CN103936906B - A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate - Google Patents
A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate Download PDFInfo
- Publication number
- CN103936906B CN103936906B CN201410195268.5A CN201410195268A CN103936906B CN 103936906 B CN103936906 B CN 103936906B CN 201410195268 A CN201410195268 A CN 201410195268A CN 103936906 B CN103936906 B CN 103936906B
- Authority
- CN
- China
- Prior art keywords
- polyfluoroalkoxy
- poly
- acid
- fluoropolymer
- salt
- 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
Links
Abstract
The invention discloses a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, being obtained the fluoropolymer without perfluoro caprylic acid or perfluorooctane sulfonate in the case of poly-polyfluoroalkoxy ether acid is as emulsifying agent after liquid phase polymerization by one or more fluorinated monomers, described poly-polyfluoroalkoxy ether acid is the poly-polyfluoroalkoxy ether acid emulsifying agent of end group band halogen or hydrogen.Its technical scheme has related generally to the improvement in terms of three below: (1) selects poly-polyfluoroalkoxy ether acid and salt replacement PFOA/ PFOS thereof as fluorine-containing emulsifier, can be effectively applied to the aqueous emulsion polymerization of fluorinated monomer；(2) fluoropolymer prepared is without perfluoro caprylic acid or perfluorooctane sulfonate, meets environmental requirement；(3) meet cost accounting, do not increasing manufacturing facilities and the output per single reactor of equipment can be greatly improved in the case of personnel, simultaneously, moreover it is possible to improving the production target such as polymerization time, polymerization yield rate.
Description
Technical field
The present invention relates to the synthesis field of fluoropolymer, specifically, be a kind of without perfluoro caprylic acid or the pungent sulphur of perfluor
The fluoropolymer of acid.
Background technology
Fluoropolymer is the general name of the alkanes polymer that part hydrogen atom is replaced by fluorine atoms, and is also that a class is more special
Different macromolecular material, can be carried out polyreaction under certain condition and form by one or more fluorochemical monomers, high in its structure
The fluorine carbon bond of bond energy and the fluorine atom shielding action to strand so that it is there is a series of excellent characteristic, such as: excellent is resistance to
Chemical corrosivity, dielectric properties, against weather, non-stick, excellent frictional behaviour etc., certainly, due to the performance of its excellence, contain
It is indispensable that fluoropolymer has become multiple fields such as modern science and technology, national defence, electric, chemical industry, medicine and mechanical industry
One of material.
In the polymerization process of fluoropolymer, it usually needs add a certain amount of fluorine-containing emulsifier, in the field, I
Know that perfluorooctane sulfonate (PFOS) or its salt can be but the most beautiful as far back as calendar year 2001 as the fluorine-containing emulsifier in polyreaction
Environmental Protection Administration of state (EPA) proposes disabling decree, to this end, 3M company have developed perfluoro butyl sulfonic acid (PFBS) C the most specially4F9SO3H
The fluorocarbon chain replacing PFOS, PFBS is short, without obvious persistency biological accumulation, can discharge body with human metabolism in the short time
Outward, and it mediates thing nonhazardous, and its commodity prove safeguard functions and environmentally friendly through a large amount of tests, by EPA and the world its
His environmental protection mechanism is ratified.But showing according to latest data, existing the most frequently used fluorine-containing emulsifier is perfluoro caprylic acid and salt thereof, with it
Reaching its maturity of market, its safety and environmental-protecting performance also suffered query, 2006, EPA promulgated restriction decree, and this decree is recognized
Generate the chemicals of PFOA for perfluorooctanoic acid (PFOA) and some decomposable asymmetric choice net due to stability of its height and to be difficult to degrade
Characteristic, it is most likely that the major diseases such as cause cancer, to this end, both at home and abroad Ge great manufacturing enterprise is just devoted to study a kind of new
Compound, to substitute this kind of fluorine-containing emulsifier with high stability feature, improves fluoropolymer and uses process in each field
In safety coefficient, particularly at medicine etc. with the industry field of direct body contact, its security performance is even more important.
Disclosed as having that fluorine-containing emulsifier in polymerization process uses: PFPE (CN101218264B), ring-type
Fluorochemical (CN102089335A), replacement perfluoro caprylic acid and the fluorine-containing emulsifier (CN101745338A) of its esters, formula
XCF2CF2(O)MCF2CF2OCF2The fluorine-containing emulsifier (CN101287766, CN101291987) that COOA represents, above-mentioned fluorine-containing emulsifying
Agent the most alternative PFOA/ PFOS is for the emulsion polymerization of fluorinated monomer, and the water-based emulsion of its fluoropolymer is the most not
Show fluorine-containing octanoic acid or its salt adverse effect.
From above-mentioned patent documentation disclosure we it will also be appreciated that existing disclosed fluorine-containing emulsifier all has
Effect, although solve the Toxicological Characterization of fluorine-containing emulsifier, but be all not directed to productivity and the granularity of fluoropolymer etc. and produce
Product feature, as a example by above-mentioned patent of invention CN101218264B, in this patent documentation, give polymerization time, particle mean size,
The particle specific gravity of SSG(fluoropolymer), the correction data of solids content, in addition to polymerization time, remainder data is all without obvious ripple
Dynamic, although it follows that the existing fluorine-containing emulsifier related to without perfluoro caprylic acid solve PFOA/ PFOS high stability and
The harm that human body may be caused by difficult degradation characteristic, but whole production efficiency is not made any substantial improvement, meanwhile,
The fluorine-containing emulsifier related to due to foregoing invention patent CN101218264B is PFPE, it is known that PFPE is
Being made up of the such ether chain of CF2 O CF 2, in its molecule, all of H atom is all substituted by F atom, raw from industry
For product, large-scale production can not be realized, it is necessary to adding institute's band halogen on end group in preparation process is not the list of F
Body, as chain-transferring agent, could realize industrialized production, and production technology is the most numerous and diverse, and based on existing market competition
Being growing more intense, we must find a kind of new fluorine-containing emulsifier, the use of the most alternative PFOA/ PFOS, also may be used meanwhile
From properties of product, it is thus achieved that economic benefit long-term, effective.
Summary of the invention
It is an object of the invention to provide a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, due to its liquid
The emulsifying agent used in phase-polymerization system is poly-polyfluoroalkoxy ether acid, does not the most produce stable carbon 8, is also not belonging to carbon
The atom straight chain perfluorocarbon saturated hydrocarbons homologue more than 8, simultaneously as the introducing of ehter bond, more makes its degradation property increase, is difficult to
Be enriched with in the environment, therefore, this fluoropolymer do not contain perfluoro caprylic acid or perfluorooctane sulfonate, do not exist bioconcentration and other
Toxicity, is suitably widely popularized use.
The present invention is achieved through the following technical solutions: a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate,
By one or more fluorinated monomers in the case of poly-polyfluoroalkoxy ether acid (or its salt) is as emulsifying agent after liquid phase polymerization
Obtaining the fluoropolymer without perfluoro caprylic acid or perfluorooctane sulfonate, described poly-polyfluoroalkoxy ether acid is selected from following one
Or several combinations:
Meet the poly-polyfluoroalkoxy ether acid of lower formula I:
(I),
Meet the poly-polyfluoroalkoxy ether acid of lower formula II:
(II),
Meet the poly-polyfluoroalkoxy ether acid of lower formula III:
(III),
Wherein:
T:、、、、；
X:H, Cl, Br, I；
R:H, Cl, Br, I；
Y:SO3H and salt, COOH and salt thereof, CH2CH2COOH and salt, CH2CH2SO3H and salt thereof,
COOCH2CH2COOH and salt, COOCH2CH2SO3H and salt thereof,And salt；And salt；
The value of n is: 0～4
The value of m is: 1～20
The value of p is: 0～4
The value of q is: 0～1
From the general structure of above-mentioned poly-polyfluoroalkoxy ether acid, poly-polyfluoroalkoxy ether acid and its esters are in the environment
Do not produce stable carbon 8, be not belonging to the carbon atom straight chain perfluorocarbon saturated hydrocarbons homologue more than 8 yet, simultaneously as the drawing of ehter bond
Enter, also make its degradation property increase, therefore, will not persistently be present in environment, it is difficult to form biology savings property, thus to human body
Damage.
Further, described poly-polyfluoroalkoxy ether acid is the poly-polyfluoroalkoxy ether acid breast of end group band halogen or hydrogen
Agent.
In the present invention, use poly-polyfluoroalkoxy ether acid emulsifying agent substitute in existing fluoropolymer manufacture use most
PFOA/ PFOS is effective, shows: the performance indications of described poly-polyfluoroalkoxy ether acid emulsifying agent include:
Acid number (in terms of NaOH): < 150mg/g；
Cross oxygen value: < 1.5 g/100g；
Boiling point: < 260 DEG C；
Surface tension: < 40mN/m；
Critical micelle concentration (CMC): < 5%.
Optimizing, the performance indications of described poly-polyfluoroalkoxy ether acid emulsifying agent farther include:
Acid number (in terms of NaOH): < 100mg/g；
Cross oxygen value: < 0.5g/100g；
Boiling point: < 160 DEG C；
Surface tension: < 20mN/m；
Critical micelle concentration (CMC): < 1.5 %.
In the present invention, the selection of fluorinated monomer can include following several situation:
(I) dividing by physical state, described fluorinated monomer can be gaseous fluorinated monomer or liquid fluorinated monomers two class,
It can also be the combination of the fluorinated monomer of gaseous state and liquid；
(II) pressing structural formula to divide, one or more described fluorinated monomers include the fluorine-containing list of end group band halogen or hydrogen
Body, or, one or more described fluorinated monomers include perfluorinated monomer.
In invention, described liquid phase polymerization refers to aqueous emulsion polymerization, it follows that in this aqueous emulsion polymerization,
Fluorinated monomer outer and as poly-polyfluoroalkoxy ether acid emulsifying agent outside, the most also should include water and initiator, the choosing of initiator
Select relatively simple, mainly have two classes: inorganic peroxide (such as persulfate etc.), organic peroxide (alkyl peroxide
Deng).
For preferably realizing the polyreaction of fluoropolymer, the amount of poly-polyfluoroalkoxy ether acid is also limited by the present invention
Fixed, as follows: described aqueous emulsion polymerization refers to that poly-polyfluoroalkoxy ether acid is as emulsifying agent and this aqueous emulsion polymerization
The weight proportion of middle water is (0.1～20): 100.
The fluoropolymer that the present invention relates to can be prepared by the following method: is carried out water by one or more fluorinated monomers
Emulsion is polymerized, and when aqueous emulsion polymerization using poly-polyfluoroalkoxy ether acid and salt thereof as emulsifying agent, described poly-polyfluoroalkoxy
Ether acid and salt thereof are (0.1～20) with the weight proportion of water in this aqueous emulsion polymerization: 100.
The fluorinated monomer of indication of the present invention can include the one in tetrafluoroethene, CTFE, vinylidene, fluorothene
Or multiple, further, described fluorinated monomer also includes hexafluoropropene, perfluoroisopropyl vinyl ethers, perfluoro alkyl ethylene
One or more in base ether, hexafluoroethylene, aqueous emulsion polymerization can be homopolymerization, is i.e. gathered by a kind of fluorinated monomer
Closing, the fluoropolymer being polymerized is homopolymer, such as:
(1) fluorinated monomer described in is politef, using poly-polyfluoroalkoxy ether acid and salt thereof as emulsifying agent
Aqueous emulsion polymerization is polymerized, wherein, poly-polyfluoroalkoxy ether acid and salt thereof and the weight of water in aqueous emulsion polymerization
Amount ratio is (0.1～0.45): 100.
(2) fluorinated monomer described in is polytrifluorochloroethylene, using poly-polyfluoroalkoxy ether acid and salt thereof as emulsifying agent
Aqueous emulsion polymerization in be polymerized, wherein, poly-polyfluoroalkoxy ether acid and salt thereof and water in aqueous emulsion polymerization
Weight ratio is (0.4～0.75): 100.
Same, the aqueous emulsion polymerization of indication of the present invention can also be copolyreaction, i.e. different by two or more
Fluorinated monomer is polymerized, and the fluoropolymer being polymerized is copolymer, such as:
(1) fluorinated monomer described in is vinylidene and CTFE, is making with poly-polyfluoroalkoxy ether acid and salt thereof
For being polymerized in the aqueous emulsion polymerization of emulsifying agent, wherein, poly-polyfluoroalkoxy ether acid and salt thereof and aqueous emulsion polymerization body
In system, the weight ratio of water is (0.5～0.9): 100.
(2) fluorinated monomer described in is vinylidene, tetrafluoroethene and hexafluoropropene, with poly-polyfluoroalkoxy ether acid and
Its salt is polymerized as in the aqueous emulsion polymerization of emulsifying agent, wherein, and poly-polyfluoroalkoxy ether acid and salt thereof and aqueous emulsion
In polymerization system, the weight ratio of water is (0.1～0.35): 100.
The present invention compared with prior art, has the following advantages and beneficial effect:
(1) present invention is using poly-polyfluoroalkoxy ether acid and salt thereof as the emulsifying in fluoropolymer aqueous emulsion polymerization
Agent, can effectively replace existing fluorine-containing emulsifier such as: PFOA/ PFOS etc., environmental friendliness, this poly-polyfluoroalkoxy ether acid and
Its salt will not produce stable carbon 8 in the environment, is also not belonging to the homologue of the carbon atom straight chain perfluorocarbon saturated hydrocarbons more than 8,
Simultaneously as the introducing of ehter bond, more make its degradation property increase, be difficult to be enriched with in the environment, be suitably widely popularized use.
(2) present invention is by poly-polyfluoroalkoxy ether acid and salt thereof as emulsifying agent, one or more fluorinated monomers enter
Row aqueous emulsion polymerization, prepared fluoropolymer does not contains perfluoro caprylic acid or perfluorooctane sulfonate, meets environmental requirement, there is not biology
Accumulative and other toxicity, can be widely applied in the field that the requirement of the safety coefficient such as kitchen tools, medicine is higher.
(3) solid of the fluorinated monomer aqueous emulsion in the present invention, produced with this kind of poly-polyfluoroalkoxy ether acid and salt thereof
Content is high (calculated by mass), is not increasing manufacturing facilities and equipment output per single reactor can be greatly improved, such as in the case of personnel:
With the solids content (calculated by mass) of fluorinated monomer aqueous emulsion prepared by this kind of poly-polyfluoroalkoxy ether acid and salt thereof, Ke Yida
To 35%～60%, it it is the solid of the fluorinated monomer aqueous emulsion typically using perfluoroalkyl acid and salt thereof to produce as surfactant
2～3 times of content.
(4) enforcement of the present invention applies also for using the aqueous emulsion polymerization of fluorinated monomer of tradition fluorinated emulsifying agent
Equipment, effectively raises the cost benefit of this polyreaction, great market value.
(5) in the present invention, needed for the fluorinated monomer aqueous emulsion with this kind of poly-polyfluoroalkoxy ether acid and salt production thereof
Production time is short, and the production capacity of process units can be greatly improved, and reduces production cost, such as: use perfluoroalkyl acid and
Salt produces Kynoar as emulsifying agent, and the one-pot reaction time is generally 8～10 hours, as used this kind of poly-polyfluoroalkoxy
Ether acid acid and salt thereof are as producing the surfactant of Kynoar, and its one-pot reaction time can foreshorten to 4～6 hours.
(6) in the present invention, nano level fluorinated monomer water and milk can be produced with this kind of poly-polyfluoroalkoxy ether acid and salt thereof
Liquid, emulsion is light blue transparence.
(7) fluorinated monomer of super high molecular weight in the present invention, can be produced with this kind of poly-polyfluoroalkoxy ether acid and salt thereof
Aqueous emulsion and sub-material, the relative number average molecular weight of general fluorinated monomer polymer is more than 10*106。
Detailed description of the invention
Below the goal of the invention of the present invention, technical scheme and beneficial effect are described in further detail.
It it is noted that described further below is all exemplary, it is intended to the required present invention is provided further
Bright, except as otherwise noted, all technology used herein and scientific terminology have the common skill with the technical field of the invention
The identical meanings that art personnel are generally understood that.
U.S. Environmental Protection Agency (EPA) (EPA) has revealed that PFOA/ PFOS and salt thereof have that degradability is poor, be prone to enrichment etc. in environment
Characteristic, all can cause toxic hazard to environment and human body, but due to its special performance, PFOA/ PFOS is often used for producing
Processing aid indispensable during high-effect fluoropolymer, these dynamical fluoropolymers are widely used the most
In the people's livelihood articles for use such as science and technology of aviation, transport, electron trade and kitchen tools, long-term use, it is most likely that cause cancer etc. are great
Disease.Existing published patent documentation CN101218264B, CN102089335A, CN101745338A, CN101287766,
CN101291987 has disclosed the harm of above-mentioned PFOA/ PFOS, and wishes to find one can substitute PFOA/ PFOS, and conduct
The fluorine-containing emulsifier that surfactant during aqueous emulsion polymerization uses, these fluorine-containing emulsifiers such as: PFPE, ring-type containing fluorination
Compound, replacement perfluoro caprylic acid and the fluorine-containing emulsifier of its esters, general formula X CF2CF2(O)MCF2CF2OCF2The fluorine-containing breast that COOA represents
Agent can be used to the aqueous emulsion polymerization of fluorinated monomer, also show the biology lower than PFOA/ PFOS and salt thereof
Accumulation and environmental degradability, but further, it is intended that find a kind of more efficient implementation, it may be assumed that can not only substitute
The fluorine-containing emulsifier that PFOA/ PFOS uses as surfactant during aqueous emulsion polymerization, simultaneously, moreover it is possible to raising polymerization time,
The production targets such as polymerization yield rate, thus meet cost-benefit accounting.To this end, present invention is disclosed a kind of without perfluoro caprylic acid or
The fluoropolymer of perfluorooctane sulfonate, its technical scheme has related generally to the improvement in terms of three below:
(1) select poly-polyfluoroalkoxy ether acid and salt replacement PFOA/ PFOS thereof as fluorine-containing emulsifier, can effectively answer
Aqueous emulsion polymerization for fluorinated monomer；
(2) fluoropolymer prepared is without perfluoro caprylic acid or perfluorooctane sulfonate, meets environmental requirement；
(3) meet cost accounting, do not increase manufacturing facilities and personnel in the case of can be greatly improved equipment one-pot produce
Amount, simultaneously, moreover it is possible to improve the production target such as polymerization time, polymerization yield rate.
The following is and technical solution of the present invention is further described:
Fluoropolymer involved in the present invention be by one or more fluorinated monomers at poly-polyfluoroalkoxy ether acid and
Salt obtains after liquid phase polymerization as in the case of emulsifying agent, and wherein, poly-polyfluoroalkoxy ether acid is selected from following one or several
The combination planted:
Meet the poly-polyfluoroalkoxy ether acid of lower formula I:
(I),
Meet the poly-polyfluoroalkoxy ether acid of lower formula II:
(II),
Meet the poly-polyfluoroalkoxy ether acid of lower formula III:
(III),
Wherein:
T:、、、、；
X:H, Cl, Br, I；
R:H, Cl, Br, I；
Y:SO3H and salt, COOH and salt thereof, CH2CH2COOH and salt, CH2CH2SO3H and salt thereof,
COOCH2CH2COOH and salt, COOCH2CH2SO3H and salt thereof,And salt；And salt；
The value of n is: 0～4
The value of m is: 1～20
The value of p is: 0～4
The value of q is: 0～1
From the general structure of above-mentioned poly-polyfluoroalkoxy ether acid, the poly-polyfluoroalkoxy ether acid emulsifying that the present invention relates to
Agent can be the poly-polyfluoroalkoxy ether acid emulsifying agent of end group band halogen or hydrogen, such as: by vinylidene, oxygen, tetrafluoro second
Alkene and hexafluoropropene mix by a certain percentage, and under 500W ultra-vioket radiation, holding system temperature is at 65 DEG C, by photooxidation certainly
By base telomerisation, the poly-polyfluoroalkoxy ether acid of end group band hydrogen can be obtained.Structural formula is as follows:
Wherein, the value of n is: 0～4；The value of m is: 1～20；The value of p is: 0～4；The value of q is: 0～1.
The most such as: mix with certain proportion with bromotrifluoroethylene, oxygen, tetrafluoroethene and hexafluoropropene, in 500W ultraviolet
Under light irradiation, keep system temperature at 65 DEG C, reacted by photooxidation free poly tone, the poly-many of end group band bromine can be obtained
Fluoroalkyloxy ether acid emulsifying agent.Structural formula is as follows:
Wherein, the value of n is: 0～4；The value of m is: 1～20；The value of p is: 0～4；The value of q is: 0～1.
It is pointed out that in the structural formula of end group band halogen or the poly-polyfluoroalkoxy ether acid emulsifying agent of hydrogen, when
When on end group, the halogen of band is all F, i.e. PFPE, for commercial production, large-scale production can not be realized, it is necessary to
Adding institute's band halogen on end group in preparation process is not the monomer of F, as chain-transferring agent, could realize industrialized production, raw
Production. art is the most numerous and diverse, therefore, and the end group band halogen that the present invention relates to or the poly-polyfluoroalkoxy ether acid emulsifying agent of hydrogen
Do not include PFPE emulsifying agent.
When reality is applied, owing to above-mentioned poly-polyfluoroalkoxy ether acid and its esters will not produce stable carbon in the environment
8, also it is not belonging to the homologue of the carbon atom straight chain perfluorocarbon saturated hydrocarbons more than 8, simultaneously as the introducing of ehter bond, also makes it drop
Solution performance increase, therefore, the most poly-polyfluoroalkoxy ether acid as fluorine-containing emulsifier for fluorinated monomer aqueous emulsion polymerization and
During the fluoropolymer prepared, this fluoropolymer does not contains perfluoro caprylic acid or perfluorooctane sulfonate, will not persistently be present in environment,
Also it is difficult to form biological savings property, can be widely applied to the safety coefficient such as kitchen tools, medicine and require in higher people's livelihood articles for use, will not
Human body is damaged.
On this basis, the performance indications of the above-mentioned poly-polyfluoroalkoxy ether acid emulsifying agent enumerated are measured by we,
As shown in table 1:
Table 1
The liquid-phase polymerization that the present invention relates to is the preparation method of the fluoropolymer of a kind of routine, in the present invention,
This liquid phase polymerization refers to aqueous emulsion polymerization, the aqueous emulsion polymerization in its polymerization process mainly have fluorinated monomer, initiator,
Water, four elements of emulsifying agent, it is known that, we have found a kind of new fluorine-containing emulsifier (that is: poly-polyfluoroalkoxy
Ether acid emulsifying agent) substitute PFOA/ PFOS, and the fluoropolymer prepared can be solid-state, and pungent without perfluoro caprylic acid or perfluor
Sulfonic acid, certainly, to better implement the present invention, we also need fluorochemical monomer, initiator, poly-polyfluoroalkoxy ether acid emulsifying agent
Select with the proportioning etc. of water, indispensable.In invention, the selection of initiator mainly has two classes: inorganic peroxide (as
Persulfate etc.), organic peroxide (alkyl peroxide etc.)；In the selection course of fluorinated monomer, it has been found that fluorination
The selection of monomer can include following several situation:
(1) by physical state divide, fluorinated monomer can be gaseous fluorinated monomer (such as: tetrafluoroethene, CTFE,
Vinylidene, hexafluoropropene etc.) or liquid fluorinated monomers (such as: perfluoropropylvinylether, perfluoro methyl vinyl ether etc.)
Two classes, it is also possible to be the combination of the fluorinated monomer of gaseous state and liquid (such as: tetrafluoroethene and the mixing of perfluoropropylvinylether
The mixture of thing, vinylidene and perfluoro methyl vinyl ether)；
(2) pressing structural formula to divide, fluorinated monomer can include the fluorochemical monomer of end group band halogen or hydrogen (such as: trifluoro chlorine
Ethylene, vinylidene etc.), it is also possible to include perfluorinated monomer (such as: tetrafluoroethene, perfluoropropylvinylether etc.).
From above-mentioned situation, the fluorinated monomer that the present invention relates to can be tetrafluoroethene, CTFE, hexafluoro third
Alkene, vinylidene, hexafluoropropylene oxide, perfluoroalkyl vinyl ether class, one or more in fluorothene etc., apply in reality
Time, the difference of the fluoropolymer owing to producing, corresponding, choose suitable fluorinated monomer and carry out homopolymerization or copolymerization also has accordingly
Standard, these are all by disclosed in prior art, but the present invention desirably finds out and is applicable to these homopolymerizations or copolymerization is anti-
The poly-polyfluoroalkoxy ether acid emulsifying agent answered and the proportioning of water so that under conditions of initiator exists, these homopolymerizations or copolymerization
Reaction all can embody the features such as polymerization time is fast, polymerization yield rate is high, meanwhile, the fluoropolymer prepared without perfluoro caprylic acid or
Perfluorooctane sulfonate.To this end, the aqueous emulsion polymerization of fluorinated monomer is defined by the present invention, limit its poly-polyfluoro alcoxyl used
Base ether acid (using as emulsifying agent) is (0.1～20) with the weight proportion of water in this aqueous emulsion polymerization: 100, optimization,
Its weight proportion is (0.1～0.9): 100.
In actual production process, by prepared without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate with conduct
The aqueous liquid dispersion of the aqueous solution of the salt of the poly-polyfluoroalkoxy ether acid of emulsifying agent, we are also referred to as dispersion.
First, it is known that this dispersion is also without perfluoro caprylic acid or perfluorooctane sulfonate, secondly, without perfluoro caprylic acid in this dispersion
Or the weight proportion of the fluoropolymer of perfluorooctane sulfonate and water should be (3～7): 10.In actual mechanical process, as emulsifying
The aqueous solution of the salt of the poly-polyfluoroalkoxy ether acid of agent is at the uniform velocity to drip poly-polyfluoroalkoxy ether acid in alkaline aqueous solution,
Dropping is while stirring and preparing, and rate of addition and mixing speed difference 0.1～10ml/s, 20～200rpm, preparation temperature is 25
～50 DEG C, the pH value of the aqueous solution of the salt of the poly-polyfluoroalkoxy ether acid prepared is 7～9, poly-polyfluoroalkoxy ether acid and water
Weight proportion is (0.1～20): 100, alkaline aqueous solution then can choose ammonia, sodium hydrate aqueous solution, potassium hydroxide aqueous solution,
The mixing of one or more in magnesium hydroxide aqueous solution, triethanolamine aqueous solution.
Below with four exemplary embodiments enumerate explanation the present invention may relate to without the pungent sulphur of perfluoro caprylic acid or perfluor
The concrete preparation method of the fluoropolymer of acid, certainly, protection scope of the present invention is not limited to following example.
Embodiment 1:
Politef is produced through aqueous emulsion polymerization, in this aqueous emulsion polymerization by gaseous fluorinated monomer tetrafluoroethene
The addition bromo-poly-polyfluoroalkoxy ether acid of 1-, as fluorine-containing emulsifier, is embodied as step as follows:
A: the aqueous solution of the salt of the preparation bromo-poly-polyfluoroalkoxy carboxylic ether acid of 1-: add 700ml in 2000ml glass beaker
Deionized water and the ammonia of 100ml 25%, then by liquid glass droplet funnel the most at the uniform velocity dropping 200g in deionized water
The bromo-poly-polyfluoroalkanoic acids of 1-, is stirred while dropping, and mixing speed is 80 rpm, then, obtains poly-polyfluoro alcoxyl
Base ether acid ammonia spirit is standby, and wherein, the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonium of 1-is 20:100 with the weight proportion of water；
B: polymerization prepares: carry out replacing deoxygenation to polymerization autoclave with nitrogen, make this polymerization autoclave be evacuated to oxygen in still
Content≤25ppm；
C: polymerization process:
A: feed intake: in the 100L rustless steel polymerization autoclave have baffle plate add 55kg deionized water, 972g paraffin with
And the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonia spirit of 1-of 962.5g20%；
B: preparation initiator: 6.0g Ammonium persulfate. is dissolved in 1L warm water (about 75 DEG C), obtains the Ammonium persulfate. of 0.6%
Aqueous solution；
C: initiation reaction: pressurize polymerization autoclave with tetrafluoroethene, stirs and is warming up to 73 DEG C, stirring
Speed is 200rpm；Again with tetrafluoroethene, polymerization autoclave is boosted, until in polymeric kettle pressure reach 1.865Mpa,
When temperature is 73 DEG C, in polymeric kettle, add the initiator prepared in step b with dosing pump；
D: when the pressure of polymerization autoclave is down to 1.756MPa (generally in 5 minutes), again adds tetrafluoroethene, make
Pressure in polymerization autoclave is maintained at 1.865MPa, temperature is 73 DEG C, carries out polyreaction；
E: when tetrafluoroethene addition reaches 27kg, make polyreaction stop, the total response time is 160min.
After measured, the amount of the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonia of 1-used is 192.5g.
Comparative example 1:
Politef is produced through aqueous emulsion polymerization, in this aqueous emulsion polymerization by gaseous fluorinated monomer tetrafluoroethene
Addition perfluorooctanoic acid is as fluorine-containing emulsifier, and implementation step is same as in Example 1.
The aqueous dispersion of polytetrafluoroethyland that the method is obtained by we is measured, as follows: polymerization reaction time
For 330min, the amount of the perfluorooctanoic acid used is 275g.
Embodiment 2:
Produced polytrifluorochloroethylene by gaseous fluorinated monomer CTFE through aqueous emulsion polymerization, gather in this aqueous emulsion
In conjunction, the addition bromo-poly-polyfluoroalkoxy carboxylic ether acid of 1-is as fluorine-containing emulsifier, is embodied as step as follows:
A: the aqueous solution of the salt of the preparation bromo-poly-polyfluoroalkoxy carboxylic ether acid of 1-: add in 5000ml glass beaker
2800ml deionized water and the ammonia of 400ml 25%, then slowly at the uniform velocity dripped in deionized water by liquid glass droplet funnel
The bromo-poly-polyfluoroalkanoic acids of 1-of 800g, is stirred while dropping, and mixing speed is 80 rpm, then, is gathered many
Fluoroalkyloxy ether acid ammonia spirit is standby, and wherein, the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonia of 1-is 20 with the weight proportion of water:
100；
B: polymerization prepares: carry out replacing deoxygenation to polymerization autoclave with nitrogen, make this polymerization autoclave be evacuated to polymeric kettle
Interior oxygen content≤20ppm；
C: polymerization process:
A: feed intake: add 75kg deionized water, 160g sodium carbonate in the 100L rustless steel polymerization autoclave have baffle plate
And the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonia spirit of 1-of 962.5g 20%；
B: preparation initiator: 8.0g Ammonium persulfate. is dissolved in 1L warm water (about 75 DEG C), obtains the Ammonium persulfate. of 0.8%
Aqueous solution；
C: initiation reaction: pressurize polymerization autoclave with CTFE, stirs and is warming up to 50 DEG C, stir
Mixing speed is 500rpm；With CTFE, polymerization autoclave is boosted again, until pressure reaches in polymeric kettle
When 2.52Mpa, temperature are 50 DEG C, with dosing pump, in polymeric kettle, add the initiator prepared in step b；
D: in course of reaction, continues to add CTFE monomer in reactor, to keep reactor pressure to maintain
2.52Mpa, when CTFE addition reaches 35kg, makes polyreaction stop, and the total response time is 300min.
After measured, the amount of the bromo-poly-polyfluoroalkoxy carboxylic ether acid ammonia of 1-used is 487.5g.
Embodiment 3:
Vinylidene CTFE is produced through aqueous emulsion polymerization, in this aqueous emulsion by vinylidene, CTFE
In polymerization, the addition chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-is as fluorine-containing emulsifier, is embodied as step as follows:
A: the aqueous solution of the salt of the preparation chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99 of 1-: add in 2000ml glass beaker
700ml deionized water and the ammonia of 100ml 25%, then slowly at the uniform velocity dripped in deionized water by liquid glass droplet funnel
The chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99 of 1-of 200g, is stirred while dropping, and mixing speed is 80 rpm, so
After, obtain poly-polyfluoroalkoxy ether acid aqueous ammonium, wherein, the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-and the weight of water
Proportioning is 20:100；
B: polymerization prepares: carry out replacing deoxygenation to polymerization autoclave with nitrogen, make this polymerization autoclave be evacuated to polymeric kettle
Interior oxygen content≤25ppm；
C: polymerization process:
A: feed intake: in the 100L rustless steel polymerization autoclave have baffle plate add 64kg deionized water, 800g paraffin with
And the aqueous solution of the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-of 2240g 20%；
B: preparation initiator: 32g Ammonium persulfate. is dissolved in 1L warm water (about 75 DEG C), obtains the Ammonium persulfate. water of 3.2%
Solution, then, adds the diethyl malonate of 80 grams in the ammonium persulfate aqueous solution of 3.2%, and the mixing obtaining compounding causes
Agent；
C: initiation reaction: use the vinylidene of 95mol% and the mix monomer of the CTFE of 5mol%, high pressure is gathered
Closing still to boost, stir and be warming up to 60 DEG C, mixing speed is 200rpm.Then with mix monomer, reactor is continued
The 2.5Mpa that is depressed into of continuing rising, maintenance autoclave temp is at 6060 DEG C, with dosing pump, by molten for the mixed initiator configured in step b
Liquid squeezes into reactor；
D: when the mix monomer addition of vinylidene, CTFE reaches 37Kg, make polyreaction stop, adding up to
Response time is 320min.
After measured, the amount of the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-used is 448g.
Embodiment 4:
Vinylidene hexafluoropropene tetrafluoro is produced through aqueous emulsion polymerization by vinylidene, hexafluoropropene, tetrafluoroethene
Ethylene, in this aqueous emulsion polymerization, the addition chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-is as fluorine-containing emulsifier, specifically real
Execute step as follows:
A: the aqueous solution of the salt of the preparation chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99 of 1-: add in 5000ml glass beaker
2800ml deionized water and the ammonia of 400ml 25%, then slowly at the uniform velocity dripped in deionized water by liquid glass droplet funnel
The chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99 of 1-of 800g, is stirred while dropping, and mixing speed is 80 rpm, so
After, obtain poly-polyfluoroalkoxy ether acid aqueous ammonium, wherein, the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-and the weight of water
Proportioning is 20:100.
B: polymerization prepares: carry out replacing deoxygenation to polymerization autoclave with nitrogen, make this polymerization autoclave be evacuated to polymeric kettle
Interior oxygen content≤20ppm.
C: polymerization process:
A: feed intake: add 60kg deionized water, 80gPH regulator in the 100L rustless steel polymerization autoclave have baffle plate
The aqueous solution of the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-of (disodium hydrogen phosphate) and 750g 20%；
B: preparation initiator: 12.5g Ammonium persulfate. is dissolved in 1L warm water (about 75 DEG C), obtains the persulfuric acid of 1.25%
Aqueous ammonium；
The tetrafluoroethene mixing of the vinylidene of c: initiation reaction: 45mol%, the hexafluoropropene of 50mol% and 5mol% is single
Body, boosts to polymerization autoclave, stirs and is warming up to 120 DEG C, and mixing speed is 200rpm, then single with mixing
Reactor is continued to boost to 3.5Mpa by body, and maintenance autoclave temp is at 120 DEG C, with dosing pump, mixed by configured in step b
Close initiator solution and squeeze into reactor, start reaction；
D: when mix monomer inventory reaches 16.8Kg, keeping reaction temperature is 120 DEG C, and mixing speed 200rpm is used
Dosing pump, adds 10ml diethyl oxalate in autoclave；
E: when the mixing addition of vinylidene, hexafluoropropene and tetrafluoroethene reaches 24Kg, make polyreaction stop.
The total response time is 260min.
After measured, the amount of the chloro-poly-polyfluoroalkoxy ether-P-TOLUENE SULFO ACID 99's ammonium of 1-used is 448g.
In the industrial production, for obtaining by prepared without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate with work
For the aqueous liquid dispersion of aqueous solution of salt of the poly-polyfluoroalkoxy ether acid of emulsifying agent, also can be in the following way:
As a example by separately below for the fluoropolymer prepared by above-described embodiment 1～4, had by embodiment 5～8
Body explanation.
Embodiment 5:
Carrying out the step of embodiment 1, after polyreaction stops, unreacted tetrafluoroethene in polymerization autoclave is being arranged
Enter recovery system, the aqueous polytetrafluoroethyldispersion emulsion obtained by cooling, and remove upper strata paraffin.
After measured, said method the solid component concentration of the aqueous polytetrafluoroethyldispersion emulsion prepared is about 49.09%, with
In aqueous emulsion polymerization, the weight ratio of water is 0.35:100.
Comparative example 2:
On the basis of comparative example 1, use the step of above-described embodiment 5, it is thus achieved that aqueous polytetrafluoroethyldispersion emulsion, through surveying
Fixed, the solid component concentration of this aqueous polytetrafluoroethyldispersion emulsion is about 32.6%, with the weight ratio of water in aqueous emulsion polymerization is
0.5:100.
Above-described embodiment 1, embodiment 5 and comparative example 1, comparative example 2 are added up, it is thus achieved that following data, such as table 2 institute
Show:
Table 2
Embodiment 6:
Carrying out the step of embodiment 2, after polyreaction stops, by CTFE unreacted in polymerization autoclave
Enter recovery system, the polytrifluorochloroethylene water-based emulsion obtained by cooling.
After measured, said method the solid component concentration of the aqueous polytetrafluoroethyldispersion emulsion prepared is about 43.38%, with
In aqueous emulsion polymerization, the weight ratio of water is 0.65:100.
Embodiment 7:
Carrying out the step of embodiment 3, after polyreaction stops, inclined by 95mol% unreacted in polymerization autoclave
The mix monomer of the CTFE of fluorothene and 5mol%, enters recovery system, the vinylidene trifluoro chlorine obtained by cooling
The water-based emulsion of ethylene copolymer, removes the paraffin on upper strata.
After measured, said method the solid constituent of the water-based emulsion of the vinylidene chlorotrifluoroethylene prepared
Concentration is about 46.88%, is 0.7:100 with the weight ratio of water in aqueous emulsion polymerization.
Embodiment 8:
Carrying out the step of embodiment 4, polyreaction stops, inclined by 45mol% unreacted in polymerization autoclave
The tetrafluoroethene mix monomer of fluorothene, the hexafluoropropene of 50mol% and 5mol% enters recovery system, the inclined fluorine obtained by cooling
The water-based emulsion of ethylene hexafluoropropene TFE copolymer.
After measured, said method the water-based emulsion of the vinylidene hexafluoropropene TFE copolymer prepared
Solid component concentration is about 37%, is 0.25:100 with the weight ratio of water in aqueous emulsion polymerization.
The method recorded according to JIS-K5663, we are to above-described embodiment 5～8 and the aqueous liquid dispersion that obtains of comparative example 2
The dispersion stabilization of (dispersion) is determined, it is thus achieved that following data, as shown in table 3:
Table 3
Wherein, the method for testing of mechanical stability is, is stirred by aqueous liquid dispersion 100g in 5000rpm even phase disperser
5min, measures its coagulation amount (unit: ppm) after placing 1d；The method of testing of high-temperature stability is, aqueous liquid dispersion is at 50 DEG C
After placing 60d, visually to determine whether precipitum.
In actual industrial production, above-mentioned four kinds of fluoropolymers (politef, the polytrifluorochloroethylene, partially related to
Fluorothene CTFE, vinylidene hexafluoropropene tetrafluoroethene) it is respectively provided with wide application prospect, such as: oil
The numerous areas such as chemical industry, electric, building coating or dipping, automobile decoration, appliance shell, medical science, quasiconductor, fiber cloth,
Now for patent documentation CN101218264B(documents 1), CN102089335A(documents 2), CN101745338A(pair
Than file 3), CN101287766(documents 4), CN101291987(documents 5) involved by fluorine-containing emulsifier, with reality
Execute as a example by example 1 and embodiment 5 are prepared the detailed description of the invention of politef and dispersion thereof, prepare politef respectively
And dispersion, its preparation time is as shown in table 4 with product index:
Table 4
According to above-mentioned data analysis, the present invention relates to by poly-polyfluoroalkoxy ether acid (the bromo-poly-polyfluoroalkoxy of 1-
Carboxylic ether acid ammonium) as emulsifying agent, during preparing fluoropolymer (politef) and aqueous liquid dispersion thereof, with contrast
File 1～5 compares, and all has a clear superiority on primary ion particle diameter, the solids content of aqueous liquid dispersion, percentage elongation,
The polymerization time of fluoropolymer, the particle specific gravity of SSG(fluoropolymer), to draw high the effect in terms of intensity the most ideal,
Suitably it is widely popularized use.
The above, be only presently preferred embodiments of the present invention, and the present invention not does any pro forma restriction, every depends on
Any simple modification of being made above example according to the technical spirit of the present invention, equivalent variations, each fall within the protection of the present invention
Within the scope of.
Claims (6)
1. one kind does not contains perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, it is characterised in that: single by one or more fluorinations
Body obtains without the pungent sulphur of perfluoro caprylic acid or perfluor in the case of poly-polyfluoroalkoxy ether acid is as emulsifying agent after liquid phase polymerization
The fluoropolymer of acid, described poly-polyfluoroalkoxy ether acid is selected from the following combination of one or more:
Meet the poly-polyfluoroalkoxy ether acid of lower formula I:
(I),
Meet the poly-polyfluoroalkoxy ether acid of lower formula II:
(II),
Wherein:
T:、、、；
X:H, Br, I；
R:H, Br, I；
Y:SO3H and salt, COOH and salt thereof, CH2CH2COOH and salt, CH2CH2SO3H and salt thereof,
COOCH2CH2COOH and salt, COOCH2CH2SO3H and
Salt,And salt；And salt；
The value of n is: 0～4；
The value of m is: 1～20；
The value of p is: 0～4；
The value of q is: 0～1
Described poly-polyfluoroalkoxy ether acid is the poly-polyfluoroalkoxy ether acid emulsifying agent of end group band halogen or hydrogen,
The performance indications of described poly-polyfluoroalkoxy ether acid emulsifying agent include:
In terms of NaOH, acid number: < 100mg/g；
Cross oxygen value: < 0.5g/100g；
Boiling point: < 160 DEG C；
Surface tension: < 40mN/m；
Critical micelle concentration (CMC): < 1.5 %,
Described liquid phase polymerization refers to that aqueous emulsion polymerization, described aqueous emulsion polymerization refer to that poly-polyfluoroalkoxy ether acid is as emulsifying
Agent is (0.1～20) with the weight proportion of water in this aqueous emulsion polymerization: 100.
It is the most according to claim 1 a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, it is characterised in that:
Described fluorinated monomer is gaseous fluorinated monomer.
3., according to described a kind of of claim 1 without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, its feature exists
In: described fluorinated monomer is liquid fluorinated monomers.
It is the most according to claim 1 a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, it is characterised in that:
Described multiple fluorinated monomer is the fluorinated monomer of gaseous state and liquid.
It is the most according to claim 1 a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, it is characterised in that:
One or more described fluorinated monomers include end group band halogen or the fluorochemical monomer of hydrogen.
It is the most according to claim 1 a kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate, it is characterised in that:
One or more described fluorinated monomers include perfluorinated monomer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410195268.5A CN103936906B (en) | 2014-05-09 | 2014-05-09 | A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410195268.5A CN103936906B (en) | 2014-05-09 | 2014-05-09 | A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103936906A CN103936906A (en) | 2014-07-23 |
| CN103936906B true CN103936906B (en) | 2016-08-31 |
Family
ID=51184806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410195268.5A Active CN103936906B (en) | 2014-05-09 | 2014-05-09 | A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103936906B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103936905B (en) * | 2014-05-09 | 2016-09-14 | 成都晨光博达橡塑有限公司 | A kind of fluoropolymer and preparation method thereof |
| CN109384911B (en) | 2018-11-15 | 2019-08-27 | 四川科源精诚新材料科技有限公司 | A kind of perfluorinated surfactant and preparation method thereof |
| WO2021145441A1 (en) * | 2020-01-15 | 2021-07-22 | ダイキン工業株式会社 | Method for producing low molecular weight polytetrafluoroethylene, composition, and low molecular weight polytetrafluoroethylene |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1172122A (en) * | 1996-07-01 | 1998-02-04 | 奥西蒙特公司 | VDF polymerization process |
| CN103270060A (en) * | 2010-12-22 | 2013-08-28 | 索尔维特殊聚合物意大利有限公司 | Vinylidene fluoride and trifluoroethylene polymers |
| CN103936905A (en) * | 2014-05-09 | 2014-07-23 | 成都晨光博达橡塑有限公司 | Fluorine-containing polymer and preparation method thereof |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1276072B1 (en) * | 1995-10-31 | 1997-10-24 | Ausimont Spa | PROCESS OF (CO) POLYMERIZATION OF FLUORINATED MONOMERS TO OBTAIN HYDROGEN CONTAINING POLYMERS |
| JP2002128833A (en) * | 2000-10-27 | 2002-05-09 | Nippon Mektron Ltd | Fluorine-containing copolymer and method of producing the same |
| CN102504063B (en) * | 2011-10-31 | 2014-12-31 | 巨化集团公司 | Preparation method of fluorine-containing polymer |
-
2014
- 2014-05-09 CN CN201410195268.5A patent/CN103936906B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1172122A (en) * | 1996-07-01 | 1998-02-04 | 奥西蒙特公司 | VDF polymerization process |
| CN103270060A (en) * | 2010-12-22 | 2013-08-28 | 索尔维特殊聚合物意大利有限公司 | Vinylidene fluoride and trifluoroethylene polymers |
| CN103936905A (en) * | 2014-05-09 | 2014-07-23 | 成都晨光博达橡塑有限公司 | Fluorine-containing polymer and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103936906A (en) | 2014-07-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103936905B (en) | A kind of fluoropolymer and preparation method thereof | |
| CN105218712B (en) | A kind of manufacture method of polytetrafluoroethylene (PTFE) | |
| US7776946B2 (en) | Aqueous emulsion polymerization of fluorinated monomers using a fluorinated surfactant | |
| US7838608B2 (en) | Fluorinated surfactants for making fluoropolymers | |
| CN102504063B (en) | Preparation method of fluorine-containing polymer | |
| WO2007062059A1 (en) | Fluorinated surfactants for use in making a fluoropolymer | |
| CN103936906B (en) | A kind of without perfluoro caprylic acid or the fluoropolymer of perfluorooctane sulfonate | |
| US20130040142A1 (en) | Process for producing ptfe and articles thereof | |
| CN104119544B (en) | The preparation method of the concentrated dispersion liquid of perfluoroethylene-propylene | |
| CN104812781A (en) | Production method for polytetrafluoroethylene aqueous dispersion | |
| JP5673541B2 (en) | Method for producing fluoropolymer | |
| JP5598476B2 (en) | Method for producing fluoropolymer | |
| CN102516438B (en) | Method for preparing fluorine-containing rubber for automobile rubber pipe | |
| JP2015529279A (en) | Fluoroelastomer | |
| CN103739756A (en) | Preparation method of polyvinylidene fluoride polymer with improved thermal stability | |
| CN103951772B (en) | A kind of being applicable to is prepared without perfluoro caprylic acid or the method for the fluoropolymer of perfluorooctane sulfonate | |
| CN103936904B (en) | Dispersion | |
| CN106632794A (en) | A method of preparing fluororubber through microemulsion polymerization | |
| CN106117397B (en) | Fluorine-containing polymer concentrated dispersion liquid and method for preparing fluorine-containing polymer by using same | |
| CN103951772A (en) | Method suitable for preparing fluorine-containing polymer free from perfluoro caprylic acid or perfluorooctane sulfonic acid | |
| CN105246925B (en) | The manufacture method of fluoropolymer | |
| JPWO2009145117A1 (en) | Method for producing fluoropolymer | |
| CN103709305B (en) | A kind of preparation method of fluorubber | |
| CN102145268A (en) | Surfactant composition and application of surfactant composition | |
| CN103459441A (en) | Method for producing fluorine-containing copolymer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No.168, Tengfei 6th Road, Southwest Airport Economic Development Zone, Shuangliu District, Chengdu, Sichuan 610200 China (Sichuan) pilot Free Trade Zone, Chengdu Patentee after: Chengdu Chenguang Boda New Material Co.,Ltd. Address before: 610000 No. 168, Tengfei 6th Road, Southwest Airport Economic Development Zone, Shuangliu County, Chengdu City, Sichuan Province Patentee before: CHENGUANG FLUORO & SILICONE ELASTOMERS CO.,LTD. |