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 PDFInfo
- 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
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
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.
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)
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)
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 |
-
2019
- 2019-04-02 CN CN201910261287.6A patent/CN109835897B/en active Active
Patent Citations (12)
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)
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 |