CN106592214A - Preparation method of amphoteric ion exchange fiber - Google Patents

Preparation method of amphoteric ion exchange fiber Download PDF

Info

Publication number
CN106592214A
CN106592214A CN201611174634.4A CN201611174634A CN106592214A CN 106592214 A CN106592214 A CN 106592214A CN 201611174634 A CN201611174634 A CN 201611174634A CN 106592214 A CN106592214 A CN 106592214A
Authority
CN
China
Prior art keywords
ion exchange
preparation
amphoteric ion
exchange fibre
aminated
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.)
Pending
Application number
CN201611174634.4A
Other languages
Chinese (zh)
Inventor
朱小平
张勇
吴云
强金凤
陈婉芳
卢珊珊
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.)
Maanshan Zhongchuang Environmental Protection Technology Co Ltd
Original Assignee
Maanshan Zhongchuang Environmental Protection Technology Co Ltd
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 Maanshan Zhongchuang Environmental Protection Technology Co Ltd filed Critical Maanshan Zhongchuang Environmental Protection Technology Co Ltd
Priority to CN201611174634.4A priority Critical patent/CN106592214A/en
Publication of CN106592214A publication Critical patent/CN106592214A/en
Pending legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/322Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing nitrogen
    • D06M13/325Amines
    • D06M13/332Di- or polyamines
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/68Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with phosphorus or compounds thereof, e.g. with chlorophosphonic acid or salts thereof
    • D06M11/70Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with phosphorus or compounds thereof, e.g. with chlorophosphonic acid or salts thereof with oxides of phosphorus; with hypophosphorous, phosphorous or phosphoric acids or their salts
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/26Polymers or copolymers of unsaturated carboxylic acids or derivatives thereof
    • D06M2101/28Acrylonitrile; Methacrylonitrile

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

The invention discloses a preparation method of amphoteric ion exchange fiber. The method comprises steps as follows: an amination step: a proper amount of polyacrylonitrile fiber is taken and slowly added to a proper amount of organic alcohol, a proper quantity of amination reagents are added, the mixture is stirred at the specific temperature and subjected to a backflow reaction for certain time, a product is washed to be neutral with water, subjected to suction filtration and air-dried, and an aminated product is obtained; a phosphorylation step: the aminated product is taken and mixed with a proper amount of clear water and a proper quantity of aldehyde solvents, the mixture is stirred at the normal temperature, a phosphorylation agent is added, the mixture is stirred at the specific temperature and subjected to a backflow reaction for certain time, the solvents are removed after the reaction ends, a product is washed with water and hydrochloric acid sequentially and washed to be neutral finally, and the amphoteric ion exchange fiber is obtained. The specific fiber is taken as a framework, a high-selectivity adsorption material is formed through a two-step reaction of amination and phosphorylation, and the preparation method has the characteristics that the preparation method is simple, raw materials are cheap and easy to obtain, the adsorption capacity is high and the chelation capability is high.

Description

A kind of preparation method of amphoteric ion exchange fibre
Technical field
The invention belongs to the application of modified ion exchanging fiber material, more particularly to one kind is with weak acid and weak base two Plant characteristic and the preparation method with adsorption function and the new type amphoteric ion-exchange fibre of ion exchanging function.
Background technology
Ion-exchange fibre (IEF) is the feature adsorbing separation material of new generation after granular ion exchange resin Material.100 μm of the most < of diameter of ion-exchange fibre, or even 10 μm of <, with obvious kinetic advantage, it has exchange speed Degree is fast, effective ratio area is big, and fluid resistance is little, regeneration is easy and the series of advantages such as easy to use.It can be in a variety of forms Using, such as fiber, yarn, fabric, non-weaving cloth, thus suitable for the ion exchange process of various ways.Extensively use In prepare electronics pure water, medicinal water, biologic product, Industrial Waste Water Treatments, the absorption of poisonous and foul gas, catalyst carrier, The fields such as precious metal recovery, the collection of ocean rare metal, the separation and Extraction of medicine and biochemistry, develop rapidly now One of new and high technology, application prospect is very wide.
When ion-exchange fibre is with electrolyte solution contacts, the ion on fiber can make have selection with the ion in solution The exchange of property.Its point cation exchange fibre, anion-exchange fibre and amphoteric ion exchange fibre.Ion-exchange fibre can use In Adsorption of Heavy Metals and pigment, it is used as new sexual function macromolecular material, the chemistry with uniqueness and physical absorption and separation property Can, there is irreplaceable effect in some association areas, it is a kind of efficient absorption material grown up after activated carbon, Because its surface area is big, ion-exchange speed is fast, easily regeneration, applicability extensively becomes one of technical field of environment pollution control Study hotspot.
The structure of ion-exchange fibre is typically made up of matrix fiber and the cation exchange groups two parts being connected thereto, wherein Matrix fiber has polyvinyl alcohol, poly- phenolic aldehyde, polyamide, polyolefin, polyacrylonitrile, polyvinyl chloride-acrylonitrile copolymer, cellulose Deng ion-exchange group has strong acid, weak acid, highly basic, weak base, amphiprotic group etc..
Cellulose is the natural high molecular substance that nature is widely present, and is a kind of renewable resources.Plant is led to every year Photosynthesis is crossed, hundreds of millions tons of cellulose can be produced.In recent years, with oil, the decline of coal reserves, its importance is increasingly Significantly.Particularly since the eighties in last century, the growing interest and attention with various countries' environmental pollution forces people's handle Notice focuses on cellulose again, and this has on the renewable resource of biodegradability, environment compatibility.Although closing It is relatively more in the research of ion-exchange fibre, but great majority carry out graft modification based on synthetic fibers, and with fiber Amphoteric ion exchange fibre relevant report based on element is relatively fewer.
The content of the invention
The reality such as it is difficult to reclaim in order to the heavy metal water pollution emergency disposal technology that solves to happen suddenly at present is deficient, dispose material to ask Topic, the invention provides a kind of preparation method of new type amphoteric ion-exchange fibre;Polyacrylonitrile fibre be a class quantity it is abundant, Wide material sources, absorption raw material cheap and easy to get, containing abundant cellulose, and high mechanical strength, chemical synthesis can be passed through Means introduce one or more heavy metal ion (such as copper ion) on polyacrylonitrile fibre the network of very strong adsorption capacity Group (such as carboxyl and amino) is closed, the purpose for rapidly and efficiently removing removing heavy metals is reached, and preparation method is simple, can be good at Solve the above problems.
The purpose of the present invention can be achieved through the following technical solutions:
A kind of preparation method of amphoteric ion exchange fibre, the preparation method comprises the steps:
(1) it is aminated:Take appropriate polyacrylonitrile fibre to be slowly added in appropriate Organic Alcohol, and add quantitative amine Base reagent, stirring and back flow reaction special time under specified temp, products in water is washed to neutrality, and suction filtration dries, and obtains amine Base product;
(2) phosphorylation:Take aminated product and add appropriate clear water and aldehyde salt solvent, after stirring under normal temperature phosphoric acid is added Chemical drug agent, stirring and back flow reaction special time, remove solvent under specified temp after terminating, successively with water, hydrochloric acid wash products, Finally wash with water to neutrality, obtain product amphoteric ion exchange fibre.
Organic Alcohol described in step (1) is one or more in ethylene glycol, triethylene glycol, glycerine.
Aminated reagent described in step (1) is the one kind or many in ethylenediamine, diethylenetriamine, triethylene tetramine Kind.
Reflux time described in step (1) is 8~12h, and specified temp is 90~100 DEG C.
Polyacrylonitrile fibre, Organic Alcohol described in step (1) is 1 with aminated reagent quality ratio:20~35:4~8.
Phosphorylation medicament described in step (2) is phosphorous acid;Described aldehyde salt solvent is in formaldehyde, acetaldehyde and propionic aldehyde One or more.
Mixing time is 5~10min under normal temperature described in step (2);Described reflux time is 12~15h, Specified temp is 100~110 DEG C;Described concentration of hydrochloric acid is 1~5%.
Aminated product, phosphorylation medicament and aldehyde salt solvent mass ratio described in step (2) is 1:6~10:0.5~1.
Amphoteric ion exchange fibre described in step (2) to Adsorption of Cu 2+, Cr6+, Pb2+, adsorption rate is 95.74~ 98.14%.
Described adsorption step is:Take appropriate amphoteric ion exchange fibre Jing certain density HCl or NaOH immersion activation Afterwards, clean and load chromatographic column, heavy metal solution is adsorbed through ion-exchange fibre.
Beneficial effects of the present invention:
1) the modifying polyacrylonitrile method that the present invention is provided is simple, and easy to operate, performance is more stable, and saving is prepared into This;
2) ion-exchange fibre that the method makes has weak acid and a big characteristic of weak base two, the scope of Adsorption of Heavy Metals it is wide and Adsorption capacity is big, especially for the treatment effeciency height in heavy metal water pollution and with stronger stability, after process is made While waste liquid realizes innoxious, precious metal can be also reclaimed;
3) product mechanically and chemically good stability, using method is simple, further increases using the economy of adsorbent Property and the feature of environmental protection.
Specific embodiment
Technical scheme is further described below, but is not limited thereto, it is every to the technology of the present invention Scheme is modified or equivalent, without deviating from the spirit and scope of technical solution of the present invention, all should be covered in the present invention Protection domain in.
A kind of preparation method of amphoteric ion exchange fibre, the method be from polyacrylonitrile fibre as raw material, and Group activated monomer is complexed by chemical modification, the characteristic after fiber amido phosphoric acid simultaneously with weak acid and weak base fiber is made;
The present invention, by aminated and phosphorylation two-step reaction, forms high-selectivity adsorption material with special fiber as skeleton Material, with preparation method it is simple, raw material is cheap and easy to get, adsorption capacity is big, the characteristics of sequestering power is strong, and applied range, especially It is directed to the treatment effeciency height of heavy metal water pollution and with stronger stability, and the waste liquid after process is made is realized innoxious While, can also reclaim precious metal, and product mechanically and chemically good stability, using method is simple, further increases Using the economy and the feature of environmental protection of adsorbent.
Embodiment 1:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml ethylene glycol and is stirred, add 5ml Diethylenetriamine, back flow reaction 10h at 100 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 3g formalins, stirring at normal temperature 10min, Add 8g phosphorous acid, 110 DEG C of reaction 15h remove solvent after terminating, successively with water, 3% hydrochloric acid wash products, finally with clear It is washed to neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%NaOH immersion activation, is cleaned and is loaded chromatographic column, by 100mL Cu2+ Solution (the 100ppm solution being configured to by copper nitrate medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Cu of post water outlet2+Concentration is 2.13ppm, and adsorption rate is 97.87%.
Embodiment 2:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml ethylene glycol and is stirred, add 5ml Ethylenediamine, back flow reaction 10h at 100 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 3g acetaldehyde liquid, stirring at normal temperature 10min, Add 8g phosphorous acid, 110 DEG C of reaction 15h remove solvent after terminating, successively with water, 3% hydrochloric acid wash products, finally with clear It is washed to neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%HCl immersion activation, is cleaned and is loaded chromatographic column, by 100mL Cr6+It is molten Liquid (the 100ppm solution being configured to by potassium bichromate medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Cr of post water outlet6+Concentration is 3.05ppm, and adsorption rate is 96.95%.
Embodiment 3:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml glycerine and is stirred, add 5ml Ethylenediamine, back flow reaction 10h at 100 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 3g acetaldehyde liquid, stirring at normal temperature 10min, Add 8g phosphorous acid, 100 DEG C of reaction 15h remove solvent after terminating, successively with water, 3% hydrochloric acid wash products, finally with clear It is washed to neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%NaOH immersion activation, is cleaned and is loaded chromatographic column, by 100mL Cu2+ Solution (the 100ppm solution being configured to by copper nitrate medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Cu of post water outlet2+Concentration is 1.86ppm, and adsorption rate is 98.14%.
Embodiment 4:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml glycerine and is stirred, add 5ml Diethylenetriamine, back flow reaction 8h at 100 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 4g formalins, stirring at normal temperature 10min, Add 8g phosphorous acid, 110 DEG C of reaction 12h remove solvent after terminating, successively with water, 3% hydrochloric acid wash products, finally with clear It is washed to neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%HCl immersion activation, is cleaned and is loaded chromatographic column, by 100mL Cr6+It is molten Liquid (the 100ppm solution being configured to by potassium bichromate medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Cr of post water outlet6+Concentration is 2.45ppm, and adsorption rate is 97.55%.
Embodiment 5:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml ethylene glycol and is stirred, add 5ml Ethylenediamine, back flow reaction 10h at 100 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 3g acetaldehyde liquid, stirring at normal temperature 10min, Add 8g phosphorous acid, 100 DEG C of reaction 12h remove solvent after terminating, successively with water, 3% hydrochloric acid wash products, finally with clear It is washed to neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%NaOH immersion activation, is cleaned and is loaded chromatographic column, by 100mL Pb2+ Solution (the 100ppm solution being configured to by plumbi nitras medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Pb of post water outlet2+Concentration is 4.26ppm, and adsorption rate is 95.74%.
Embodiment 6:
(1) it is aminated:Polyacrylonitrile fibre 4g is taken, is slowly added in 100ml triethylene glycols and is stirred, add 8ml Triethylene tetramine, back flow reaction 12h at 90 DEG C, after suction filtration with clean water to it is close neutrality after dry;
(2) phosphorylation:Take it is aminated after intermediate product, be added to 100ml water, 3g propionic aldehyde liquid, stirring at normal temperature 5min, then Add 8g phosphorous acid, 100 DEG C of reaction 15h that solvent is removed after terminating, successively with water, 3% hydrochloric acid wash products finally use clear water It is washed till neutrality and obtains product;
(3) adsorption experiment:0.5g products are taken Jing after 2%NaOH immersion activation, is cleaned and is loaded chromatographic column, by 100mL Cr6+ Solution (the 100ppm solution being configured to by potassium bichromate medicament) adsorbs through ion-exchange fibre, speed 2ml/min.
Cross the Cr of post water outlet6+Concentration is 2.06ppm, and adsorption rate is 97.94%.
Above content is only citing made for the present invention and explanation, and affiliated those skilled in the art are to being retouched The specific embodiment stated is made various modifications or supplements or substituted using similar mode, without departing from invention or super More scope defined in the claims, all should belong to protection scope of the present invention.

Claims (10)

1. a kind of preparation method of amphoteric ion exchange fibre, it is characterised in that the preparation method comprises the steps:
(1) it is aminated:Take appropriate polyacrylonitrile fibre to be slowly added in appropriate Organic Alcohol, and add quantitative aminated Reagent, stirring and back flow reaction special time under specified temp, products in water is washed to neutrality, and suction filtration dries, and obtains aminated Product;
(2) phosphorylation:Take aminated product and add appropriate clear water and aldehyde salt solvent, after stirring under normal temperature phosphoric acid chemical drug is added Agent, stirring and back flow reaction special time, remove solvent, successively with water, hydrochloric acid wash products, finally under specified temp after terminating Wash with water to neutrality, obtain product amphoteric ion exchange fibre.
2. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (1) Described Organic Alcohol is one or more in ethylene glycol, triethylene glycol, glycerine.
3. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (1) Described aminated reagent is one or more in ethylenediamine, diethylenetriamine, triethylene tetramine.
4. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (1) Described reflux time is 8~12h, and specified temp is 90~100 DEG C.
5. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (1) Described polyacrylonitrile fibre, Organic Alcohol and aminated reagent quality ratio are 1:20~35:4~8.
6. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (2) Described phosphorylation medicament is phosphorous acid;Described aldehyde salt solvent is one or more in formaldehyde, acetaldehyde and propionic aldehyde.
7. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (2) Mixing time is 5~10min under described normal temperature;Described reflux time is 12~15h, and specified temp is 100~110 ℃;Described concentration of hydrochloric acid is 1~5%.
8. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (2) Described aminated product, phosphorylation medicament and aldehyde salt solvent mass ratio are 1:6~10:0.5~1.
9. the preparation method of a kind of amphoteric ion exchange fibre according to claim 1, it is characterised in that in step (2) Described amphoteric ion exchange fibre is to Adsorption of Cu2+、Cr6+、Pb2+, adsorption rate is 95.74~98.14%.
10. a kind of preparation method of amphoteric ion exchange fibre according to claim 9, it is characterised in that described suction Attached step is:Appropriate amphoteric ion exchange fibre is taken Jing after certain density HCl or NaOH immersion activation, is cleaned and is loaded chromatography Post, heavy metal solution is adsorbed through ion-exchange fibre.
CN201611174634.4A 2016-12-19 2016-12-19 Preparation method of amphoteric ion exchange fiber Pending CN106592214A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611174634.4A CN106592214A (en) 2016-12-19 2016-12-19 Preparation method of amphoteric ion exchange fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611174634.4A CN106592214A (en) 2016-12-19 2016-12-19 Preparation method of amphoteric ion exchange fiber

Publications (1)

Publication Number Publication Date
CN106592214A true CN106592214A (en) 2017-04-26

Family

ID=58601329

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611174634.4A Pending CN106592214A (en) 2016-12-19 2016-12-19 Preparation method of amphoteric ion exchange fiber

Country Status (1)

Country Link
CN (1) CN106592214A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114712893A (en) * 2022-03-26 2022-07-08 昆明理工大学 Method for recovering gold in thiosulfate solution
CN115770626A (en) * 2022-11-22 2023-03-10 河南科高辐射化工科技有限公司 Amphoteric ion exchange fiber and preparation method and application thereof
CN116655812A (en) * 2023-05-23 2023-08-29 苏州博睿特环保科技有限公司 Lead ion adsorption material in battery recovery feed liquid and preparation method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1172870A (en) * 1997-06-18 1998-02-11 中国科学院生态环境研究中心 Multi-dentate ion exchange chelating fibre and its synthetic method
CN1363426A (en) * 2001-01-11 2002-08-14 中国科学院生态环境研究中心 Ion exchange fibre and its synthesizing process
CN1563554A (en) * 2004-03-26 2005-01-12 钢铁研究总院 Method for preparing chelate fiber possessing reduction function
CN106000480A (en) * 2016-05-24 2016-10-12 马鞍山中创环保科技有限公司 Ion exchange fiber used for soil restoration, and preparation method thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1172870A (en) * 1997-06-18 1998-02-11 中国科学院生态环境研究中心 Multi-dentate ion exchange chelating fibre and its synthetic method
CN1363426A (en) * 2001-01-11 2002-08-14 中国科学院生态环境研究中心 Ion exchange fibre and its synthesizing process
CN1563554A (en) * 2004-03-26 2005-01-12 钢铁研究总院 Method for preparing chelate fiber possessing reduction function
CN106000480A (en) * 2016-05-24 2016-10-12 马鞍山中创环保科技有限公司 Ion exchange fiber used for soil restoration, and preparation method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114712893A (en) * 2022-03-26 2022-07-08 昆明理工大学 Method for recovering gold in thiosulfate solution
CN115770626A (en) * 2022-11-22 2023-03-10 河南科高辐射化工科技有限公司 Amphoteric ion exchange fiber and preparation method and application thereof
CN116655812A (en) * 2023-05-23 2023-08-29 苏州博睿特环保科技有限公司 Lead ion adsorption material in battery recovery feed liquid and preparation method thereof
CN116655812B (en) * 2023-05-23 2024-08-23 苏州博睿特环保科技有限公司 Lead ion adsorption material in battery recovery feed liquid and preparation method thereof

Similar Documents

Publication Publication Date Title
CN101357325B (en) Globular cellulose chelate sorbent containing amidoxime group and carboxy and preparation method thereof
CN102294231B (en) Molecularly imprinted fiber material and preparation method thereof
CN102274753B (en) Method for preparing bacterial cellulose loaded nanometer palladium catalyst
CN101701042B (en) Carboxymethyl chitosan thiourea resin and preparation method and application thereof
CN102188957A (en) Polyethyleneimine modified magnetic porous adsorbent and preparation method and application thereof
Jian et al. Preparation of polydopamine nanofibers mat as a recyclable and efficient adsorbent for simultaneous adsorption of multiple tetracyclines in water
CN108816204A (en) A kind of preparation method of copper ion imprinted crosslinked chitosan microballoon
CN106592214A (en) Preparation method of amphoteric ion exchange fiber
CN105214617A (en) Surface imprinted chitosan microball of high efficiency selected heavy metal ion and preparation method thereof
CN101898126A (en) Heavy metal ion adsorption carrier and preparation method thereof
CN107138135A (en) A kind of ion blotting nano-cellulose sorbing material and its preparation method and application
Huang et al. Efficient and selective capture of uranium by polyethyleneimine-modified chitosan composite microspheres from radioactive nuclear waste
CN102527087A (en) Method for absorbing and recycling heavy metals by using persimmon tannins
CN105061607A (en) Lithium-ion imprinted polymer and preparation method thereof
CN102580698A (en) Persimmon tannin adsorption material and preparation method thereof
CN105080504A (en) Fluoride ion surface imprinted polymer and processing method of fluorinated water
CN105268417A (en) Preparation method of composite membrane with functions of adsorbing and separating heavy metal ions
Huang et al. Rice straw derived adsorbent for fast and efficient phosphate elimination from aqueous solution
CN112452310B (en) Nitrogen-doped carbon adsorbent, preparation method thereof and application of nitrogen-doped carbon adsorbent to adsorption of organic dye
CN108772038B (en) Adsorbent for removing lead ions in water and preparation method and application thereof
CN101215366A (en) Tannin chelating resin and preparing method thereof
CN104130440A (en) Preparation method for iron ion imprinted polymer
CN107176649B (en) Method for separating 2-naphthalenesulfonic acid in wastewater by using iron-loaded copper macroporous resin
CN115138341A (en) Preparation method of cross-linked chitosan nano sponge adsorbent for efficiently removing anionic and cationic dyes
CN101797498B (en) Preparation method and application of chitosan absorbent

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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170426