-03-09 太原师范学院 A kind of application of photoelectrocatalysis film
CN107779909B (en) * 2017-11-07 2019-05-07 太原师范学院 A kind of application of photoelectrocatalysis film
CN109082677A (en) * 2018-09-11 2018-12-25 太原师范学院 A kind of application of the Bipolar Membrane of area load graphite alkene in photoelectrocatalysis water decomposition
CN109082677B (en) * 2018-09-11 2019-09-03 太原师范学院 A kind of application of the Bipolar Membrane of area load graphite alkene in photoelectrocatalysis water decomposition
CN111101142A (en) * 2018-10-26 2020-05-05 中国科学院金属研究所 Construction method of graphical integrated high-efficiency photocatalytic decomposition water system
CN111101142B (en) * 2018-10-26 2021-05-18 中国科学院金属研究所 Construction method of graphical integrated high-efficiency photocatalytic decomposition water system
CN110079816A (en) * 2019-04-30 2019-08-02 太原师范学院 A kind of device and method of photoelectrocatalysis fixed nitrogen synthesis ammonia
CN110079816B (en) * 2019-04-30 2020-06-19 太原师范学院 Device and method for synthesizing ammonia by photoelectrocatalysis nitrogen fixation
CN114318388A (en) * 2022-01-25 2022-04-12 山西大学 Photoelectrocatalysis olefin hydrogenation device and application thereof
CN114318388B (en) * 2022-01-25 2023-12-26 山西大学 Photoelectrocatalysis olefin hydrogenation device and application thereof
CN114672819A (en) * 2022-03-10 2022-06-28 东南大学 Method and system for preparing hydrogen by coupling photoelectrocatalysis PET plastic oxidation with water decomposition

Also Published As

Publication number Publication date
CN107012475B (en) 2018-11-30

Similar Documents

Publication Publication Date Title
CN107012475B (en) A kind of application of Bipolar Membrane surface powder state photochemical catalyst in water decomposition
CN107099815B (en) A kind of application of Bipolar Membrane surface powder state photochemical catalyst in CO2 reduction
Bloor et al. Solar-driven water oxidation and decoupled hydrogen production mediated by an electron-coupled-proton buffer
Kim et al. Artificial photosynthesis for high‐value‐added chemicals: old material, new opportunity
Yang et al. One dimensional SnO2 NRs/Fe2O3 NTs with dual synergistic effects for photoelectrocatalytic reduction CO2 into methanol
CN107376897B (en) Oxidation catalysis film containing trimetal and preparation method and application thereof
CN101748423B (en) Efficient electrochemical reactor of electro-catalysis in-situ hydrogen peroxide
CN104340957B (en) Photosynthetical system two and the method for semiconductor hybrid system photocatalytic hydrogen production by water decomposition gas
CN105293688B (en) The system that nitrate nitrogen in water removal is removed in a kind of coupled biological anode electro-catalysis
CN104117391B (en) A kind of photoelectrocatalysis film preparation for hydrogen production by water decomposition
CN103981537B (en) The preparation method of the Pd/3DOM TiO2/BDD electrode of a kind of photoelectrocatalysis reduction treatment organic pollution and application thereof
WO2023160261A1 (en) System and method for capture and electric regeneration and synchronous conversion of co2
WO2005063393A1 (en) Method for electrolyzing water using organic photocatalyst
CN111097402B (en) Nano beta-lead dioxide catalyst, preparation method and application thereof
CN108842163B (en) Application of bipolar membrane taking copper-metal organic framework material as middle interface layer in photoelectrocatalysis nitrogen fixation
CN106876722A (en) A kind of Carbon dioxide electrochemical reduction gas-diffusion electrode and its preparation and application
KR100699556B1 (en) The equipment for producing hydrogen gas by using photocatalyst and biocatalyst
CN108842164B (en) Bipolar membrane with copper-metal organic framework material as middle interface layer and preparation method thereof
CN105293644B (en) Optical electro-chemistry electrolysis installation and the battery lead plate for the optical electro-chemistry electrolysis installation
CN105714326B (en) Suspension electro-catalysis solution aquatic products hydrogen production device
CN107916433B (en) The preparation of micro nano structure zinc electrode and zinc electrode and application
CN209537276U (en) A kind of photoelectrocatalysis microorganism electrolysis cell device
CN108866567B (en) Bipolar membrane with zinc-metal organic framework material as middle interface layer and preparation method thereof
CN205170459U (en) Optical electro -Chemistry electrolysis equipment and be used for this optical electro -Chemistry electrolysis equipment's plate electrode
Yang et al. Light-Driven Fuel Cell with a 2D/3D Hierarchical CuS@ MnS Z-Scheme Catalyst for H2O2 Generation

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