CN109835897A - Modified distillers ' grains matrix activated carbon of a kind of metal/hetero atom and preparation method thereof - Google Patents

Modified distillers ' grains matrix activated carbon of a kind of metal/hetero atom and preparation method thereof Download PDF

Info

Publication number
CN109835897A
CN109835897A CN201910261287.6A CN201910261287A CN109835897A CN 109835897 A CN109835897 A CN 109835897A CN 201910261287 A CN201910261287 A CN 201910261287A CN 109835897 A CN109835897 A CN 109835897A
Authority
CN
China
Prior art keywords
grains
distillers
preparation
hetero atom
activated carbon
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
CN201910261287.6A
Other languages
Chinese (zh)
Other versions
CN109835897B (en
Inventor
杨郭
董静文
邢波
刘兴勇
叶宇玲
莫莎
宋翔
宋博文
迟旭
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.)
Sichuan University of Science and Engineering
Original Assignee
Sichuan University of Science and Engineering
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 Sichuan University of Science and Engineering filed Critical Sichuan University of Science and Engineering
Priority to CN201910261287.6A priority Critical patent/CN109835897B/en
Publication of CN109835897A publication Critical patent/CN109835897A/en
Application granted granted Critical
Publication of CN109835897B publication Critical patent/CN109835897B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Carbon And Carbon Compounds (AREA)

Abstract

The invention discloses modified distillers ' grains matrix activated carbons of a kind of metal/hetero atom and preparation method thereof.Method includes the following steps: the distillers ' grains after drying are crushed to and the nitrogenous compound that mass fraction is 2.5%~20% are added after 50~200 mesh and the transistion metal compound that mass fraction is 2%~8% ground and mixed in mortar is uniform by (1), then by 1~3h of high temperature carbonization at its in a nitrogen atmosphere 600~900 DEG C, active carbon after charing is placed in 5~15h of immersion in acid, filtration washing drying;(2) by the active carbon after charing under activated gas atmosphere 700~900 DEG C of 2~5h of high-temperature activation, obtain the modified distillers ' grains matrix activated carbon of metal/hetero atom.The method of the present invention is easy, quick, easy to operate, is suitable for industrialized production, and it is a kind of effective catalyst that the modification vinasse matrix activated carbon of preparation, which has biggish specific surface area and biggish aperture, effectively catalysis oxidation can remove the organic pollutant in water removal.

Description

Modified distillers ' grains matrix activated carbon of a kind of metal/hetero atom and preparation method thereof
Technical field
The invention belongs to active carbon preparation technical fields, and in particular to a kind of modified distillers ' grains base activity of metal/hetero atom Charcoal and preparation method thereof.
Background technique
With the fast development of the every profession and trades such as chemical industry, pesticide, medicine, printing and dyeing and constantly pushing away for the cities and towns process of integration Into organic pollution problem is increasingly prominent in water body, has very important genotoxic potential effect to water resource and human health. And conventional sewage treatment process (activated sludge, elution, coagulation, film process, absorption etc.) be difficult to effectively remove water body Poisoning it is big, Bio-refractory has pollutant.Fenton oxidation technology is as a kind of common high-level oxidation technology, and can be degraded water with deep oxidation Organic pollutant in body, to remove removal organic polluter.But there are sludge quantities that big, catalyst is difficult to recycle for traditional Fenton technology The problems such as, restrict its application.Therefore, more and more researchs are dedicated to multiphase is made being urged using activated carbon supported transition metal Agent effectively realizes catalyst recycling problem and avoids the generation of sludge.
In having activated carbon supported transition-metal catalyst, the problem of active metal is easy dissolution is still remained, is lacked A method of preparing the activated carbon supported transition-metal catalyst of efficient stable.The present invention is adopted using vinasse as biomass resource With the mode and transition metal, nitrogenous compound high-temperature calcination of blending, metal/miscellaneous original is obtained in the way of gas activation later The modified distillers ' grains matrix activated carbon of son, the oxidative degradation for Organic Pollutants In Water.Utilize transition metal and nitrogenous precursor Between strong interaction, the stability of traditional catalyst both can be improved, while can also realize large waste vinasse Resource utilization, realization kill two birds with one stone.
Summary of the invention
Treatment of Organic Wastewater there are aiming at the problem that and distillers ' grains resource utilization necessity, the present invention provides one kind Modified distillers ' grains matrix activated carbon of metal/hetero atom and preparation method thereof, and dropped for the catalysis oxidation of Organic Pollutants In Water Solution, can effectively realize and recycle to vinasse.
The present invention prepares technical solution used by the modified distillers ' grains matrix activated carbon of metal/hetero atom:
A kind of preparation method of the modified distillers ' grains matrix activated carbon of metal/hetero atom, comprising the following steps:
(1) distillers ' grains after drying and crushing are mixed with nitrogen source and metallic compound, after grinding uniformly, 600~900 DEG C, in protective gas atmosphere carbonize 1~3h, be then placed in acid solution and impregnate again, filtering drying must carbonize after active carbon;
(2) active carbon after charing is placed in 2~5h of activation in 700~900 DEG C of activated gas, it is living obtains modified distillers ' grains base Property charcoal.
Further, the smashed partial size of distillers ' grains is 50~200 mesh in step (1).
Further, nitrogen source weight is the 2.5%~14.5% of total weight of the mixture.
Further, the nitrogen source in step (1) is dicyandiamide, melamine, ammonium chloride, urea etc..
Further, the weight of metallic compound is the 2%~8% of total weight of the mixture.
Further, metallic compound is iron chloride, ferric nitrate, nickel nitrate, cobalt nitrate, cobalt chloride etc. in step (1).
Further, the concentration of acid solution is 1~4mol/L in step (1).
Further, acid solution is hydrochloric acid or sulfuric acid.
Further, activated gas is carbon dioxide or water vapour in step (2).
The active carbon that the above method is prepared.
The invention has the benefit that
1, it is raw material that the present invention, which selects distillers ' grains, by distillers ' grains and nitrogen source (dicyandiamide, melamine, ammonium chloride, urea Deng) and metallic compound (iron chloride, nickel nitrate, cobalt nitrate, cobalt chloride etc.) mixed grinding after carbonize under high temperature, later in height Temperature is lower to use carbon dioxide or steam activation, obtains the modified distillers ' grains matrix activated carbon of metal/hetero atom, the method for the present invention letter Just, fast, it is easy to operate, it is easy to accomplish industrial applications
2, the modified distillers ' grains matrix activated carbon specific surface area of the metal being prepared/hetero atom is up to 240m2/ g or more, total hole Volume reaches 0.16cm3/ g or more, aperture integrated distribution can effectively be catalyzed persulfate oxidation in 3~4nm at normal temperatures and pressures The organic pollutants such as acid red, methyl orange in degradation water body, removal rate reaches 60% or more, and individually persulfate oxidation is organic Object removal rate is only 10% or so.
Detailed description of the invention
Fig. 1 is the active carbon phenogram that embodiment 1 is prepared;Wherein, Fig. 1 a is Pore Diameter Detection figure;Fig. 1 b is nitrogen suction Attached desorption curve figure;
Fig. 2 is the active carbon phenogram that embodiment 2 is prepared;Wherein, Fig. 2 a is Pore Diameter Detection figure;Fig. 2 b is nitrogen suction Attached desorption curve figure;
Fig. 3 is the active carbon phenogram that embodiment 3 is prepared;Wherein, Fig. 3 a is Pore Diameter Detection figure;Fig. 3 b is nitrogen Adsorption/desorption curve figure;
Fig. 4 is the activated carbon catalysis degradation quadracycline curve graph that embodiment 1 is prepared;
Fig. 5 is the activated carbon catalysis degradation methyl orange curve graph that embodiment 2 is prepared;
Fig. 6 is the activated carbon catalysis degradation of methylene blue curve graph that embodiment 3 is prepared.
Specific embodiment
A specific embodiment of the invention is described below, in order to facilitate understanding by those skilled in the art this hair It is bright, it should be apparent that the present invention is not limited to the ranges of specific embodiment, for those skilled in the art, As long as various change is in the spirit and scope of the present invention that the attached claims limit and determine, these variations are aobvious and easy See, all are using the innovation and creation of present inventive concept in the column of protection.
Embodiment 1
A kind of preparation method of the modified distillers ' grains matrix activated carbon of metal/hetero atom, comprising the following steps:
(1) distillers ' grains after drying are crushed to 50~100 mesh with pulverizer, then by 10g distillers ' grains powder, 0.3607g ferric nitrate and 1.45g melamine are uniformly mixed, and are fully ground in mortar, the mixture that then will be obtained It is placed in tube furnace, calcines 1h at 750 DEG C under nitrogen atmosphere, carbonized;
(2) calcined active carbon is taken out, after it is cooled to room temperature, is impregnated with the hydrochloric acid solution that concentration is 3mol/L 12h;
(3) it is filtered after impregnating, is washed with deionized to neutrality and is dried at 100 DEG C;
(4) active carbon after drying is placed in activation 2h in 800 DEG C of carbon dioxide atmosphere.
Specific surface area and pore structure property representation are carried out to the active carbon that is prepared, the result is shown in Figure 1 a and Fig. 1 b;Its In, Fig. 1 a is graph of pore diameter distribution, by Fig. 1 a it is found that the aperture integrated distribution for the active carbon being prepared is in 3~4nm, Fig. 1 b Nitrogen adsorption desorption isotherm, by Fig. 1 b it is found that in relative partial pressure P/P0To have an apparent hysteresis loop between 0.4~0.9, The doping carbon material for illustrating synthesis is meso-hole structure.It is 295.4m by its specific surface area known to analysis2/ g, total pore volume are 0.183cm3/ g, mesopore volume 0.145cm3/ g, the modification distillers ' grains matrix activated carbon illustrated have large specific surface area and Pore volume.
Embodiment 2
A kind of preparation method of the modified distillers ' grains matrix activated carbon of metal/hetero atom, comprising the following steps:
(1) distillers ' grains after drying are crushed to 100~200 mesh with pulverizer, then by 10g distillers ' grains powder, 0.3607g cobalt nitrate and 0.65g melamine are uniformly mixed, and are fully ground in mortar, the mixture that then will be obtained It is placed in tube furnace, calcines 1h at 750 DEG C under nitrogen atmosphere, carbonized;
(2) calcined active carbon is taken out, after it is cooled to room temperature, is impregnated with the hydrochloric acid solution that concentration is 3mol/L 12h;
(3) it is filtered after impregnating, is washed with deionized to neutrality and is dried at 100 DEG C;
(4) active carbon after drying is placed in activation 2h in 800 DEG C of carbon dioxide atmosphere.
Specific surface area and pore structure property representation are carried out to the active carbon being prepared, the result is shown in Fig. 2 a and Fig. 2 b;Its In, Fig. 2 a is graph of pore diameter distribution, by Fig. 2 a it is found that the aperture integrated distribution for the active carbon being prepared is in 3~4nm, Fig. 2 b Nitrogen adsorption desorption isotherm, by Fig. 2 b it is found that being to have an apparent hysteresis loop between 0.4~0.9 in relative partial pressure P/P0, The doping carbon material for illustrating synthesis is meso-hole structure.It is 248.5m by its specific surface area known to analysis2/ g, total pore volume are 0.169cm3/ g, mesopore volume 0.123cm3/ g, the modification distillers ' grains matrix activated carbon illustrated have large specific surface area and Pore volume.
Embodiment 3
A kind of preparation method of the modified distillers ' grains matrix activated carbon of metal/hetero atom, comprising the following steps:
(1) distillers ' grains after drying are crushed to 100~200 mesh with pulverizer, then by 10g distillers ' grains powder, 0.3607g ferric nitrate and 2g melamine are uniformly mixed, and are fully ground in mortar, are then placed in obtained mixture In tube furnace, 1h is calcined at 750 DEG C under nitrogen atmosphere, is carbonized;
(2) calcined active carbon is taken out, after it is cooled to room temperature, is impregnated with the hydrochloric acid solution that concentration is 3mol/L 12h;
(3) it is filtered after impregnating, is washed with deionized to neutrality and is dried at 100 DEG C;
(4) active carbon after drying is placed in activation 2h in 900 DEG C of steam atmosphere.
Specific surface area and pore structure property representation are carried out to the active carbon being prepared, the result is shown in Fig. 3 a and Fig. 3 b;Its In, Fig. 3 a is graph of pore diameter distribution, by Fig. 3 a it is found that the aperture integrated distribution for the active carbon being prepared is in 3~4nm, Fig. 3 b Nitrogen adsorption desorption isotherm, by Fig. 3 b it is found that being to have an apparent hysteresis loop between 0.4~0.9 in relative partial pressure P/P0, The doping carbon material for illustrating synthesis is meso-hole structure.It is 271.5m by its specific surface area known to analysis2/ g, total pore volume are 0.161cm3/ g, mesopore volume 0.135cm3/ g, the modification distillers ' grains matrix activated carbon illustrated have large specific surface area and Pore volume.
Embodiment 4
It is utilized respectively the active carbon that Examples 1 to 3 is prepared and carries out catalysis persulfate degradable organic pollutant experiment, Experimental result is shown in Fig. 4~6 for it.
As shown in Figure 4, it can be seen that for independent persulfate oxidation, shown after active carbon is added in embodiment 1 The efficiency for improving catalysis sodium peroxydisulfate degradation quadracycline is write, removal rate reaches 10% or more, and individually persulfate oxygen The removal rate of change is only 55%.Degradation experiment condition are as follows: 30 DEG C of temperature, sodium peroxydisulfate concentration are 1.2g/L, active carbon dosage is 0.2g/L, quadracycline initial concentration are 20mg/L.
As shown in Figure 5, it can be seen that for independent persulfate oxidation, shown after active carbon is added in embodiment 2 The efficiency for improving catalysis sodium peroxydisulfate degradation methyl orange is write, removal rate reaches 90% or more, and individually persulfate oxidation Removal rate is only 12%.Degradation experiment condition are as follows: 30 DEG C of temperature, sodium peroxydisulfate concentration are 1.2g/L, active carbon dosage is 0.2g/ L, methyl orange initial concentration is 100mg/L.
As shown in Figure 6, it can be seen that for independent persulfate oxidation, shown after active carbon is added in embodiment 3 The efficiency for improving catalysis sodium peroxydisulfate degradation of methylene blue is write, removal rate reaches 75% or more, and independent persulfate oxidation Removal rate be only 13%.Degradation experiment condition are as follows: 30 DEG C of temperature, sodium peroxydisulfate concentration are 1.2g/L, active carbon dosage is 0.2g/L, methylene blue initial concentration are 100mg/L.

Claims (10)

1. a kind of preparation method of the modified distillers ' grains matrix activated carbon of metal/hetero atom, which comprises the following steps:
(1) distillers ' grains and nitrogen source and iron after drying and crushing, cobalt or nickel metallization are closed object and mix, after grinding is uniform, 600~ 900 DEG C, 1~3h is carbonized in nitrogen protection gas atmosphere, is then placed in acid solution and impregnates again, filtering drying must carbonize after activity Charcoal;
(2) active carbon after charing is placed in 2~5h of activation in 700~900 DEG C of activated gas, obtains modified distillers ' grains base activity Charcoal.
2. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1/hetero atom, which is characterized in that The smashed partial size of distillers ' grains described in step (1) is 50~200 mesh.
3. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1/hetero atom, which is characterized in that The nitrogen source weight is the 2.5%~20% of total weight of the mixture.
4. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1 or 3/hetero atom, feature exist In nitrogen source described in step (1) is dicyandiamide, melamine, ammonium chloride, urea etc..
5. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1/hetero atom, which is characterized in that The weight of the metallic compound is the 2%~8% of total weight of the mixture.
6. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1 or 6/hetero atom, feature exist In metallic compound described in step (1) is iron chloride, ferric nitrate, nickel nitrate, cobalt nitrate, cobalt chloride.
7. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1/hetero atom, which is characterized in that The concentration of acid solution described in step (1) is 1~4mol/L.
8. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 7/hetero atom, which is characterized in that The acid solution is hydrochloric acid or sulfuric acid.
9. the preparation method of the modified distillers ' grains matrix activated carbon of metal according to claim 1/hetero atom, which is characterized in that Activated gas described in step (2) is carbon dioxide or water vapour.
10. the active carbon that any one of claim 1~9 the method is prepared.
CN201910261287.6A 2019-04-02 2019-04-02 Metal/heteroatom modified distiller's grain-based activated carbon and preparation method thereof Active CN109835897B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910261287.6A CN109835897B (en) 2019-04-02 2019-04-02 Metal/heteroatom modified distiller's grain-based activated carbon and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910261287.6A CN109835897B (en) 2019-04-02 2019-04-02 Metal/heteroatom modified distiller's grain-based activated carbon and preparation method thereof

Publications (2)

Publication Number Publication Date
CN109835897A true CN109835897A (en) 2019-06-04
CN109835897B CN109835897B (en) 2021-01-12

Family

ID=66886651

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910261287.6A Active CN109835897B (en) 2019-04-02 2019-04-02 Metal/heteroatom modified distiller's grain-based activated carbon and preparation method thereof

Country Status (1)

Country Link
CN (1) CN109835897B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627037A (en) * 2019-06-26 2019-12-31 陕西科技大学 Preparation method of nitrogen-doped biomass porous carbon nano electrode material
CN110655169A (en) * 2019-10-17 2020-01-07 威海中远造船科技有限公司 Sewage treatment method for enhancing Fenton reaction by adopting activated carbon
CN111389368A (en) * 2020-04-22 2020-07-10 徐州工程学院 Preparation method of excess sludge biochar and application of excess sludge biochar in removing tetracycline in water
CN114849760A (en) * 2022-06-08 2022-08-05 四川轻化工大学 Catalyst and preparation method and application thereof

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102718212A (en) * 2012-06-25 2012-10-10 安徽古井贡酒股份有限公司 Method using spent grains of white liquor for preparing active carbon
CN103964412A (en) * 2013-01-30 2014-08-06 北京化工大学 Preparation method of nitrogen-doped porous-structure carbon material
CN104475172A (en) * 2014-11-21 2015-04-01 东华大学 Preparation method and application of three-dimensional porous heteroatom-doped graphene
CN104843668A (en) * 2015-04-23 2015-08-19 北京理工大学 Method for preparing nitrogen doped porous carbon material by using biologic proteins
CN104891473A (en) * 2015-05-24 2015-09-09 西北大学 Preparation method of nitrogen-doped carbon material
CN105772708A (en) * 2016-03-10 2016-07-20 合肥工业大学 Method for using biomass waste for preparing nitrogen-doped carbon nanotube coated metal particle composite material
CN105819443A (en) * 2016-03-04 2016-08-03 四川大学 Active carbon prepared from waste plant-based biomass, and preparation method thereof
CN106629655A (en) * 2017-01-05 2017-05-10 中国科学院新疆理化技术研究所 Application and preparation method of biomass-based nitrogen-doped porous carbon
US20170333868A1 (en) * 2014-01-16 2017-11-23 Carbon Technology Holdings, LLC Carbon micro-plant
CN107555433A (en) * 2017-10-26 2018-01-09 电子科技大学 Anthracite nitrating activated carbon and preparation method thereof
CN107555434A (en) * 2017-09-05 2018-01-09 桂林电子科技大学 A kind of nitrating porous carbon materials based on agar and its preparation method and application
CN108975333A (en) * 2018-07-24 2018-12-11 启东创潞新材料有限公司 A kind of preparation method of modified vinasse matrix activated carbon

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102718212A (en) * 2012-06-25 2012-10-10 安徽古井贡酒股份有限公司 Method using spent grains of white liquor for preparing active carbon
CN103964412A (en) * 2013-01-30 2014-08-06 北京化工大学 Preparation method of nitrogen-doped porous-structure carbon material
US20170333868A1 (en) * 2014-01-16 2017-11-23 Carbon Technology Holdings, LLC Carbon micro-plant
CN104475172A (en) * 2014-11-21 2015-04-01 东华大学 Preparation method and application of three-dimensional porous heteroatom-doped graphene
CN104843668A (en) * 2015-04-23 2015-08-19 北京理工大学 Method for preparing nitrogen doped porous carbon material by using biologic proteins
CN104891473A (en) * 2015-05-24 2015-09-09 西北大学 Preparation method of nitrogen-doped carbon material
CN105819443A (en) * 2016-03-04 2016-08-03 四川大学 Active carbon prepared from waste plant-based biomass, and preparation method thereof
CN105772708A (en) * 2016-03-10 2016-07-20 合肥工业大学 Method for using biomass waste for preparing nitrogen-doped carbon nanotube coated metal particle composite material
CN106629655A (en) * 2017-01-05 2017-05-10 中国科学院新疆理化技术研究所 Application and preparation method of biomass-based nitrogen-doped porous carbon
CN107555434A (en) * 2017-09-05 2018-01-09 桂林电子科技大学 A kind of nitrating porous carbon materials based on agar and its preparation method and application
CN107555433A (en) * 2017-10-26 2018-01-09 电子科技大学 Anthracite nitrating activated carbon and preparation method thereof
CN108975333A (en) * 2018-07-24 2018-12-11 启东创潞新材料有限公司 A kind of preparation method of modified vinasse matrix activated carbon

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110627037A (en) * 2019-06-26 2019-12-31 陕西科技大学 Preparation method of nitrogen-doped biomass porous carbon nano electrode material
CN110627037B (en) * 2019-06-26 2021-07-06 陕西科技大学 Preparation method of nitrogen-doped biomass porous carbon nano electrode material
CN110655169A (en) * 2019-10-17 2020-01-07 威海中远造船科技有限公司 Sewage treatment method for enhancing Fenton reaction by adopting activated carbon
CN111389368A (en) * 2020-04-22 2020-07-10 徐州工程学院 Preparation method of excess sludge biochar and application of excess sludge biochar in removing tetracycline in water
CN114849760A (en) * 2022-06-08 2022-08-05 四川轻化工大学 Catalyst and preparation method and application thereof
CN114849760B (en) * 2022-06-08 2023-10-17 四川轻化工大学 Catalyst and preparation method and application thereof

Also Published As

Publication number Publication date
CN109835897B (en) 2021-01-12

Similar Documents

Publication Publication Date Title
CN109835897A (en) Modified distillers ' grains matrix activated carbon of a kind of metal/hetero atom and preparation method thereof
CN106076335B (en) A kind of preparation method and application of heterogeneous Fenton catalyst
CN106622227B (en) A kind of preparation method of the monatomic catalyst of indoor air purification
CN106944053A (en) A kind of sludge carbon base type Fenton catalyst and its preparation method and application
CN111744476B (en) Preparation method and application of red mud carbon-based catalyst
CN105036256A (en) Novel microelectrolysis filler, and preparation method and application thereof
CN109928391A (en) A kind of modified distillers ' grains matrix activated carbon and preparation method thereof
CN108380214B (en) A kind of preparation of modified meerschaum and method applied to wastewater treatment
CN105080540A (en) Wet oxidation catalyst and preparation method thereof
CN106391037B (en) One kind decomposing N for high-temperature catalytic2The preparation process of the catalyst of O
CN105478121B (en) A kind of preparation method for the titanium dioxide efficient visible light catalyst that di-iron trioxide is modified
CN111389435B (en) Iron-carbon micro-electrolysis-Fenton-like catalytic system and application
CN108607572A (en) Three-dimensional porous perovskite-cellulose carbon gel composite catalyst and its preparation and application
CN104096540A (en) Preparation method of adsorption and catalysis material for removing heavy metals and organic pollutants in municipal sludge
CN109482219A (en) Activate the CoFe of persulfate advanced treatment on coking wastewater2O4/ N doping sludge-based activated carbon catalyst and preparation method
CN110947418A (en) CTFs/GO composite material for adsorption and photocatalytic site separation, and preparation method and application thereof
Gao et al. Preparation of spiramycin fermentation residue derived biochar for effective adsorption of spiramycin from wastewater
CN106345486A (en) High-efficiency solid-phase ozone oxidation catalyst, and preparation method and application thereof
CN106000416A (en) Method for preparing ozone catalyst by using agricultural waste straw as raw material and application thereof
CN106064962A (en) Utilize mud and coal ash for manufacturing for the method for catalyst particle electrode and application
CN107930670A (en) Heterogeneous catalysis material that a kind of self-cradling type is homogeneously changed and its preparation method and application
CN109364924B (en) Magnetic nano ozone catalyst CoFe2O4And preparation method and application thereof
CN113441142B (en) Preparation method and application of oxygen vacancy-rich graphene-loaded porous nano ferroelectric oxide catalyst
CN107876053A (en) A kind of high intensity wastewater treatment catalyst and its preparation method and application
CN107128912A (en) A kind of preparation method of the Chinese medicine slag activated carbon of supported ion liquid

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