CN101665276B - Composite activated carbon fiber polar plate - Google Patents

Composite activated carbon fiber polar plate Download PDF

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CN101665276B
CN101665276B CN2009101529651A CN200910152965A CN101665276B CN 101665276 B CN101665276 B CN 101665276B CN 2009101529651 A CN2009101529651 A CN 2009101529651A CN 200910152965 A CN200910152965 A CN 200910152965A CN 101665276 B CN101665276 B CN 101665276B
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activated carbon
carbon fiber
polar plate
ruthenium
dioxide
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CN101665276A (en
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王万寿
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HANGZHOU HUISHUI TECHNOLOGY Co Ltd
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Abstract

The invention relates to a composite activated carbon fiber polar plate which takes activated carbon fiber as a carrier and is sintered with iridic oxide and ruthenium dioxide on the surface thereof, wherein iridic oxide accounts for 0.3%-0.5% of activated carbon, ruthenium dioxide accounts for 0.1%-0.3% of activated carbon. In the invention, rare metal iridium and ruthenium are added on an ACF plate, thus enabling an electrochemical reactor to have better processing effect.

Description

Composite activated carbon fiber polar plate
Technical field
The invention belongs to technical field of sewage, particularly relate to the dispose of sewage pole plate of usefulness of a kind of electrochemical process, more specifically, relate to a kind of composite activated carbon fiber polar plate.
Background technology
In recent years, utilize solvability or the organic research of suspended state bio-refractory in the electrochemical method treating water more and more.This mainly concentrates on anodic oxidation and cathodic reduction to aspects such as the principle method of removing pollutent and Technologies.Traditional plate material has iron, aluminium etc., and newer invention and research mainly are at utilizing the anodic oxidation degradation of organic substances, and chamber, the two poles of the earth electrolyzer also uses the oxygen evolution potential electrode usually, as PbO 2And SnO 2Electrode, the effect of cathodic electricity catalyzed degradation does not then cause enough attention.
Utilize electrochemical techniques degradation of organic substances between negative electrode, it mainly is the strong oxidizing property intermediate material oxidize contaminants that produces by electrochemistry.At graphite or reticulated vitreous carbon cathode surface two electronic reduction reactions generation H takes place by dissolved molecular oxygen at cathode compartment normally 2O 2, under slightly acidic (pH-3) condition and Fe 2+Generation Fenton reaction, the OH of generation strong oxidizing property, do not have selectively rapid and three kinds of forms reactions of aromatic organic compounds generation: the addition reaction and the electron-transfer reaction of dehydrogenation reaction, destruction C=C unsaturated link(age) make it that chemical degradation take place.Fe in the reaction 3+Can become Fe in cathodic reduction 2+, continue and H 2O 2The Fenton reaction takes place, so Fe 2+In reaction, play the effect of catalyzer.The Fenton reaction mechanism is as follows:
O 2(g)+2H ++2e→H 2O 2
Fe 2++H 2O 2+H +→Fe 3++H 2O+OH
OH+RH→R+H 2O
Fe 3+The reversible Fe of+e 2+
The essence of Fenton method is the Fe that will produce in the electrochemical reaction process 2+And H 2O 2Lasting source as Fenton reagent.The Fenton method is compared with light Fenton method, has automatic generation H 2O 2More perfect, the H of mechanism 2O 2Utilization ratio height, the more advantages such as (except that the oxygenizement of OH, also having anodic oxidation, electro-adsorption) of organic matter degradation factor.Therefore, the Fenton method is one of important directions of Fenton method development.
In the Fenton method, the selection of cathode plate material is also few at present, and wherein a kind of is activated carbon fiber (ACF) pole plate.Activated carbon fiber (ACF) also claims fibrous activated carbon, is high-efficiency activated sorbing material and environment-friendly engineering material that performance is better than gac.Its carbon atom above 50% is positioned at surfaces externally and internally, is built into unique adsorption structure, is called as the superficiality solid.It is by fibrous presoma, forms through the certain procedure carbonization-activation.The difference of precursor material, the production technique of ACF is also obviously different with the structure of product.The production of ACF generally is that the organic precursor fiber is carried out stabilization treatment under 200 ℃~400 ℃ of low temperature, carries out (charing) activation subsequently.Activation method commonly used mainly contains: with the physical activation method of CO2 or water vapor and use ZnCI2, H3PO, H2PO4, the chemical activation method of KOH, treatment temp is between 700 ℃~1000 ℃, different treatment process (time, temperature, activation dosage etc.) corresponding product has different pore textures and performance.Organic fibre as the ACF presoma mainly contains cellulose base, the PAN base, and the phenolic aldehyde base, asphaltic base, PVA-based, vinylbenzene/olefin copolymer and lignin fibre etc.Flourishing specific surface area and narrower pore size distribution make it have adsorption/desorption speed and bigger loading capacity faster, and because it can be processed as different shapes such as felt, cloth, paper easily, and have the acid and alkali-resistance corrosion resistance characteristic, can be widely used in industrial aspect such as daily lifes such as water treatment, deodorizing and liquid phase decolouring, catalyst, gas delivery.ACF has following characteristics:
(1) there is the adsorption and diffusion effect in interfibrous space in the pore structure, and its micropore is positioned at the surface, and the aperture is little, can produce the capillary condensation effect, has strengthened adsorption effect.
(2) loading capacity is big, and adsorption process is mainly the fiber surface micro-porous adsorption, and adsorption layer is very thin, thereby rate of adsorption is very fast.
(3) a large amount of oxygen-containing functional groups is contained on the surface, as-OH, C=O ,-COOH ,-OC nH 2n+1, also have the C-N key, N-N key etc., easy and polar adsorption matter molecule forms hydrogen bond; It can also be to the II electron production inductive capacity in the phenyl ring, so have good adsorptive power to containing water soluble organic substances such as oxygen, chlorine, aromatic ring simultaneously.
Aspect electrochemical applications, ACF has absorption, conduction and catalytic performance, be a kind of carbon electrode material, also be used as a kind of accurate three-dimensional structure electrode and be used for the organism that electro-adsorption is removed water, and the charcoal fibre felt electrode also be used as cathodic reduction generation H with applications well prospect 2O 2
Summary of the invention
The purpose of this invention is to provide a kind of electrochemical treatment that is suitable for, the composite activated carbon fiber polar plate of better effects if.
For this reason, the technical solution used in the present invention is as follows: composite activated carbon fiber polar plate is a carrier with the activated carbon fiber, and it is characterized in that: surperficial sintering has iridium dioxide and ruthenium dioxide.
Further, described iridium dioxide is the 0.3%-0.5% of activated carbon fiber, and ruthenium dioxide is the 0.1%-0.3% (being weight ratio) of activated carbon fiber.
Described activated carbon fiber is a graphite felt.
Preparation method of the present invention is such: at first prepare activated carbon fiber polar plate, at quantitative iridium dioxide of surface coated and ruthenium dioxide, then at 1600-1800 ℃ of sintering, ruthenium, iridium are got attached to polar board surface.
The present invention follows catalyzed reaction owing to added rare metal iridium, ruthenium on the ACF plate in reaction process, produce the higher H of concentration 2O 2, and produce the stronger hydroxyl of oxidisability, thus make electrochemical reactor that better treatment effect is arranged.
Embodiment
One, the preparation of compound polar plate
At first prepare the graphite felt pole plate, control thickness is 5mm, and heatproof is 2000 ℃; At the iridium dioxide of surface coated 0.4% and 0.2% ruthenium dioxide; 1700 ℃ of high temperature sinterings 40 minutes.
The comparison of two, invention effect
Respectively with equal area pole plate of the present invention, ACF plate and graphite cake as negative electrode, anode adopts the iron pole plate.By colourity in the electrochemical treatment dyeing and printing sewage and COD.Reaction times is 3 minutes, 5 minutes, 7 minutes, voltage 110V, electric current 3A.Former water COD is 850mg/l.Result is as shown in the table.
Figure G2009101529651D00041
H when pole plate of the present invention, ACF and graphite cake are negative electrode 2O 2The contrast of electrochemistry growing amount, as shown in the table.Unit: umolL -1
3min 5min 7min
The present invention 300 570 670
ACF 270 450 480
Graphite cake 50 70 90
The H that electrochemical reaction produced 2O 2Effective degradable organic pollutant.In solution, there is Fe 2+In the time of (1.0mmolL-1), Fe 2+The H that can produce with electrochemistry 2O 2The homogeneous catalytic reaction generation takes place have the cause of highly active OH, H 2O 2When concentration was high, COD and chroma removal rate relatively also improved.
As seen, the present invention can obviously improve the performance of ACF pole plate, finishes goal of the invention.

Claims (3)

1. composite activated carbon fiber polar plate, with the activated carbon fiber is carrier, it is characterized in that: surperficial sintering has iridium dioxide and ruthenium dioxide, and described iridium dioxide is the 0.3%-0.5% of activated carbon fiber, and ruthenium dioxide is the 0.1%-0.3% (being weight ratio) of activated carbon fiber.
2. composite activated carbon fiber polar plate as claimed in claim 1 is characterized in that: described activated carbon fiber is a graphite felt.
3. composite activated carbon fiber polar plate as claimed in claim 1 or 2, it is characterized in that: it is at first to prepare activated carbon fiber polar plate, at quantitative iridium dioxide of surface coated and ruthenium dioxide,, ruthenium, iridium are got attached to polar board surface then at 1600-1800 ℃ of sintering.
CN2009101529651A 2009-09-23 2009-09-23 Composite activated carbon fiber polar plate Active CN101665276B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106400048B (en) * 2016-09-10 2018-07-20 华南理工大学 A kind of electric Fenton cathode material and preparation method thereof based on lignin
CN107188273A (en) * 2017-04-27 2017-09-22 华中科技大学 A kind of preparation method of three-dimensional carbon metal oxides electro catalytic electrode
CN109576733B (en) * 2018-11-22 2020-10-27 太原理工大学 Preparation method of carbon fiber loaded chlorine evolution catalytic electrode

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1189395A (en) * 1998-01-12 1998-08-05 南开大学 Compounded active carbon fibre solid catalyst
CN1293263A (en) * 2000-09-30 2001-05-02 华东师范大学 Non-crack nm-class Ti-based anode and its preparing process
US6517906B1 (en) * 2000-06-21 2003-02-11 Board Of Trustees Of University Of Illinois Activated organic coatings on a fiber substrate
CN1792936A (en) * 2005-12-09 2006-06-28 中山大学 Composite active carbon fibre and preparation process thereof
CN1943851A (en) * 2006-10-13 2007-04-11 中国石油大学(华东) Carbon base optic catalytic composite material and its preparing method and using method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1189395A (en) * 1998-01-12 1998-08-05 南开大学 Compounded active carbon fibre solid catalyst
US6517906B1 (en) * 2000-06-21 2003-02-11 Board Of Trustees Of University Of Illinois Activated organic coatings on a fiber substrate
CN1293263A (en) * 2000-09-30 2001-05-02 华东师范大学 Non-crack nm-class Ti-based anode and its preparing process
CN1792936A (en) * 2005-12-09 2006-06-28 中山大学 Composite active carbon fibre and preparation process thereof
CN1943851A (en) * 2006-10-13 2007-04-11 中国石油大学(华东) Carbon base optic catalytic composite material and its preparing method and using method

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