CN106311125B - A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing - Google Patents

A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing Download PDF

Info

Publication number
CN106311125B
CN106311125B CN201610964133.XA CN201610964133A CN106311125B CN 106311125 B CN106311125 B CN 106311125B CN 201610964133 A CN201610964133 A CN 201610964133A CN 106311125 B CN106311125 B CN 106311125B
Authority
CN
China
Prior art keywords
polyvinyl alcohol
composite material
manganese oxide
water solution
absorption
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
CN201610964133.XA
Other languages
Chinese (zh)
Other versions
CN106311125A (en
Inventor
李梦娟
苏扬帆
林毅
葛明桥
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.)
Jiangnan University
Original Assignee
Jiangnan University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangnan University filed Critical Jiangnan University
Priority to CN201610964133.XA priority Critical patent/CN106311125B/en
Publication of CN106311125A publication Critical patent/CN106311125A/en
Application granted granted Critical
Publication of CN106311125B publication Critical patent/CN106311125B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B01J20/08Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
    • AHUMAN NECESSITIES
    • A62LIFE-SAVING; FIRE-FIGHTING
    • A62DCHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
    • A62D3/00Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/002Mixed oxides other than spinels, e.g. perovskite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/32Manganese, technetium or rhenium
    • B01J23/34Manganese
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/36Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
    • C02F2103/38Polymers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/10Photocatalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Toxicology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Health & Medical Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • General Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Business, Economics & Management (AREA)
  • Emergency Management (AREA)
  • Analytical Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Catalysts (AREA)

Abstract

The present invention relates to a kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing, belong to offal treatment and environmental protection technical field.It uses dipping calcination method to prepare MnxOy/γ‑Al2O3Composite material, and the absorption for polyvinyl alcohol and catalytic degradation processing.Mn prepared by the present inventionxOy/γ‑Al2O3Composite material can be realized simultaneously absorption and the catalytic degradation of polyvinyl alcohol, can be used for the processing of solid polyethylene alcohol and polyvinyl alcohol waste water the like waste, used MnxOy/γ‑Al2O3Composite material can be realized by washing, filtering and drying calcining to be regenerated, regenerated MnxOy/γ‑Al2O3Composites have many advantages, such as simple high adsorption, high catalytic property, reusable, method, simple operation, at low cost, efficient.

Description

A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing
Technical field
The present invention relates to a kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing, belong to discarded Object processing and environmental protection technical field.
Background technology
Polyvinyl alcohol (PVA) is a kind of to be widely used in the fields such as textile garment, printing and dyeing, papermaking, chemical industry, building Artificial synthesized high molecular material.Reagent and additive in polymerization, fabric containing polyvinyl alcohol and paper making pulp, building coating, coating, adhesive Generated waste water has certain viscosity to equal materials in the production and use process, and COD value is higher, and water is big, organic pollution Complicated component, it is unprocessed be discharged into nature after, problem of environmental pollution will be caused.
Manganese oxide is stronger one kind of catalytic capability in all metal oxides present in nature, they can conduct The electron acceptor of many redox reactions.γ-Al2O3With good mechanical performance and thermal stability, under the high temperature conditions Almost without loss, and there is very high absorption property, is commonly used to do the carrier of organic catalyst.With γ-Al2O3For carrier, Manganese oxide/alumina composite material that load manganese series oxides obtain in the above, meso-hole structure make it have larger ratio Surface area, excellent absorption property and preferable catalytic action, while there is higher surface-active and thermal stability, not only may be used Using as the residues of banned pesticides in good adsorbent collaboration microwave method removal agricultural chemicals waste water, such as glyphosate waste water can also be applied The CO and NO in mercury removal, vehicle exhaust in flue coal combustion exhaustxRemoving and O3 catalytic oxidation gas pollutant Etc..The present invention select manganese oxide/alumina composite material as containing polyvinyl alcohol waste water absorption and catalyst, can solve It is insufficient present in certainly existing polyvinyl alcohol Waste Disposal Technology.
Invention content
It is insufficient present in existing polyvinyl alcohol Waste Disposal Technology the purpose of the present invention is overcoming, a kind of oxidation is provided Application of the manganese/alumina composite material in terms of polyvinyl alcohol processing can not only synchronize the adsorption treatment for realizing polyvinyl alcohol And catalytic degradation processing, and with the features such as renewable, at low cost, efficient, easy to operate.
According to technical solution provided by the invention, a kind of manganese oxide/alumina composite material is in terms of polyvinyl alcohol processing Application, pass through MnxOy/γ-Al2O3Composite material carries out adsorption treatment to polyvinyl alcohol water solution or catalytic degradation is handled.
Adsorption treatment is as follows:The polyvinyl alcohol water solution for preparing 10~70g/L of 1L mass concentrations, uses quality A concentration of 0.15~0.30% dilute hydrochloric acid adjusts solution ph to 3~4.5, and 1~10g manganese oxide/alumina composite material is added MnxOy/γ-Al2O3, it is sufficiently stirred under the conditions of 25~80 DEG C 2~6 hours;Polyvinyl alcohol water solution is dense before and after absorption Degree is chosen supernatant and is tested using Finley methods.
Absorption and catalytic degradation polyvinyl alcohol water solution are as follows:Prepare the poly- of 10~70g/L of 1L mass concentrations Vinyl alcohol aqueous solution is that 0.15~0.30% dilute hydrochloric acid adjusts solution ph to 3~4.5 with mass concentration, 1~10g oxygen is added Change manganese/alumina composite material MnxOy/γ-Al2O3And 10~30% hydrogen peroxide of 50~300mL, in 25~80 DEG C of conditions Under be sufficiently stirred 2~6 hours, while realizing absorption and the catalytic degradation of polyvinyl alcohol;Polyvinyl alcohol water solution before and after the processing Concentration is chosen supernatant and is tested using Finley methods.
The manganese oxide/alumina composite material preparation method is as follows:Mn is prepared using dip-calcination methodxOy/γ- Al2O3Composite material;In the MnSO that 1L mass concentrations are 7.5g/L41~5g γ-Al are added in solution2O3Powder is sufficiently stirred 12 ~24 hours, solid particle is obtained by filtration, through being dried in vacuo 2~4 hours under the conditions of 90~110 DEG C, 0.08~0.09MPa, obtains To dry blocks of solid, after fully grinding, 300~650 DEG C are warming up to the heating rate of 10~20 DEG C/min, calcining 1~5 Hour, natural cooling obtains manganese oxide/alumina composite material MnxOy/γ-Al2O3Powder.
The MnxOy/γ-Al2O3Composite material can be used for the aqueous solution of adsorption treatment polyvinyl alcohol, to polyethylene Alcohol adsorption rate reaches as high as 13.6%;And used MnxOy/γ-Al2O3It is dry that composite material can pass through washing-filtering- The step of dry-calcining, realizes regeneration, through 5 regenerated MnxOy/γ-Al2O3Composite material is still reachable to polyvinyl alcohol adsorption rate To 13.1%.
The MnxOy/γ-Al2O3Composite material, can be used for simultaneously adsorb and catalytic degradation polyvinyl alcohol it is water-soluble Liquid reaches as high as 99.0% to the total handling rate of polyvinyl alcohol;And used MnxOy/γ-Al2O3Composite material can pass through The step of washing-filtering-drying-calcining, realizes regeneration, through 5 regenerated MnxOy/γ-Al2O3Composite material is to polyvinyl alcohol Total handling rate still can reach 98.8%.
Beneficial effects of the present invention:Mn prepared by the present inventionxOy/γ-Al2O3Composite material can be realized simultaneously polyethylene The absorption of alcohol and catalytic degradation can be used for the processing of solid polyethylene alcohol and polyvinyl alcohol waste water the like waste, have repeatable Using, method simple, simple operation, it is at low cost, efficient the advantages that.
Specific implementation mode
With reference to test example and specific implementation mode, the present invention is described in further detail.But this should not be understood It is only limitted to embodiment below for the range of the above-mentioned theme of the present invention, it is all that this is belonged to based on the technology that the content of present invention is realized The range of invention.
The absorption of 1 polyvinyl alcohol water solution of embodiment
(1)MnxOy/γ-Al2O3The preparation of composite material:The present invention prepares Mn using dip-calcination methodxOy/γ-Al2O3 Composite material, in the MnSO that 1L mass concentrations are 7.5g/L44g γ-Al are added in solution2O3Powder is sufficiently stirred 24 hours, mistake Filter obtains solid particle, is dried in vacuo 2 hours through 110 DEG C, 0.08MPa, obtains dry blocks of solid, after fully grinding, with The heating rate of 10 DEG C/min is warming up to 450 DEG C, calcines 2 hours, natural cooling obtains MnxOy/γ-Al2O3Composite wood feed powder End.
(2)MnxOy/γ-Al2O3Composite material adsorption treatment polyvinyl alcohol water solution:Prepare 1L mass concentrations 10g/L's Polyvinyl alcohol water solution adjusts solution ph to 3 with dilute hydrochloric acid, 1g Mn/ γ-Al is added2O3Composite material, under the conditions of 80 DEG C It is sufficiently stirred 6 hours, takes the supernatant of the front and back polyvinyl alcohol water solution of absorption respectively, it is front and back poly- using the test absorption of Finley methods Ethylene determining alcohol, is calculated adsorption rate.
Using the present embodiment absorption and catalytic degradation polyvinyl alcohol water solution, adsorption rate is up to 13.4%.
The absorption of 2 polyvinyl alcohol water solution of embodiment and catalytic degradation
Gained Mn is prepared using embodiment 1xOy/γ-Al2O3Composite material.
MnxOy/γ-Al2O3Composite material catalytic degradation polyvinyl alcohol water solution:Prepare the poly- second of 1L mass concentrations 10g/L Enol aqueous solution adjusts solution ph to 3 with dilute hydrochloric acid, 1g Mn/ γ-Al is added2O3The hydrogen peroxide of composite material and 120mL, It is sufficiently stirred under the conditions of 80 DEG C 4 hours, takes the supernatant of polyvinyl alcohol water solution before and after the processing respectively, surveyed using Finley methods Polyvinyl alcohol concentration before and after the processing is tried, total handling rate is calculated.
The total handling rate of the present embodiment is up to 99.0%.
Used MnxOy/γ-Al2O3Composite material can be realized by the step of washing-filtering-drying-calcining Regeneration, through 5 regenerated MnxOy/γ-Al2O3Composite material still can reach 98.6% to the total handling rate of polyvinyl alcohol.
The absorption of 3 polyvinyl alcohol water solution of embodiment
Gained Mn is prepared using embodiment 1xOy/γ-Al2O3Composite material.
MnxOy/γ-Al2O3Composite material adsorption treatment polyvinyl alcohol water solution:Prepare the poly- second of 1L mass concentrations 50g/L Enol aqueous solution adjusts solution ph to 3 with dilute hydrochloric acid, 2g Mn/ γ-Al is added2O3Composite material, under the conditions of 60 DEG C fully Stirring 6 hours takes the supernatant of the front and back polyvinyl alcohol water solution of absorption respectively, using the front and back polyethylene of Finley methods test absorption Adsorption rate is calculated in determining alcohol.
Using the present embodiment absorption and catalytic degradation polyvinyl alcohol water solution, adsorption rate is up to 12.9%.
The absorption of 4 polyvinyl alcohol water solution of embodiment and catalytic degradation
Gained Mn is prepared using embodiment 1xOy/γ-Al2O3Composite material.
MnxOy/γ-Al2O3Composite material catalytic degradation polyvinyl alcohol water solution:Prepare the poly- second of 1L mass concentrations 50g/L Enol aqueous solution adjusts solution ph to 3 with dilute hydrochloric acid, 2g Mn/ γ-Al is added2O3The hydrogen peroxide of composite material and 100mL, It is sufficiently stirred under the conditions of 60 DEG C 6 hours, takes the supernatant of polyvinyl alcohol water solution before and after the processing respectively, surveyed using Finley methods Polyvinyl alcohol concentration before and after the processing is tried, total handling rate is calculated.
Total handling rate of the present embodiment is up to 97.6.
Used MnxOy/γ-Al2O3Composite material can be realized by the step of washing-filtering-drying-calcining Regeneration, through 5 regenerated MnxOy/γ-Al2O3Composite material still can reach 97.3% to the total handling rate of polyvinyl alcohol.

Claims (1)

1. a kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing, it is characterized in that:Pass through MnxOy/γ- Al2O3Composite material carries out adsorption treatment to polyvinyl alcohol water solution or catalytic degradation is handled;
Adsorption treatment is as follows:The polyvinyl alcohol water solution for preparing 10 ~ 70g/L of 1L mass concentrations, uses mass concentration Solution ph is adjusted to 3 ~ 4.5 for 0.15 ~ 0.30% dilute hydrochloric acid, and 1 ~ 10g manganese oxide/alumina composite material Mn is addedxOy/γ- Al2O3, it is sufficiently stirred under the conditions of 25 ~ 80 DEG C 2 ~ 6 hours;The concentration of the front and back polyvinyl alcohol water solution of absorption chooses supernatant Liquid is tested using Finley methods;
Absorption and catalytic degradation polyvinyl alcohol water solution are as follows:Prepare the polyvinyl alcohol of 10 ~ 70g/L of 1L mass concentrations Aqueous solution is that 0.15 ~ 0.30% dilute hydrochloric acid adjusts solution ph to 3 ~ 4.5 with mass concentration, 1 ~ 10g manganese oxide/oxidation is added Aluminium composite material MnxOy/γ-Al2O3And 10 ~ 30% hydrogen peroxide of 50 ~ 300mL, it is sufficiently stirred 2 ~ 6 under the conditions of 25 ~ 80 DEG C Hour, while realizing absorption and the catalytic degradation of polyvinyl alcohol;The concentration of polyvinyl alcohol water solution chooses supernatant before and after the processing It is tested using Finley methods;
The manganese oxide/alumina composite material preparation method is as follows:Mn is prepared using dip-calcination methodxOy/ γ-Al2O3It is multiple Condensation material;In the MnSO that 1L mass concentrations are 7.5g/L41 ~ 5g γ-Al are added in solution2O3It is small to be sufficiently stirred 12 ~ 24 for powder When, solid particle is obtained by filtration, through being dried in vacuo 2 ~ 4 hours under the conditions of 90 ~ 110 DEG C, 0.08 ~ 0.09 MPa, obtains drying Blocks of solid, after fully grinding, be warming up to 300 ~ 650 DEG C with the heating rate of 10 ~ 20 DEG C/min, calcine 1 ~ 5 hour, it is natural It is cooling, obtain manganese oxide/alumina composite material MnxOy / γ-Al2O3Powder.
CN201610964133.XA 2016-11-04 2016-11-04 A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing Active CN106311125B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610964133.XA CN106311125B (en) 2016-11-04 2016-11-04 A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610964133.XA CN106311125B (en) 2016-11-04 2016-11-04 A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing

Publications (2)

Publication Number Publication Date
CN106311125A CN106311125A (en) 2017-01-11
CN106311125B true CN106311125B (en) 2018-09-21

Family

ID=57815957

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610964133.XA Active CN106311125B (en) 2016-11-04 2016-11-04 A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing

Country Status (1)

Country Link
CN (1) CN106311125B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115337924A (en) * 2022-08-31 2022-11-15 江南大学 Method for efficiently recovering PVA degradation catalyst

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102233259A (en) * 2010-05-04 2011-11-09 北京林业大学 Adsorbent for removing heavy metal from water and preparation method of adsorbent

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1812835A (en) * 2003-04-29 2006-08-02 约翰逊马西有限公司 Manganese ozone decomposition catalysts and process for its preparation

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102233259A (en) * 2010-05-04 2011-11-09 北京林业大学 Adsorbent for removing heavy metal from water and preparation method of adsorbent

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
Elemental mercury oxidation from flue gas by microwave catalytic oxidation over Mn/g-Al2O3;Z.S Wei et al.;《Journal of Industrial and Engineering Chemistry》;20141013;第24卷;第315-321页 *
催化氧化法处理聚乙烯醇废水;刘宝生等;《广东化工》;20101231;第37卷(第12期);第101-102,115页 *
聚乙烯醇在Al2O3、SiO2颗粒上的吸附及对Zeta电位的影响;韦园红 等;《华东理工大学学报》;20010228;第27卷(第1期);第99-102页 *

Also Published As

Publication number Publication date
CN106311125A (en) 2017-01-11

Similar Documents

Publication Publication Date Title
CN107694510B (en) Method for removing methylene blue in printing and dyeing wastewater by two-dimensional magnetic MXene
CN110961159B (en) Supported Fe-Co/ZIF-67 bimetallic catalyst and preparation method and application thereof
CN101732998B (en) Preparation method for cross-linking polyvinyl alcohol furfural nanofiltration membrane
CN105214612A (en) A kind of application of metal-organic framework functionalization material
CN107486045B (en) MoS2Polyelectrolyte hybrid nanofiltration membrane and preparation method thereof
CN102580746A (en) Activated carbon supported cobalt oxide catalyst and application of same in organic pollutant degradation
CN112028180B (en) Catalytic functional ceramic membrane and preparation method and application thereof
CN107051468A (en) Load the preparation method and application of poly-metal deoxide ozone catalytic oxidation catalyst
CN109867266B (en) Layered double-metal hydroxide, composite membrane, application of composite membrane and suction filtration device
CN104001371A (en) Method for recycling waste dust removal filter material
CN106824069B (en) For handling the preparation method of the rear-earth-doped iron Carbon Materials of arsenic-containing waste water
CN109092083A (en) A kind of preparation and application of ferroso-ferric oxide/regenerated cellulose magnetism forward osmosis membrane
CN114602552A (en) Photocatalytic composite membrane and preparation method and application thereof
Cao et al. Wool graft polyacrylamidoxime as the adsorbent for both cationic and anionic toxic ions from aqueous solutions
CN106311125B (en) A kind of application of manganese oxide/alumina composite material in terms of polyvinyl alcohol processing
CN112263920A (en) Preparation method and application of macromolecular dye nanofiltration membrane
CN105013500A (en) Heterogeneous Fenton catalyst for degrading azo dye wastewater as well as preparation method and application of heterogeneous Fenton catalyst
Selambakkannu et al. Modification of radiation grafted banana trunk fibers for adsorption of anionic dyes
CN108101147B (en) A kind of method of new catalytic material catalytic degradation wastewater from chemical industry
CN103041780A (en) Silica supported polyamine water treatment agent, application thereof and preparation method
CN113522038A (en) Preparation method and application of composite membrane for removing pollutants in water
CN109351329A (en) A kind of Zeolite modifying activated coke adsorbent material and its preparation method and application
CN106513021B (en) Layered hydroxide/BiOCl photocatalytic material and preparation method thereof
CN104587969A (en) Preparation method of carbon-base adsorbing material capable of selectively adsorbing copper ions
CN108745405A (en) Carbonitride/nitrogen mixes hollow mesoporous carbon/bismuth oxide ternary Z-type photochemical catalyst and preparation method thereof

Legal Events

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