CN1715552A - Novel method for preparing ion exchange fiber by graft copolymerization - Google Patents
Novel method for preparing ion exchange fiber by graft copolymerization Download PDFInfo
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- CN1715552A CN1715552A CNA2004100483821A CN200410048382A CN1715552A CN 1715552 A CN1715552 A CN 1715552A CN A2004100483821 A CNA2004100483821 A CN A2004100483821A CN 200410048382 A CN200410048382 A CN 200410048382A CN 1715552 A CN1715552 A CN 1715552A
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- 239000000835 fiber Substances 0.000 title claims abstract description 80
- 238000000034 method Methods 0.000 title claims abstract description 37
- 238000005342 ion exchange Methods 0.000 title claims abstract description 22
- 238000007334 copolymerization reaction Methods 0.000 title abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 26
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 24
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 19
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 238000005406 washing Methods 0.000 claims description 14
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 12
- 238000002360 preparation method Methods 0.000 claims description 11
- 230000007704 transition Effects 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 10
- 238000005349 anion exchange Methods 0.000 claims description 9
- 238000005341 cation exchange Methods 0.000 claims description 9
- 238000007265 chloromethylation reaction Methods 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 8
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical group CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 claims description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 6
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 6
- -1 aliphatic tertiary amine Chemical class 0.000 claims description 6
- 150000001412 amines Chemical class 0.000 claims description 6
- 239000003957 anion exchange resin Substances 0.000 claims description 6
- 230000035484 reaction time Effects 0.000 claims description 6
- 239000004952 Polyamide Substances 0.000 claims description 5
- 239000003054 catalyst Substances 0.000 claims description 5
- 229920002647 polyamide Polymers 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- HRQGCQVOJVTVLU-UHFFFAOYSA-N bis(chloromethyl) ether Chemical compound ClCOCCl HRQGCQVOJVTVLU-UHFFFAOYSA-N 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 230000007935 neutral effect Effects 0.000 claims description 4
- 230000001376 precipitating effect Effects 0.000 claims description 4
- 230000008961 swelling Effects 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims description 2
- 238000011049 filling Methods 0.000 claims description 2
- 230000005251 gamma ray Effects 0.000 claims description 2
- 150000008282 halocarbons Chemical class 0.000 claims description 2
- 239000011261 inert gas Substances 0.000 claims description 2
- 239000003112 inhibitor Substances 0.000 claims description 2
- 239000012452 mother liquor Substances 0.000 claims description 2
- 238000006116 polymerization reaction Methods 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 238000000967 suction filtration Methods 0.000 claims description 2
- 238000006277 sulfonation reaction Methods 0.000 claims description 2
- 238000003828 vacuum filtration Methods 0.000 claims description 2
- 229920000098 polyolefin Polymers 0.000 claims 1
- 229920002554 vinyl polymer Polymers 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 239000012209 synthetic fiber Substances 0.000 abstract description 7
- 229920002994 synthetic fiber Polymers 0.000 abstract description 7
- 238000012986 modification Methods 0.000 abstract description 6
- 230000004048 modification Effects 0.000 abstract description 6
- 229920001519 homopolymer Polymers 0.000 abstract description 3
- 239000003431 cross linking reagent Substances 0.000 abstract description 2
- 230000008929 regeneration Effects 0.000 abstract description 2
- 238000011069 regeneration method Methods 0.000 abstract description 2
- 238000005272 metallurgy Methods 0.000 abstract 1
- 239000004743 Polypropylene Substances 0.000 description 12
- 229920001155 polypropylene Polymers 0.000 description 12
- 230000005855 radiation Effects 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002657 fibrous material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical class CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- 229920000433 Lyocell Polymers 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- KGVBVOYQIKFIGA-UHFFFAOYSA-N n,n-dimethylmethanamine Chemical compound CN(C)C.CN(C)C KGVBVOYQIKFIGA-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
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- Manufacture Of Macromolecular Shaped Articles (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
The present invention relates to co-irradiation grafting modification and functional reaction process of preparing ion exchange fiber on the basis of synthetic fiber. The co-irradiation grafting copolymerization reaction process is controlled in homopolymer production to raise grafting efficiency, and has proper cross-linking agent is added to raise the mechanical performance of the fiber, and the ion exchange fiber passing through the functional reactions has relatively high exchange capacity. The ion exchange fiber the present invention prepared has great exchange capacity, fast exchange speed, short regeneration time, high stability, simple production process, low cost and other advantages, and may be used widely in environment protection, food decolorizing, wet metallurgy, water treatment, resource recovering and other fields.
Description
Invention field
The present invention relates to a kind of new method that on the synthetic fiber basis, prepares ion-exchange fibre by mutual radiation graft modification and multiple reaction kinetic.
Background technology
Adopt fibre modification and reaction kinetic can prepare tencel with difference in functionality base.The preparation ion-exchange fibre mainly contains two kinds of methods: a class is unit or the polymer and unit or the polymer copolymerization or the blend that can become fibre that can be transformed into ion-exchange group with having, and is spun into fiber then; Another kind of is the inertial base of natural or synthetic fiber to be caused by chemistry or radiation causes and carries out modification, and for example CN1210763A discloses a kind of manufacture method and application thereof of ion-exchange fibre, and what this invention was used is the chemistry initiation.First kind preparation method's processing step complexity, production cost height, production cycle are long; In second class methods, adopt chemical graft to carry out modification, owing to add chemical initiator in producing, make the production process complexity, and easily produce and pollute.
Along with the civil nature of atomic energy technology is constantly popularized, adopt irradiation grafting to become a kind of both economical polymer modification method in recent years.At present mainly adopt the method for pre-irradiation to carry out graft copolymerization, but pre-irradiation to the having relatively high expectations of raw material, grafting simultaneously and irradiation needed for two steps finished.Adopting the mutual radiation technology to carry out graft copolymerization is directly to carry out the reaction that irradiation is finished after polymer and the monomer mixing, and it can avoid above shortcoming.But mutual radiation unavoidably can make monomer generation homopolymerization, influences graft effect, so the practical application on ion-exchange fibre does not also have aspect preparing to produce so far.
Purpose of the present invention just is to overcome above-mentioned preparation method's deficiency, and a kind of new method of utilizing synthetic fiber to prepare ion-exchange fibre by mutual radiation graft modification and reaction kinetic is provided.Utilize the inventive method in the mutual radiation graft copolymerization, can control the generation of homopolymers, improve grafting efficiency, and because the adding of suitable crosslinking agent, make the satisfactory mechanical property of fiber can guarantee behind the reaction kinetic that ion-exchange fibre has higher exchange capacity.
Summary of the invention
Preparation method of the present invention is on the synthetic fiber basis, prepares serial ion-exchange fibre by processing steps such as preliminary treatment, mutual radiation grafting and reaction kinetics.Ion-exchange fibre of the present invention is because through special treatment, not only percent grafting and exchange capacity height, and also its heat resistance, hot water resistance, corrosion resistance etc. all greatly improve.
The purpose of this invention is to provide a kind of new method for preparing functional ion exchange fiber, this method comprises processing steps such as preliminary treatment, mutual radiation grafting.
In specific embodiment, the method that the present invention prepares functional ion exchange fiber comprises the steps:
A) preliminary treatment: polyamide fiber was soaked 2-15 days vacuumize in swelling solution.Remove polymerization inhibitor in styrene and the divinylbenzene with the 5-10%NaOH solution washing or with anion exchange resin.
B) grafting liquid preparation: the styrene that will contain the 2-8% divinylbenzene joins in the alcohol, be mixed with the mixed liquor of the described styrene of 15-40% concentration in alcohol, pour this mixed liquor into container for example in the rustless steel container, is 1 with the polyamide fiber that obtains in the steps A according to described fiber and described mixed liquor: 10-30 (weight ratio, down together, unless otherwise mentioned) bath raio is put into container, charges into inert gas such as nitrogen after the sealing;
C) irradiation grafting: the container of above-mentioned filling fiber and grafting liquid is placed under room temperature
60Carry out irradiation in the Co gamma ray projector device, exposure time absorbed accumulated dose at 10-35Kgy at 7-18 hour;
D) washing: will be through step C) product that obtains takes out, and suction filtration is removed the residue grafting liquid, and with the precipitating agent washing, it is dry to dry the back, obtains modified fibre, is a kind of graft fibres.
Can be used for polyamide fiber of the present invention and can exemplify polyethylene (PE) and polypropylene (PP) fiber etc.Can select the fiber number of fiber as required.Generally speaking, the fiber number of fiber is between 1.0-8.4dtex, preferably between 1.0-4.0dtex, more preferably between the 1.2-2.0dtex.The fiber that adopts can be short silk or long filament.
Can be used for swelling solution of the present invention and can exemplify halogenated hydrocarbons for example dichloroethanes, carbon tetrachloride; Aromatic hydrocarbon is benzene,toluene,xylene etc. for example; Acetone.Be preferably acetone.
Can be used for steps A) anion exchange resin be conventional anion exchange resin, for example 717 anion exchange resin, D296 anion exchange resin.
Can be used for step B of the present invention) alcohol in the grafting liquid preparation is C
1-C
4-aliphatic alcohol mainly works to help free-radical generating and reduces homopolymers to generate, and for example can be methyl alcohol, ethanol, normal propyl alcohol, isopropyl alcohol, n-butanol etc.Be preferably methyl alcohol and ethanol.
At step D) washing step in the precipitating agent that adopted be the polymer precipitant of using always, for example can select methyl alcohol and ethanol for use.
The modified fibre that the inventive method is prepared (hereinafter being called graft fibres) can be made CATION or anion-exchange fibre through functionalization.
The present invention also provides a kind of method for preparing cation exchange fibre, and described method comprises carries out sulfonating reaction, processing etc. transition steps with the above-mentioned graft fibres that obtain.
In specific embodiment, the method that the present invention prepares cation exchange fibre comprises the steps:
E) sulfonating reaction: to through above-mentioned steps A) to D) add 80%～98% sulfuric acid in the graft fibres that obtain, the sulfonation bath raio of graft fibres and sulfuric acid is 1: 25-35, the reaction time is 5～10 hours; Wash with dilute sulfuric acid then, last water is washed till neutrality with product;
F) handle transition: the aqueous slkali with 15～25% is handled, and time transition is 3-30 minute;
G) washing: utilizing the water flushing, is neutral until pH, obtains cation exchange fibre.
In above-mentioned sulfonating reaction, can use the dilute sulfuric acid of variable concentrations to wash repeatedly successively with the dilute sulfuric acid washing, for example, the dilute sulfuric acid with 60-70%, 40-50% and 20-30% washs successively respectively.
In handling above-mentioned transition, can use different strong base solutions to handle, for example adopt NaOH, potassium hydroxide or ammonia spirit and composition thereof, preferably sodium hydroxide solution.
The washing amount is generally 1 part of cation exchange fibre: 90-120 part water.
The present invention also provides a kind of method for preparing anion-exchange fibre, and described method comprises carries out the above-mentioned graft fibres that obtain steps such as chloromethylation, aminating reaction, processing transition.
In specific embodiment, the method that the present invention prepares anion-exchange fibre comprises the steps:
H), chloromethylation: with through steps A) to D) graft fibres that obtain are raw material, with the anhydrous chloride is catalyst, the ratio of graft fibres and catalyst is 1: 0.5-2.5, the bath raio of graft fibres and chloromethyl ether is 1: 10-25, be preferably 1: 15-20,40-60 ℃ of reaction 6-40 hour, reaction finished the back with alcohol for example methyl alcohol or alcohol immersion 4-10 hour, vacuum filtration flush away mother liquor washes with water to neutrality;
I), aminating reaction: with the reaction of chloromethylation fiber and amine aqueous solution, the chloromethylation fiber is 1 with the reactive bath technique ratio of amine: 15-25 is preferably 1: 15-20, reaction temperature 25-40 ℃, the reaction time is 16-34 hour;
J), handle transition: behind aminating reaction, in the gained fiber, feed acid solution and react reaction time 5-30 minute;
K), washing: the water flushing is neutral until pH, obtains anion-exchange fibre.
Can be used as above-mentioned steps H) in catalyst be the chloride catalytic materials of using always, can exemplify for example zinc chloride, alchlor, butter of tin etc.
The amine that can be used for above-mentioned aminating reaction is aliphatic tertiary amine, as trimethylamine or triethylamine.
The acid solution of handling that can be used to make the transition can be any inorganic acid solution commonly used, for example dilute sulfuric acid or watery hydrochloric acid etc., and concentration is not particularly limited, and is the conventional concentration of described diluted acid, the dilute sulfuric acid of 10-70% for example, the watery hydrochloric acid of 10-20% concentration.
The washing amount is generally 1 part of anion-exchange fibre: 90-120 part water.
The inventive method is without particular limitation to the material performance that is adopted, and can adopt the conventional raw material of industry.For example in the preferred specific embodiments of the present invention, the performance of various raw materials can exemplify as follows:
| Raw material | Performance |
| Synthetic fiber | Fiber number is the basic fiber of polypropylene (PP) of 1.0～4.0dtex, comprises short silk and long filament |
| Styrene | Technical grade |
| Divinylbenzene | Concentration is greater than 48% |
| Methyl alcohol or ethanol | Technical grade |
| Trimethylamine | Technical grade |
| Chloromethyl ether | Concentration is greater than 42% |
| Trimethylamine | Trimethylamine aqueous solution concentration is greater than 30% |
| Sulfuric acid | Concentration is 80%～98% |
| NaOH | Technical grade |
| Hydrochloric acid | Technical grade |
The inventive method has that raw material is easy to get, preparation technology is simple, cost is low, with short production cycle, be convenient to suitability for industrialized production.
The ion-exchange fibre that is made by the inventive method has following advantage:
(1) have higher exchange capacity, exchange capacity is 3.0～3.5mmol/g;
(2) both had very strong ion-exchange capacity, and had the advantage of general fibre again, diameter is little, water flowing good, random layer should not take place, the exchange adsorption process has very significantly penetration power;
(3) mechanical strength is good, has good heat resistance, anti-chemistry and organic solvent-resistant;
(4) has superpower adsorption bleaching characteristic;
(5) reproduction speed is fast, and half an hour is promptly renewable, and does not influence exchange capacity.
Embodiment
Embodiment
Produce four batches of ion exchange fiber materials by preparation method of the present invention, produce required raw material and see Table 1, production process system sees Table 2, and the key property of the ion exchange fiber material that makes sees Table 3.Embodiment only is the embodiment of several the bests, can not play restriction effect of the present invention, and one of ordinary skill in the art can reasonably be revised its technical scheme with reference to embodiment, can obtain effect of the present invention equally.
Table 1 raw material
| Raw material | 1 | 2 | 3 | 4 |
| Synthetic fiber | The PP fiber, fiber number 1.5dtex | The PP fiber, fiber number 1.5dtex | The PP fiber, fiber number 1.5dtex | The PP fiber, fiber number 1.5dtex |
| Styrene | Consumption (PP fiber relatively) 25% | Consumption (PP fiber relatively) 25% | Consumption (PP fiber relatively) 20% | Consumption (PP fiber relatively) 20% |
| Divinylbenzene | Consumption (styrene relatively) 8% | Consumption (styrene relatively) 8% | Consumption (styrene relatively) 7% | Consumption (styrene relatively) 7% |
| The grafting liquid bath raio | 1∶15 | 1∶25 | 1∶15 | 1∶25 |
| Chloromethyl ether | Bath raio is about 1: 20 (weight) | Bath raio is about 1: 15 (weight) | / | / |
| Trimethylamine | Bath raio is about 1: 20 (weight) | Bath raio is about 1: 20 (weight) | / | / |
| Sulfuric acid | / | / | Concentration 95% | Concentration 98% |
| Running water | In right amount | In right amount | In right amount | In right amount |
Table 2 production process system
| Process system | 1 | 2 | 3 | 4 |
| Preliminary treatment (my god) | 5 | 5 | 5 | 5 |
| Irradiation (hour) | 7 | 14 | 7 | 14 |
| Sulfonating reaction (hour) | 8 | 10 | ||
| Chloromethylation (hour) | 8 | 8 | / | / |
| Aminating reaction (hour) | 18 | 18 | / | / |
| Handle transition (minute) | 25 | 30 | 25 | 25 |
The key property of table 3 ion exchange fiber material
| Performance | 1 | 2 | 3 | 4 |
| Product type | The strong base anion-exchange fibre | The strong base anion-exchange fibre | The strong-acid type cation exchange fiber | The strong-acid type cation exchange fiber |
| Moisture (%) | 65 | 64 | 67 | 64 |
| Complete exchange capacity (milliequivalent/gram) | 3.2 | 3.1 | 4.5 | 4.0 |
| Saltsplitting capacity (milliequivalent/gram) | 3.1 | 3.0 | 3.8 | 3.6 |
| Intensity (kilograms per centimeter 2) | 70 | 70 | 75 | 74 |
| Regeneration degree (%) | 85 | 76 | 90 | 87 |
Claims (10)
1, a kind of preparation method of functional ion exchange fiber comprises the steps:
A) preliminary treatment: polyamide fiber was soaked in swelling solution 2-15 days, and vacuumize is removed polymerization inhibitor in styrene and the divinylbenzene with the 5-10%NaOH solution washing or with anion exchange resin;
B) grafting liquid preparation: the styrene that will contain the 2-8% divinylbenzene joins in the alcohol, be mixed with the mixed liquor of the described styrene of 15-40% concentration in alcohol, this mixed liquor is poured in the container, with steps A) in the polyamide fiber that obtains be 1 according to described fiber and described mixed liquor: the 10-30 bath raio is put into container, charges into inert gas after the sealing;
C) irradiation grafting: the container of above-mentioned filling fiber and grafting liquid is placed under room temperature
60Carry out irradiation in the Co gamma ray projector device, exposure time was at 7-18 hour, and the irradiation accumulated dose is at 10-35Kgy;
D) washing: will be through step C) product that obtains takes out, and suction filtration is removed the residue grafting liquid, and with the precipitating agent washing, it is dry to dry the back.
2, according to the process of claim 1 wherein steps A) described polyolefin is polyvinyl fiber or polypropylene-base fiber, fiber number is 1.0-8.4dtex.
3, according to the method for claim 1 or 2, wherein, steps A) described swelling solution is halogenated hydrocarbons, aromatic hydrocarbon or acetone.
4, the alcohol according to arbitrary method of claim 1-3, wherein, step B) is C
1-C
4-aliphatic alcohol.
5, the precipitating agent according to arbitrary method of claim 1-4, wherein, step D) is methyl alcohol or ethanol.
6, a kind of method for preparing cation exchange fibre, this method comprise arbitrary step and the following step of claim 1-5:
E) sulfonating reaction: to through above-mentioned steps A) to D) add 80%～98% sulfuric acid in the graft fibres that obtain, the sulfonation bath raio of graft fibres and sulfuric acid is 1: 25-35, the reaction time is 5～10 hours; Wash with dilute sulfuric acid then, last water is washed till neutrality with product;
F) handle transition: the aqueous slkali with 15～25% is handled, and time transition is 3-30 minute;
G) washing: utilizing the water flushing, is neutral until pH, obtains cation exchange fibre.
7, according to the method for claim 6, wherein, aqueous slkali is selected from potassium hydroxide, NaOH or ammonia spirit.
8, a kind of method for preparing anion-exchange fibre, this method comprise arbitrary step and the following processing step of claim 1-5:
H), chloromethylation: with through steps A) to D) graft fibres that obtain are raw material, with the anhydrous chloride is catalyst, the ratio of graft fibres and catalyst is 1: 0.5-2.5, the bath raio of graft fibres and chloromethyl ether is 1: 10-25, reaction is 6-40 hour in the time of 40-60 ℃, soaked 4-10 hour with alcohol after reaction finishes, vacuum filtration flush away mother liquor washes with water to neutrality;
I), aminating reaction: with the reaction of chloromethylation fiber and amine aqueous solution, the chloromethylation fiber is 1 with the reactive bath technique ratio of amine: 15-25, reaction temperature 25-40 ℃, the reaction time is 16-34 hour;
J), handle transition: behind aminating reaction, in the gained fiber, feed acid solution and react reaction time 5-30 minute;
K), washing: the water flushing is neutral until pH, obtains anion-exchange fibre.
9, the amine method according to Claim 8, wherein, step I) is aliphatic tertiary amine.
10, according to the method for claim 9, wherein said aliphatic tertiary amine is trimethylamine or triethylamine.
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|---|---|---|---|
| CNB2004100483821A CN100439591C (en) | 2004-06-30 | 2004-06-30 | Novel method for preparing ion exchange fiber by graft copolymerization |
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|---|---|---|---|
| CNB2004100483821A CN100439591C (en) | 2004-06-30 | 2004-06-30 | Novel method for preparing ion exchange fiber by graft copolymerization |
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| CN100439591C CN100439591C (en) | 2008-12-03 |
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Cited By (7)
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| CN102051811A (en) * | 2010-11-23 | 2011-05-11 | 郑州大学 | Method for preparing polyphenylene sulfide-based strong basic ion exchange fibers |
| CN102492781A (en) * | 2011-12-01 | 2012-06-13 | 桂林正翰科技开发有限责任公司 | Syrup decolorization method |
| CN102758351A (en) * | 2012-07-11 | 2012-10-31 | 江苏玉人服装有限公司 | Manufacturing method for strong-acid ion exchange fiber |
| CN104195826A (en) * | 2014-08-13 | 2014-12-10 | 广西桂林正翰辐照中心有限责任公司 | Preparation method of functional ion exchange fiber |
| CN108084302A (en) * | 2016-11-22 | 2018-05-29 | 中国科学院大连化学物理研究所 | A kind of preparation method of alkalescence anion-exchange resin |
| CN110485198A (en) * | 2018-05-15 | 2019-11-22 | 上海东升新材料有限公司 | Radiation modification cellulose emulsifier and the AKD lotion prepared using the emulsifier |
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| CN106012491A (en) * | 2016-06-27 | 2016-10-12 | 安徽金联地矿科技有限公司 | Method for preparing efficient modified ion exchange fiber |
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| SU1162821A1 (en) * | 1983-01-18 | 1985-06-23 | Институт физико-органической химии АН БССР | Method of obtaining carboxyl cationite |
| SU1155287A1 (en) * | 1983-12-01 | 1985-05-15 | Институт физико-органической химии АН БССР | Method of cleaning gases from sulfur dioxide |
| SU1684291A1 (en) * | 1989-04-24 | 1991-10-15 | Научно-исследовательский институт физико-химических проблем Белорусского государственного университета им.В.И.Ленина | Method of producing ion-exchange graft-copolymers |
| CN1112257C (en) * | 1998-07-30 | 2003-06-25 | 中国石油化工总公司 | Method for producing ion exchanging fiber and its use |
| JP2000262894A (en) * | 1999-03-19 | 2000-09-26 | Mitsubishi Chemicals Corp | Fibrous synthetic adsorbent and production thereof |
| AU5629600A (en) * | 1999-06-23 | 2001-01-09 | Warner-Lambert Company | Solid-supported initiators and functional polymers for use in organic synthesis and combinatorial chemistry |
| CN1128020C (en) * | 2001-09-17 | 2003-11-19 | 桂林正翰科技开发有限责任公司 | Method of preparing functional ion exchange fiber |
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| CN108084302A (en) * | 2016-11-22 | 2018-05-29 | 中国科学院大连化学物理研究所 | A kind of preparation method of alkalescence anion-exchange resin |
| CN110485198A (en) * | 2018-05-15 | 2019-11-22 | 上海东升新材料有限公司 | Radiation modification cellulose emulsifier and the AKD lotion prepared using the emulsifier |
| CN110485198B (en) * | 2018-05-15 | 2022-07-01 | 上海东升新材料有限公司 | Radiation modified cellulose emulsifier and AKD emulsion prepared by adopting same |
| CN117672582A (en) * | 2023-08-16 | 2024-03-08 | 西南科技大学 | Nuclear medicine radioactive wastewater deep purification treatment system and application method |
| CN117672582B (en) * | 2023-08-16 | 2024-05-17 | 西南科技大学 | Nuclear medicine radioactive wastewater deep purification treatment system and application method |
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