CN105195150B - One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst - Google Patents

One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst Download PDF

Info

Publication number
CN105195150B
CN105195150B CN201510677383.0A CN201510677383A CN105195150B CN 105195150 B CN105195150 B CN 105195150B CN 201510677383 A CN201510677383 A CN 201510677383A CN 105195150 B CN105195150 B CN 105195150B
Authority
CN
China
Prior art keywords
feal
class fenton
composite film
fenton catalyst
efficient
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
CN201510677383.0A
Other languages
Chinese (zh)
Other versions
CN105195150A (en
Inventor
姜兆华
王建康
姚忠平
夏琦兴
王志江
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.)
Harbin Institute of Technology
Original Assignee
Harbin Institute 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 Harbin Institute of Technology filed Critical Harbin Institute of Technology
Priority to CN201510677383.0A priority Critical patent/CN105195150B/en
Publication of CN105195150A publication Critical patent/CN105195150A/en
Application granted granted Critical
Publication of CN105195150B publication Critical patent/CN105195150B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Catalysts (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst, it is related to a kind of methods and applications for preparing class fenton catalyst.The invention aims to solve existing class fenton catalyst to have the problem of separation and recovery of catalyst is using hardly possible, poor mechanical property.Method:First, carbon steel polishing;2nd, bright carbon steel is connected with positive source, is used as anode;Stainless steel electrolytic groove is connected with power cathode, is used as negative electrode;3rd, plasma electrolysis reaction is adopted, efficient Fe is obtained3O4/FeAl2O4Composite film class fenton catalyst.Fe prepared by the present invention3O4/FeAl2O4The degradation efficiency of composite film class fenton catalyst Pyrogentisinic Acid in 60min is up to 100%.The present invention can obtain one kind and prepare efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst.

Description

One kind prepares efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst and Using
Technical field
The present invention relates to a kind of methods and applications for preparing class fenton catalyst.
Background technology
With economic fast development and the continuous growth of population, the discharge of industrial wastewater, agricultural effluent and sanitary wastewater Amount and discharge species are continuously increased, and harm of the Organic Pollutants In Water to environment and the mankind is increasingly serious.In order to greatest extent Ground reduction water pollution, improvement water quality condition, have weight to the advanced treating before discharge of wastewater for the problem of curbing environmental pollution The meaning wanted.
Fenton oxidation method is mixed as a kind of high-level oxidation technology using a certain amount of ferrous ion with hydrogen peroxide, Strong oxidizing property hydroxyl radical free radical is produced under certain pH value and carrys out degradable organic pollutant.Because Fenton oxidation method is simple to operate, drop Efficiency high, device simple are solved, in addition using Fe2+As catalyst, and iron material is abundant, bio-compatibility, with low cost, therefore Fenton oxidation method is favored extensively.
However, homogeneous Fenton oxidation method is present, pH applications are narrow, produce a large amount of iron cements after reaction, need to be pre-adjusted waste water The problems such as pH value.In order to overcome the shortcoming that homogeneous Fenton oxidation method is present, class Fenton technology, out-phase class Fenton are further developed Catalyst applicable pH range is wide can even degrade under near-neutral sulfite deinking, catalyst recoverable, without iron cement generation, H2O2Profit With rate height by domestic and international extensive concern.
Traditional different in nature class fenton catalyst is mainly powder body material, there is catalyst and recycles difficult, poor mechanical property Shortcoming
The content of the invention
The invention aims to solve existing class fenton catalyst to there is separation and recovery of catalyst using difficult, mechanical property Poor the problem of, and one kind is provided and prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst.
One kind prepares efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst, is to complete according to the following steps 's:
First, carbon steel polishing:Use 500 mesh silicon carbide papers, 1000 mesh silicon carbide papers, 1500 mesh water millings successively first The surface that paper mesh, 2000 mesh silicon carbide papers and 2500 mesh silicon carbide papers carry out being polishing to carbon steel to the surface of carbon steel is minute surface;So Afterwards using the surface 3 times~5 times of deionized water rinsing carbon steel, the surface 3 times~5 times that absolute ethyl alcohol rinses carbon steel is reused, most Dried up afterwards using hair-dryer, obtain the carbon steel of light;
2nd, the bright carbon steel obtained in step one is placed in the electrolyte in stainless steel electrolytic groove, bright carbon steel It is connected with positive source, is used as anode;Stainless steel electrolytic groove is connected with power cathode, is used as negative electrode;
3rd, powered using the pulse power, be 1A/cm in current density2~20A/cm2, supply frequency 100Hz~3000Hz, The pH value of 10 DEG C~50 DEG C of electrolyte temperature and electrolyte is progress plasma electrolytic oxidation reaction under conditions of 8.0~14.0 5min~30min, obtains efficient Fe3O4/FeAl2O4Composite film class fenton catalyst;
Electrolyte described in step 3 is made up of main film forming agent and additive, and solvent is water;Described main film forming agent Concentration is 1g/L~20g/L;The concentration of described additive is 0.1g/L~2g/L.
Efficient Fe3O4/FeAl2O4Composite film class fenton catalyst is used to handle the waste water containing phenol.
Advantage of the present invention:
First, electrolyte system of the invention is simple, economical and practical, and preparation technology is simple;
2nd, the present invention prepares Fe using plasma electrolysis oxidation method first3O4/FeAl2O4Composite film class Fenton is catalyzed Agent;
3rd, present invention gained film layer has multistage nested pore structure, and Film color is grey black, and average pore size is 6.4 μm;
4th, efficient Fe prepared by the present invention3O4/FeAl2O4Composite film class fenton catalyst is easily recycled, iron-free Mud is produced, with excellent stability, and processing cost is cheap, technique simple, thus is had a good application prospect;
5th, the present invention is successfully prepared efficient Fe using plasma electrolysis deposition technique on carbon steel3O4/FeAl2O4It is compound Film layer class fenton catalyst, can be mass-produced;
6th, Fe prepared by the present invention3O4/FeAl2O4The degraded of composite film class fenton catalyst Pyrogentisinic Acid in 60min Efficiency is up to 100%.
The present invention can obtain one kind and prepare efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst.
Brief description of the drawings
Fig. 1 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The XRD spectrum of composite film class fenton catalyst;Figure " ▲ " represents Fe3O4 diffraction maximums in 1, and "●" represents FeAl2O4Diffraction maximum;
Fig. 2 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The Fe 2p3/2 couple of composite film class fenton catalyst The XPS spectrum peak answered;
Fig. 3 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst amplifies 1000 times SEM schemes;
Fig. 4 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The digital photograph of composite film class fenton catalyst;
Fig. 5 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst amplifies 5000 times SEM schemes;
Fig. 6 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The drop of composite film class fenton catalyst degrading waste water Solve efficiency versus time curve figure.
Embodiment
Embodiment one:Present embodiment is that one kind prepares efficient Fe3O4/FeAl2O4Composite film class Fenton is catalyzed The method of agent is completed according to the following steps:
First, carbon steel polishing:Use 500 mesh silicon carbide papers, 1000 mesh silicon carbide papers, 1500 mesh water millings successively first The surface that paper mesh, 2000 mesh silicon carbide papers and 2500 mesh silicon carbide papers carry out being polishing to carbon steel to the surface of carbon steel is minute surface;So Afterwards using the surface 3 times~5 times of deionized water rinsing carbon steel, the surface 3 times~5 times that absolute ethyl alcohol rinses carbon steel is reused, most Dried up afterwards using hair-dryer, obtain the carbon steel of light;
2nd, the bright carbon steel obtained in step one is placed in the electrolyte in stainless steel electrolytic groove, bright carbon steel It is connected with positive source, is used as anode;Stainless steel electrolytic groove is connected with power cathode, is used as negative electrode;
3rd, powered using the pulse power, be 1A/cm in current density2~20A/cm2, supply frequency 100Hz~3000Hz, The pH value of 10 DEG C~50 DEG C of electrolyte temperature and electrolyte is progress plasma electrolytic oxidation reaction under conditions of 8.0~14.0 5min~30min, obtains efficient Fe3O4/FeAl2O4Composite film class fenton catalyst;
Electrolyte described in step 3 is made up of main film forming agent and additive, and solvent is water;Described main film forming agent Concentration is 1g/L~20g/L;The concentration of described additive is 0.1g/L~2g/L.
Present embodiment advantage:
First, the electrolyte system of present embodiment is simple, economical and practical, and preparation technology is simple;
2nd, present embodiment prepares Fe using plasma electrolysis oxidation method first3O4/FeAl2O4Composite film class Fenton is urged Agent;
3rd, film layer obtained by present embodiment has multistage nested pore structure, and Film color is grey black, and average pore size is 6.4 μm;
4th, efficient Fe prepared by present embodiment3O4/FeAl2O4Composite film class fenton catalyst is easily recycled, Produced without iron cement, with excellent stability, and processing cost is cheap, technique simple, thus has a good application prospect;
5th, present embodiment is successfully prepared efficient Fe using plasma electrolysis deposition technique on carbon steel3O4/FeAl2O4 Composite film class fenton catalyst, can be mass-produced;
6th, Fe prepared by present embodiment3O4/FeAl2O4Composite film class fenton catalyst Pyrogentisinic Acid in 60min Degradation efficiency is up to 100%.
Present embodiment can obtain one kind and prepare efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst.
Embodiment two:Present embodiment is with the difference of embodiment one:Described main film forming agent is aluminium Sour sodium.Other steps are identical with embodiment one.
Embodiment three:One of present embodiment and embodiment one or two difference is:Described addition Agent is a hydration sodium hypophosphite.Other steps are identical with embodiment one or two.
Embodiment four:One of present embodiment and embodiment one to three difference is:Institute in step one The carbon steel stated is Q235 carbon steels.Other steps are identical with embodiment one to three.
Embodiment five:One of present embodiment and embodiment one to four difference is:Adopted in step 3 Powered with the pulse power, be 8A/cm in current density2~20A/cm2, supply frequency 100Hz~3000Hz, electrolyte temperature 10 DEG C~50 DEG C and electrolyte ph be to carry out plasma electrolytic oxidation reaction 5min~30min under conditions of 8.0~14.0, obtain To efficient Fe3O4/FeAl2O4Composite film class fenton catalyst.Other steps are identical with embodiment one to four.
Embodiment six:One of present embodiment and embodiment one to five difference is:Adopted in step 3 Powered with the pulse power, be 10A/cm in current density2~20A/cm2, supply frequency 500Hz~3000Hz, electrolyte temperature The pH value of 10 DEG C~50 DEG C and electrolyte be carry out under conditions of 8.0~14.0 plasma electrolytic oxidation reaction 5min~ 30min, obtains efficient Fe3O4/FeAl2O4Composite film class fenton catalyst.Other steps and the phase of embodiment one to five Together.
Embodiment seven:One of present embodiment and embodiment one to six difference is:Institute in step 3 The electrolyte stated is made up of main film forming agent and additive, and solvent is water;The concentration of described main film forming agent is 5g/L~20g/L; The concentration of described additive is 0.5g/L~2g/L.Other steps are identical with embodiment one to six.
Embodiment eight:One of present embodiment and embodiment one to seven difference is:Institute in step 3 The electrolyte stated is made up of main film forming agent and additive, and solvent is water;The concentration of described main film forming agent is 10g/L~20g/L; The concentration of described additive is 1g/L~2g/L.Other steps are identical with embodiment one to seven.
Embodiment nine:Present embodiment is efficient Fe3O4/FeAl2O4Composite film class fenton catalyst is used to locate Manage the waste water containing phenol.
Embodiment ten:The difference of present embodiment and embodiment nine is:By efficient Fe3O4/ FeAl2O4Composite film class fenton catalyst is added in the waste water containing phenol, and low whipping speed is 100r/min~500r/ The hydrogen peroxide that mass fraction is 30% is added under min, then low whipping speed is stirring reaction under 100r/min~500r/min 45min~60min, water after being handled;Described efficient Fe3O4/FeAl2O4The geometric surface of composite film class fenton catalyst Product and the volume ratio (5cm in the waste water containing phenol2~10cm2):50mL;Phenol in the described waste water containing phenol Concentration is 20mg/L~50mg/L;Described efficient Fe3O4/FeAl2O4The geometric area and matter of composite film class fenton catalyst The volume ratio for measuring the hydrogen peroxide that fraction is 30% is (5cm2~10cm2):0.034mL.Other are identical with embodiment nine.
Beneficial effects of the present invention are verified using following examples:
Embodiment one:One kind prepares efficient Fe3O4/FeAl2O4The method of composite film class fenton catalyst is by following step Suddenly complete:
First, carbon steel polishing:Use 500 mesh silicon carbide papers, 1000 mesh silicon carbide papers, 1500 mesh water millings successively first The surface that paper mesh, 2000 mesh silicon carbide papers and 2500 mesh silicon carbide papers carry out being polishing to carbon steel to the surface of carbon steel is minute surface;So Afterwards using the surface 4 times of deionized water rinsing carbon steel, the surface 4 times that absolute ethyl alcohol rinses carbon steel is reused, finally using blowing Machine is dried up, and obtains the carbon steel of light;
Carbon steel described in step one is Q235 carbon steels;
2nd, the bright carbon steel obtained in step one is placed in the electrolyte in stainless steel electrolytic groove, bright carbon steel It is connected with positive source, is used as anode;Stainless steel electrolytic groove is connected with power cathode, is used as negative electrode;
3rd, powered using the pulse power, be 15A/cm in current density2, supply frequency 2000Hz, 30 DEG C of electrolyte temperature PH value with electrolyte is progress plasma electrolytic oxidation reaction 15min under conditions of 13.0, obtains efficient Fe3O4/ FeAl2O4Composite film class fenton catalyst;
Electrolyte described in step 3 is made up of main film forming agent and additive, and solvent is water;Described main film forming agent Concentration is 10g/L;The concentration of described additive is 1.5g/L;
Main film forming agent described in step 3 is sodium aluminate;
Additive described in step 3 is a hydration sodium hypophosphite.
Fig. 1 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The XRD spectrum of composite film class fenton catalyst;Figure " ▲ " represents Fe3O4 diffraction maximums in 1, and "●" represents FeAl2O4Diffraction maximum;
Composite film necessarily contains Fe as can be seen from Figure 13O4, FeAl may be contained2O4
Fig. 2 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The Fe 2p3/2 couple of composite film class fenton catalyst The XPS spectrum peak answered;
As can be seen from Figure 2,709.9eV, 713.4eV correspond to Fe after swarming3O4In Fe2+、Fe3+, 709.9eV, 713.4 EV corresponds to FeAl2O4In Fe2+、Fe3+, thus, it can be known that the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film Class fenton catalyst composition is by Fe3O4And FeAl2O4Constitute.
Fig. 3 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst amplifies 1000 times SEM schemes;
Fig. 4 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The digital photograph of composite film class fenton catalyst;
Fig. 5 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst amplifies 5000 times SEM schemes;
It was found from Fig. 3 and Fig. 5, the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst is Multistage nesting pore structure, average pore size is 6.4 μm;
As can be seen from Figure 4, the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The color of composite film class fenton catalyst To show grey black.
By 6cm2Efficient Fe3O4/FeAl2O4Composite film class fenton catalyst is added to 50mL phenol concentrations for 35mg/L The waste water containing phenol in, low whipping speed is that the hydrogen peroxide that 0.034mL mass fractions are 30% is added under 150r/min, then Low whipping speed is stirring reaction 0min~60min, water after being handled under 150r/min;As shown in Figure 6.
Fig. 6 is the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4The drop of composite film class fenton catalyst degrading waste water Solve efficiency versus time curve figure.
As can be seen from Figure 6, the Fe that the step 3 of embodiment one is obtained3O4/FeAl2O4Composite film class fenton catalyst is in 60min The degradation efficiency of interior Pyrogentisinic Acid is up to 100%.

Claims (1)

1. a kind of efficient Fe3O4/FeAl2O4The application of composite film class fenton catalyst, it is characterised in that efficient Fe3O4/ FeAl2O4Composite film class fenton catalyst is used to handle the waste water containing phenol;
Described efficient Fe3O4/FeAl2O4It is by following step that composite film class fenton catalyst, which is used to handle the waste water containing phenol, Suddenly complete:
By efficient Fe3O4/FeAl2O4Composite film class fenton catalyst is added in the waste water containing phenol, and low whipping speed is The hydrogen peroxide that mass fraction is 30% is added under 100r/min~500r/min, then low whipping speed is 100r/min~500r/ Stirring reaction 45min~60min, water after being handled under min;Described efficient Fe3O4/FeAl2O4Composite film class Fenton is urged The geometric area of agent and the volume ratio (5cm in the waste water containing phenol2~10cm2):50mL;Described is useless containing phenol The concentration of phenol is 20mg/L~50mg/L in water;Described efficient Fe3O4/FeAl2O4Composite film class fenton catalyst The volume ratio for the hydrogen peroxide that geometric area is 30% with mass fraction is (5cm2~10cm2):0.034mL;
Described efficient Fe3O4/FeAl2O4The preparation method of composite film class fenton catalyst is completed according to the following steps:
First, carbon steel polishing:Use 500 mesh silicon carbide papers, 1000 mesh silicon carbide papers, 1500 mesh silicon carbide papers successively first The surface that mesh, 2000 mesh silicon carbide papers and 2500 mesh silicon carbide papers carry out being polishing to carbon steel to the surface of carbon steel is minute surface;Then Using the surface 4 times of deionized water rinsing carbon steel, the surface 4 times that absolute ethyl alcohol rinses carbon steel is reused, finally using hair-dryer Drying, obtains the carbon steel of light;
Carbon steel described in step one is Q235 carbon steels;
2nd, the bright carbon steel obtained in step one is placed in the electrolyte in stainless steel electrolytic groove, bright carbon steel and electricity Source positive pole is connected, and is used as anode;Stainless steel electrolytic groove is connected with power cathode, is used as negative electrode;
3rd, powered using the pulse power, be 15A/cm in current density2, supply frequency 2000Hz, 30 DEG C of electrolyte temperature and electricity The pH value for solving liquid is progress plasma electrolytic oxidation reaction 15min under conditions of 13.0, obtains efficient Fe3O4/FeAl2O4It is multiple Close film layer class fenton catalyst;
Electrolyte described in step 3 is made up of main film forming agent and additive, and solvent is water;The concentration of described main film forming agent For 10g/L;The concentration of described additive is 1.5g/L;
Main film forming agent described in step 3 is sodium aluminate;
Additive described in step 3 is a hydration sodium hypophosphite;
Described efficient Fe3O4/FeAl2O4Composite film class fenton catalyst degradation efficiency of Pyrogentisinic Acid in 60min is reachable 100%.
CN201510677383.0A 2015-10-16 2015-10-16 One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst Active CN105195150B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510677383.0A CN105195150B (en) 2015-10-16 2015-10-16 One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510677383.0A CN105195150B (en) 2015-10-16 2015-10-16 One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst

Publications (2)

Publication Number Publication Date
CN105195150A CN105195150A (en) 2015-12-30
CN105195150B true CN105195150B (en) 2017-11-03

Family

ID=54943309

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510677383.0A Active CN105195150B (en) 2015-10-16 2015-10-16 One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst

Country Status (1)

Country Link
CN (1) CN105195150B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105536812A (en) * 2016-01-08 2016-05-04 清华大学 Nano Fe3O4/Mn3O4 composite material and preparation method and application thereof
CN106345472A (en) * 2016-08-05 2017-01-25 哈尔滨工业大学 Method for preparing high-efficient Fenton-like catalyst of sulphur modified iron-based composite material solid acid ceramic film layer and application
CN107245749B (en) * 2017-06-09 2019-03-12 哈尔滨工业大学 A kind of method and application preparing sulfur doping out-phase fenton catalyst in titanium alloy surface

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1762895A (en) * 2005-08-10 2006-04-26 武汉科技大学 Synthetic ferro-aluminum spinel and its preparation method
US8808522B2 (en) * 2011-09-07 2014-08-19 National Chung Hsing University Method for forming oxide film by plasma electrolytic oxidation
CN104437502B (en) * 2014-12-15 2017-01-04 南京理工大学 Magnetic fenton catalyst ferrospinel with Fenton iron containing sludge as source of iron and application
CN104928725B (en) * 2015-07-07 2017-07-28 哈尔滨工业大学 A kind of method for efficiently preparing dendritic α Fe absorbing materials

Also Published As

Publication number Publication date
CN105195150A (en) 2015-12-30

Similar Documents

Publication Publication Date Title
CN106807376B (en) Magnetic nano composite catalyst and preparation method and application thereof
CN107758836B (en) Method for removing refractory organic matters through in-situ coupling of microbial fuel cell and persulfate Fenton technology
CN105923628B (en) Method of wastewater treatment in a kind of graphene preparation technology
CN105439258A (en) Wastewater treatment method through generating H2O2 with in situ electricity to cooperate with O3 to oxidize
CN102874960A (en) Device and method for treating high-salinity and degradation-resistant organic industrial waste water by performing photoelectrical synchro coupling and catalytic oxidation on three-dimensional particles
CN105195150B (en) One kind prepares efficient Fe3O4/FeAl2O4The methods and applications of composite film class fenton catalyst
CN105016573B (en) Method for treatment of dye and PVA containing neutral wastewater by UV collaborated complexing/Fenton system
CN110357347B (en) Method for treating wastewater by persulfate advanced oxidation coupling biological sulfate reduction
CN104891733A (en) Treatment method of landfill leachate
CN104276734A (en) Electrochemical oxidation-denitriding biological aerated filter coupled reactor
CN104261518B (en) A kind of manganese charcoal catalyzed internal electrocatalysis filler and preparation method thereof and application
CN102295389B (en) Industrial waste water treating technology
CN110606539B (en) Method for treating organic wastewater by utilizing sludge resource
CN211471183U (en) Device for treating Fenton iron mud
CN107552052B (en) Treatment method of refractory organic wastewater
CN105297108B (en) A kind of utilization plasma electrolytic oxidation method prepares the methods and applications of ceramic film class fenton catalyst on Q235 carbon steels surface
CN107381712A (en) Difficult degradation, high-salt wastewater strengthen the photoelectricity catalytic ozonation method administered
CN104817139B (en) Upflow electro-Fenton fixed-bed reactor
CN110615501B (en) Method for treating landfill leachate
CN109293100A (en) A kind of processing method of heavy metal containing sewage
CN103570165A (en) Process for treating printing and dyeing wastewater through combination method
CN105568343B (en) The methods and applications of ferriferous oxide ceramic film class fenton catalyst are prepared in titanium alloy surface using plasma electrolytic oxidation method
CN102211832B (en) Method for treating cutting fluid wastewater by photocatalytic oxidation
CN1958462A (en) Method for preparing potassium ferrate by using waste liquid from acid washing steel
CN106345472A (en) Method for preparing high-efficient Fenton-like catalyst of sulphur modified iron-based composite material solid acid ceramic film layer and application

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant