CN108236846A - A kind of polymer compound film and preparation method thereof - Google Patents

A kind of polymer compound film and preparation method thereof Download PDF

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Publication number
CN108236846A
CN108236846A CN201611224678.3A CN201611224678A CN108236846A CN 108236846 A CN108236846 A CN 108236846A CN 201611224678 A CN201611224678 A CN 201611224678A CN 108236846 A CN108236846 A CN 108236846A
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CN
China
Prior art keywords
polymer compound
compound film
film
casting solution
cellulose acetate
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CN201611224678.3A
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Chinese (zh)
Inventor
唐剑锋
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Ningbo Urban Environment Observation And Research Station-Nueors Chinese Academy Of Sciences
Institute of Urban Environment of CAS
Original Assignee
Ningbo Urban Environment Observation And Research Station-Nueors Chinese Academy Of Sciences
Institute of Urban Environment of CAS
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Application filed by Ningbo Urban Environment Observation And Research Station-Nueors Chinese Academy Of Sciences, Institute of Urban Environment of CAS filed Critical Ningbo Urban Environment Observation And Research Station-Nueors Chinese Academy Of Sciences
Priority to CN201611224678.3A priority Critical patent/CN108236846A/en
Publication of CN108236846A publication Critical patent/CN108236846A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0079Manufacture of membranes comprising organic and inorganic components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12Composite membranes; Ultra-thin membranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/08Polysaccharides
    • B01D71/12Cellulose derivatives
    • B01D71/14Esters of organic acids
    • B01D71/16Cellulose acetate

Abstract

The present invention relates to environmental monitorings and pollution control technology field, and in particular to a kind of polymer compound film belongs to technology field of membrane materials.The material of polymer compound film of the present invention includes cellulose acetate, acetone, dioxane and magnesium perchlorate, by mass percentage, cellulose acetate 15 25%, acetone 65 80%, dioxane 8 20% and magnesium perchlorate 1 3%.Addition adsorbent is not needed in the polymer compound film of the present invention, pass through the rational proportion of cellulose acetate, solvent and magnesium perchlorate, directly rely on the adsorption capacity of cellulose acetate in itself, improve the structural effectiveness of film, the bioaccumulation efficiency of film is improved, obtains effectively being enriched with the polymer compound film of toxic organic pollutant.

Description

A kind of polymer compound film and preparation method thereof
Technical field
The present invention relates to environmental monitorings and pollution control technology field, and in particular to a kind of polymer compound film and its preparation Method belongs to technology field of membrane materials.
Background technology
With natural or artificial synthesized macromolecule membrane, using outside energy or chemical potential difference as motive force, to bi-component or The method that multi-component solute is detached with solvent, be classified, purified and is enriched with, is referred to as membrane separation process.Synthesis film can divide For organic (polymer) film and inoranic membrane, most important one membrane material is organic matter, i.e. polymer or macromolecular.It is so far Only, applied to most importantly cellulose esters mesentery in industry and laboratory, in addition synthetic polymeric membrane such as aliphatic and fragrance The research of polyamide film, fragrance-heterocyclic polymer film, ionic film, polyvinyl and co-polymer membrane, PS membrane etc. is near Also there is very big development over year.In recent years, with the introduction of technology and the acquirement of the successes achieved in research, the effective UF membrane of a batch Device gradually has been widely used in fields such as water process, industrial separation, wastewater treatment, laboratory separation.
Can only pointedly therefrom select some emphasis since toxic pollutant is numerous in environmental monitoring Pollutant is controlled.But the ratio that some toxic organic pollutants account for is less, but endanger it is but very big, have potential ecology and Health threat, such as most carcinogenic substances belong to organic matter.
Traditional sample concentration pretreatment technology mainly generally uses water using active enrichment process, such as environmental monitoring department Sample liquid/liquid extraction, XAD resin absorption, solid phase extraction, precipitation method etc..These methods are little for content in water body, have tired Product property, the big lipophilicity toxic organic pollutant accumulation ability of risk of toxicity is poor, far can not meet low detection limits, high enrichment The requirement of amount or there are a large amount of matrix interferences analysis measure the phenomenon that.
Invention content
The purpose of the present invention is be directed to the above-mentioned problems in the prior art, it is proposed that one kind can effectively be enriched with toxic The polymer compound film of organic pollution.
The above-mentioned purpose of the present invention is achieved through the following technical solutions:A kind of polymer compound film, polymer compound film Material includes cellulose acetate, acetone, dioxane and magnesium perchlorate, by mass percentage, cellulose acetate 15-25%, Acetone 65-80%, dioxane 8-20% and magnesium perchlorate 1-3%.
Containing neutral esters as adsorbent in polymer compound film of the prior art, as glycerol trioleate or/ With phosphoglyceride, iron/aluminium compound, and addition adsorbent is not needed in the polymer compound film of the present invention, it is fine to pass through acetic acid The rational proportion of dimension element, solvent and magnesium perchlorate directly by the adsorption capacity of cellulose acetate in itself, improves the structure effect of film Energy improves the bioaccumulation efficiency of film, obtains effectively being enriched with the polymer compound film of toxic organic pollutant.It is and if multiple in the present invention Cost can not only be increased by closing addition ester in film, can reduce the basic physicochemical property of film instead, and then reduce the structural effectiveness of film, drop The bioaccumulation efficiency of low film.
Preferably, the polymer compound film material is by mass percentage, cellulose acetate 18%, acetone 70%, Dioxane 10% and magnesium perchlorate 2%.
Preferably, the polymer compound film material is by mass percentage, cellulose acetate 24%, acetone 65%, Dioxane 8.8% and magnesium perchlorate 2.2%.
Preferably, the thickness of the polymer compound film is 45-70 μm, porosity 48-60%.If the thickness mistake of film It is low or excessive, then it can not achieve enrichment toxic organic pollutant.
Preferably, the water content of the polymer compound film is 55-62%, elongation at break 8-12.8%, stretch Intensity is 2.8-5.0kg.The mechanical effect of polymer compound film of the present invention is higher, and may be such that in practical application in the wild has not The advantage of destructible.
The preparation method of the polymer compound film of the present invention, includes the following steps:
S1, casting solution is prepared:By the mass percent weighing of above-mentioned polymer compound film raw material, the material weighed up is mixed and is matched Casting solution is made;
S2, casting solution is homogenized:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting film at 15-25 DEG C Liquid;
S3, film:Uniform casting solution using L-S phase inversion methods is film-made, evaporates 25-40s at 18-28 DEG C;
S4, coagulating bath:The film liquid layer prepared in step S3 is immersed in temperature to impregnate 6- in 20-30 DEG C of weak aqua ammonia 15min, secure satisfactory grades sub- composite membrane.
The polymer compound film of the present invention has the application of enrichment toxic organic pollutant.
Polymer compound film of the present invention does not need to addition adsorbent, passes through the conjunction of cellulose acetate, solvent and magnesium perchlorate Reason proportioning is on the one hand frame material using cellulose acetate family macromolecule directly by the adsorption capacity of cellulose acetate in itself Material, while using the absorption property that high molecular material has in itself to Adsorption of Organic, the nanoscale aperture on film causes The molecule of free solubilised state can enter, other are incorporated in cannot enter on particulate matter or Dissolved Organic Matter.The height of the present invention Molecular compound film material has very strong adsorption capacity to organic pollution, is because organic pollution easily enters quilt in film High molecular material is adsorbed.It, can be easily by the organic contamination of absorption using organic solvent such as n-hexane etc. by the similar principle that mixes Object elutes, and after taking out film, can measure organic pollution concentration in organic solvent.According to the exhausted of recycling organic pollution To the volume of content and raw water sample, the organic pollution concentration in raw water sample can obtain.
Compared with prior art, polymer compound film of the present invention is substantially increased by the proportioning of material to having in water body The adsorption capacity of malicious organic pollution.
Description of the drawings
Fig. 1 is the electron-microscope scanning figure of polymer compound film of the present invention.
Fig. 2 is absorption dynamics curve of the polymer compound film of the present invention to six kinds of organo-chlorine pesticides.
Specific embodiment
The following is specific embodiments of the present invention, and technical scheme of the present invention is further described, but the present invention is simultaneously It is not limited to these embodiments.
Embodiment 1
Prepare casting solution:By the mass percent weighing of polymer compound film raw material:Cellulose acetate 18%, acetone The material weighed up is hybridly prepared into casting solution by the 70%th, dioxane 10% and magnesium perchlorate 2%;
Homogenize casting solution:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 24 DEG C;
Film:Uniform casting solution using L-S phase inversion methods is film-made, film liquid is poured on scraper plate and scrapes 45-70 μ m-thicks Film liquid layer, evaporate 35s at 26 DEG C;
Coagulating bath:The related scraper plate of film liquid layer is immersed in temperature in 28 DEG C of weak aqua ammonias, to impregnate 8min together, it is washed to obtain Polymer compound film of the present invention.After tested, the thickness of the polymer compound film is 45-70 μm, porosity 60%, and water content is 61%, elongation at break 12.5%, tensile strength 4.8kg.
Embodiment 2
Prepare casting solution:By the mass percent weighing of polymer compound film raw material:Cellulose acetate 24%, acetone The material weighed up is hybridly prepared into casting solution by the 65%th, dioxane 8.8% and magnesium perchlorate 2.2%;
Homogenize casting solution:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 22 DEG C;
Film:Uniform casting solution using L-S phase inversion methods is film-made, film liquid is poured on scraper plate and scrapes 45-70 μ m-thicks Film liquid layer, evaporate 35s at 22 DEG C;
Coagulating bath:The related scraper plate of film liquid layer is immersed in temperature in 22 DEG C of weak aqua ammonias, to impregnate 12min together, it is washed Obtain polymer compound film of the present invention.After tested, the thickness of the polymer compound film is 45-70 μm, porosity 58%, water content It is 62%, elongation at break 11.8%, tensile strength 5.0kg.
Embodiment 3
Prepare casting solution:By the mass percent weighing of polymer compound film raw material:Cellulose acetate 15-25%, acetone The material weighed up is hybridly prepared into casting solution by 65-80%, dioxane 8-20% and magnesium perchlorate 1-3%;
Homogenize casting solution:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 20 DEG C;
Film:Uniform casting solution using L-S phase inversion methods is film-made, film liquid is poured on scraper plate and scrapes 45-70 μ m-thicks Film liquid layer, evaporate 30s at 20 DEG C;
Coagulating bath:The related scraper plate of film liquid layer is immersed in temperature in 25 DEG C of weak aqua ammonias, to impregnate 6min together, it is washed to obtain Polymer compound film of the present invention.After tested, the thickness of the polymer compound film is 45-70 μm, porosity 59%, and water content is 61%, elongation at break 12.8%, tensile strength 4.4kg.
Embodiment 4
Prepare casting solution:By the mass percent weighing of polymer compound film raw material:Cellulose acetate 15-25%, acetone The material weighed up is hybridly prepared into casting solution by 65-80%, dioxane 8-20% and magnesium perchlorate 1-3%;
Homogenize casting solution:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 18 DEG C;
Film:Uniform casting solution using L-S phase inversion methods is film-made, film liquid is poured on scraper plate and scrapes 45-70 μ m-thicks Film liquid layer, evaporate 25s at 28 DEG C;
Coagulating bath:The related scraper plate of film liquid layer is immersed in temperature in 20 DEG C of weak aqua ammonias, to impregnate 15min together, it is washed Obtain polymer compound film of the present invention.After tested, the thickness of the polymer compound film is 45-70 μm, porosity 52%, water content It is 56%, elongation at break 11.5%, tensile strength 3.5kg.
Embodiment 5
Prepare casting solution:By the mass percent weighing of polymer compound film raw material:Cellulose acetate 15-25%, acetone The material weighed up is hybridly prepared into casting solution by 65-80%, dioxane 8-20% and magnesium perchlorate 1-3%;
Homogenize casting solution:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 25 DEG C;
Film:Uniform casting solution using L-S phase inversion methods is film-made, film liquid is poured on scraper plate and scrapes 45-70 μ m-thicks Film liquid layer, evaporate 40s at 18 DEG C;
Coagulating bath:The related scraper plate of film liquid layer is immersed in temperature in 30 DEG C of weak aqua ammonias, to impregnate 6min together, it is washed to obtain Polymer compound film of the present invention.After tested, the thickness of the polymer compound film is 45-70 μm, porosity 54%, and water content is 57%, elongation at break 11.2%, tensile strength 3.8kg.
Application Example
Polymer compound film in embodiment 1-5 is used to be enriched with to the application of toxic organic pollutant.
Performance test
1st, polymer compound film obtained in embodiment 1 is subjected to electron-microscope scanning, as shown in Figure 1.It can be obtained from Fig. 1, this The compactness of invention polymer compound film is good, uniform surface.
2nd, a concentration of 500ng/L of indoor simulation organo-chlorine pesticide is tested, constant temperature extracting experiment is carried out on shaking table, is stood sudden and violent Dew 2,4,6,8,10h, takes out polymer compound film of the invention in 3 embodiments 1, and all enrichment experiments take every 1h to replace The mode of solution.Polymer compound film is dialysed for 24 hours through n-hexane, and analyzing organo-chlorine pesticide in n-hexane with GC-ECD contains Amount, the results are shown in Figure 2.
The capillary chromatographic column using two kinds of opposed polarities is tested, analysis condition is as follows:Carrier gas:High pure nitrogen;Detector (μ ECD) make-up gas:High pure nitrogen, make-up gas flow 30mL/min.Chromatographic column:SPB-1701 capillary chromatographic columns (30m × 0.25mm×0.25m).Post case uses temperature programming:Begin 60 DEG C of temperature, keeps 2min;Then the heating of the first rank is with 20 DEG C/min liters To 160 DEG C;Second-order heating rises to 260 DEG C, then keep 5min with 4 DEG C/min.Corresponding injector temperature:200℃;Injection port is adopted With constant current mode, flow velocity 0.9mL/min, linear velocity 27cm/s, Splitless injecting-Sample 1L.Corresponding detector temperature:280℃.
As can be seen from Figure 2, polymer compound film of the invention has very such as organo-chlorine pesticide of toxic organic pollutant in water body Strong adsorption capacity, it is every to endrin (endrin), drinox (aldrin), β-six six six, γ-six six six and Heptachlor epoxide Gram film distinguishes adsorbable 164.7ng, 101.5ng, 94.3ng, 71.3ng, 116.1ng per hour.
Specific embodiment described herein is only an example for the spirit of the invention.Technology belonging to the present invention is led The technical staff in domain can do various modifications or supplement to described specific embodiment or substitute in a similar way, but simultaneously The spirit or beyond the scope of the appended claims of the present invention is not deviated by.
It is skilled to this field although having been made a detailed description to the present invention and being cited some specific embodiments For technical staff, as long as it is obvious that can make various changes or correct without departing from the spirit and scope of the present invention.

Claims (7)

1. a kind of polymer compound film, which is characterized in that the material of polymer compound film includes cellulose acetate, acetone, dioxy Six rings and magnesium perchlorate, by mass percentage, cellulose acetate 15-25%, acetone 65-80%, dioxane 8-20% and Magnesium perchlorate 1-3%.
2. polymer compound film according to claim 1, which is characterized in that the polymer compound film material presses quality hundred Divide than meter, cellulose acetate 18%, acetone 70%, dioxane 10% and magnesium perchlorate 2%.
3. polymer compound film according to claim 1, which is characterized in that the polymer compound film material presses quality hundred Divide than meter, cellulose acetate 24%, acetone 65%, dioxane 8.8% and magnesium perchlorate 2.2%.
4. according to the polymer compound film described in claims 1 or 2 or 3, which is characterized in that the thickness of the polymer compound film It is 45-70 μm, porosity 48-60%.
5. according to the polymer compound film described in claims 1 or 2 or 3, which is characterized in that the polymer compound film it is aqueous It measures as 55-62%, elongation at break 8-12.8%, tensile strength 2.8-5.0kg.
6. a kind of preparation method of polymer compound film as described in claim 1, which is characterized in that the method is included such as Lower step:
S1, casting solution is prepared:By the mass percent weighing of above-mentioned polymer compound film raw material, the material weighed up is hybridly prepared into Casting solution;
S2, casting solution is homogenized:By casting solution, isothermal vibration to film liquid is completely dissolved to obtain uniform casting solution at 15-25 DEG C;
S3, film:Uniform casting solution using L-S phase inversion methods is film-made, evaporates 25-40s at 18-28 DEG C;
S4, coagulating bath:The film liquid layer prepared in step S3 is immersed in temperature to impregnate 6-15min in 20-30 DEG C of weak aqua ammonia, is obtained Polymer compound film.
7. polymer compound film as described in claim 1 has the application of enrichment toxic organic pollutant.
CN201611224678.3A 2016-12-27 2016-12-27 A kind of polymer compound film and preparation method thereof Pending CN108236846A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109265833A (en) * 2018-09-29 2019-01-25 桐城市强峰包装有限公司 It is a kind of for being injected intravenously the composite membrane outer cover of plastic containers insert port

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CN1395983A (en) * 2002-08-26 2003-02-12 中国科学院生态环境研究中心 Preparing process and application of composite biolipid/cellulose acetate membrane
CN1640531A (en) * 2004-01-13 2005-07-20 中国科学院生态环境研究中心 Acetyl cellulose/Fe-Al oxide composite membrane, and its preparing method and use
US9192894B2 (en) * 2012-06-11 2015-11-24 Enerage Inc. Electrochemical separation membrane and the manufacturing method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1395983A (en) * 2002-08-26 2003-02-12 中国科学院生态环境研究中心 Preparing process and application of composite biolipid/cellulose acetate membrane
CN1640531A (en) * 2004-01-13 2005-07-20 中国科学院生态环境研究中心 Acetyl cellulose/Fe-Al oxide composite membrane, and its preparing method and use
US9192894B2 (en) * 2012-06-11 2015-11-24 Enerage Inc. Electrochemical separation membrane and the manufacturing method thereof

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109265833A (en) * 2018-09-29 2019-01-25 桐城市强峰包装有限公司 It is a kind of for being injected intravenously the composite membrane outer cover of plastic containers insert port

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