CN103642031B - A kind of high-flow polyphenylene ether sulfone ketone resin and industrialized producing technology thereof - Google Patents
A kind of high-flow polyphenylene ether sulfone ketone resin and industrialized producing technology thereof Download PDFInfo
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- CN103642031B CN103642031B CN201310609135.3A CN201310609135A CN103642031B CN 103642031 B CN103642031 B CN 103642031B CN 201310609135 A CN201310609135 A CN 201310609135A CN 103642031 B CN103642031 B CN 103642031B
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- benzophenone
- polyphenylene ether
- ether sulfone
- ketone resin
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- 239000011347 resin Substances 0.000 title claims abstract description 30
- 229920005989 resin Polymers 0.000 title claims abstract description 30
- 229920001955 polyphenylene ether Polymers 0.000 title claims abstract description 21
- -1 sulfone ketone Chemical class 0.000 title claims abstract description 21
- 238000005516 engineering process Methods 0.000 title claims abstract description 15
- 239000000178 monomer Substances 0.000 claims abstract description 33
- 239000007787 solid Substances 0.000 claims abstract description 25
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 20
- 239000000126 substance Substances 0.000 claims abstract description 18
- 229920001577 copolymer Polymers 0.000 claims abstract description 5
- 239000012965 benzophenone Substances 0.000 claims description 23
- SQNZJJAZBFDUTD-UHFFFAOYSA-N durene Chemical compound CC1=CC(C)=C(C)C=C1C SQNZJJAZBFDUTD-UHFFFAOYSA-N 0.000 claims description 19
- HXJUTPCZVOIRIF-UHFFFAOYSA-N sulfolane Chemical group O=S1(=O)CCCC1 HXJUTPCZVOIRIF-UHFFFAOYSA-N 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 239000004305 biphenyl Substances 0.000 claims description 11
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 claims description 10
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 229910052731 fluorine Inorganic materials 0.000 claims description 10
- XKZQKPRCPNGNFR-UHFFFAOYSA-N 2-(3-hydroxyphenyl)phenol Chemical compound OC1=CC=CC(C=2C(=CC=CC=2)O)=C1 XKZQKPRCPNGNFR-UHFFFAOYSA-N 0.000 claims description 9
- GPAPPPVRLPGFEQ-UHFFFAOYSA-N 4,4'-dichlorodiphenyl sulfone Chemical compound C1=CC(Cl)=CC=C1S(=O)(=O)C1=CC=C(Cl)C=C1 GPAPPPVRLPGFEQ-UHFFFAOYSA-N 0.000 claims description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 9
- 150000003839 salts Chemical class 0.000 claims description 9
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 claims description 8
- DSNHSQKRULAAEI-UHFFFAOYSA-N 1,4-Diethylbenzene Chemical compound CCC1=CC=C(CC)C=C1 DSNHSQKRULAAEI-UHFFFAOYSA-N 0.000 claims description 8
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 8
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 claims description 7
- 238000009835 boiling Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 238000010792 warming Methods 0.000 claims description 7
- LSQARZALBDFYQZ-UHFFFAOYSA-N 4,4'-difluorobenzophenone Chemical compound C1=CC(F)=CC=C1C(=O)C1=CC=C(F)C=C1 LSQARZALBDFYQZ-UHFFFAOYSA-N 0.000 claims description 6
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000011737 fluorine Substances 0.000 claims description 6
- 210000003097 mucus Anatomy 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 150000005323 carbonate salts Chemical class 0.000 claims description 5
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 239000008367 deionised water Substances 0.000 claims description 3
- 229910021641 deionized water Inorganic materials 0.000 claims description 3
- KZTYYGOKRVBIMI-UHFFFAOYSA-N diphenyl sulfone Chemical compound C=1C=CC=CC=1S(=O)(=O)C1=CC=CC=C1 KZTYYGOKRVBIMI-UHFFFAOYSA-N 0.000 claims description 3
- 239000003495 polar organic solvent Substances 0.000 claims description 3
- XFTXWDDQIXYAGY-UHFFFAOYSA-N (3-chlorophenyl)-(4-chlorophenyl)methanone Chemical compound C1=CC(Cl)=CC=C1C(=O)C1=CC=CC(Cl)=C1 XFTXWDDQIXYAGY-UHFFFAOYSA-N 0.000 claims description 2
- FIFXBQVRZOTUNN-UHFFFAOYSA-N (4-chlorophenyl)-(3-fluorophenyl)methanone Chemical compound FC1=CC=CC(C(=O)C=2C=CC(Cl)=CC=2)=C1 FIFXBQVRZOTUNN-UHFFFAOYSA-N 0.000 claims description 2
- OKISUZLXOYGIFP-UHFFFAOYSA-N 4,4'-dichlorobenzophenone Chemical class C1=CC(Cl)=CC=C1C(=O)C1=CC=C(Cl)C=C1 OKISUZLXOYGIFP-UHFFFAOYSA-N 0.000 claims description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 2
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 2
- 238000013019 agitation Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000002798 polar solvent Substances 0.000 claims description 2
- 239000011541 reaction mixture Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000003021 water soluble solvent Substances 0.000 claims description 2
- 125000001174 sulfone group Chemical group 0.000 abstract description 15
- 239000004721 Polyphenylene oxide Substances 0.000 abstract description 12
- 229920000570 polyether Polymers 0.000 abstract description 12
- 239000002904 solvent Substances 0.000 abstract description 9
- 150000008365 aromatic ketones Chemical class 0.000 abstract description 7
- 238000007334 copolymerization reaction Methods 0.000 abstract description 5
- 229920006260 polyaryletherketone Polymers 0.000 abstract description 3
- 238000007493 shaping process Methods 0.000 abstract description 2
- 229920000491 Polyphenylsulfone Polymers 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 15
- 125000000468 ketone group Chemical group 0.000 description 13
- 238000000034 method Methods 0.000 description 9
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 239000011734 sodium Substances 0.000 description 6
- 239000004695 Polyether sulfone Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical compound C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 4
- 229920006393 polyether sulfone Polymers 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000004044 response Effects 0.000 description 4
- 150000003457 sulfones Chemical class 0.000 description 4
- ZHUXSAKDWNNBCQ-UHFFFAOYSA-N (3-fluorophenyl)-(4-fluorophenyl)methanone Chemical compound C1=CC(F)=CC=C1C(=O)C1=CC=CC(F)=C1 ZHUXSAKDWNNBCQ-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 229920000090 poly(aryl ether) Polymers 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 125000000472 sulfonyl group Chemical group *S(*)(=O)=O 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 235000010290 biphenyl Nutrition 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N monobenzene Natural products C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- QRFMXBKGNQEADL-UHFFFAOYSA-N 1,1'-biphenyl;phenol Chemical compound OC1=CC=CC=C1.OC1=CC=CC=C1.C1=CC=CC=C1C1=CC=CC=C1 QRFMXBKGNQEADL-UHFFFAOYSA-N 0.000 description 1
- AUHZEENZYGFFBQ-UHFFFAOYSA-N 1,3,5-trimethylbenzene Chemical compound CC1=CC(C)=CC(C)=C1 AUHZEENZYGFFBQ-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 description 1
- 150000001492 aromatic hydrocarbon derivatives Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
Abstract
The invention discloses a kind of high-flow polyphenylene ether sulfone ketone (PPSUK) resin, it introduces aromatic ketone monomer in PPSU polymkeric substance, especially isomery aromatic ketone monomer copolymerization, containing polyether sulphone and polyaryletherketone random copolymerization structure on the copolymer molecule main chain obtained, wherein
group with
Description
Technical field
The invention belongs to technical field of polymer materials, be specifically related to a kind of high-flow polyphenylene ether sulfone ketone resin PPSUK and industrialized producing technology thereof.
Background technology
Polyether sulphone is a kind of high performance engineering plastics, because they have thermotolerance, hot water resistance, creep resistance, dimensional stability, shock-resistance, chemical proofing, the excellent over-all properties such as nontoxic, fire-retardant, thus for a long time electronics, electrical equipment, machinery, automobile, medical apparatus, food-processing and not the field such as stickness paint be widely used.
Industrial important polyether sulphone comprises polyethersulfone (PES) and biphenyl polyether sulfone (PPSU), all has very high second-order transition temperature (~ 220 DEG C).In use, because polyether sulphone has higher melt viscosity, be not easy the product of molding structure complexity, and in moulding product, have bubble, the defect such as hollow, therefore in the urgent need to improving its processing fluidity, thermal characteristics and don't the impact transparency of its excellence can be kept simultaneously, expand its range of application.In addition, polyether sulphone is more responsive to some chemical solvents, and pressure embrittlement problem easily occurs.
Copolymerization is a kind of effective ways changing molecular structure, if Chinese patent CN200910217764 is by biphenyl sulfone ether and polyethersulfone terpolymer, can change the Tg of polymkeric substance.American documentation literature US20100310804A1 discloses a kind of method of ketone group containing polyether sulphone, it take sulfobenzide as solvent, the mixture of sodium carbonate and salt of wormwood is salt forming agent, 275 DEG C of polyreactions, later stage adds end-capping reagent, anti-depolymerizing agent etc., prepare fusing point from the PPSK of 319 ~ 360 DEG C, but its industrial process unexposed.Chinese patent literature CN102757561A discloses a kind of ketone group containing polyethersulfone resin, mol ratio containing sulfone monomer and ketone group containing monomer is 9:1 ~ 1:1, and it take tetramethylene sulfone as solvent, and toluene is a point aqua, potassium hydroxide solution is salt forming agent, but its industrialized preparing process unexposed.
In actual production and application, the polyether sulphone not adding ketone group monomer is amorphous, and because the viscosity of itself is higher, thus processing temperature, more than 360 DEG C, reaches 380 DEG C or higher, therefore can not apply in some industry usually.There is regular phenomenon in the ternary or the multi-component copolymer polyether sulphone that add ketone group monomer, have fixing fusing point, the introducing due to ketone group adds the regularity of molecule, and its mobility have also been obtained raising.When ketone group containing monomer ratio is greater than 30% of sulfuryl monomer and ketone group monomer sum, polyreaction can more difficult, polymerization produce cycle longer, thus product color and the higher problem of fusing point can be caused, especially when ketone group containing monomer ratio is greater than 40% of sulfuryl monomer and ketone group monomer sum, lower than at the temperature of 240 DEG C, polyreaction occurs hardly.When ketone group containing monomer ratio is greater than 25% of sulfuryl monomer and ketone group monomer sum, the Tm of the random copolymers of gained is greater than 350 DEG C, and its processing temperature of the product of gained can reach 380 DEG C or higher equally, thus causes processing difficulties, is difficult to be widely used.In addition, the transparency of its product also has certain decline.Therefore, controlling ketone group containing monomer ratio in the reasonable scope, is the scheme of polyaryletherketone simple possible developing high workability, easily processing, chemical solvent resistance energy and radiance.
Technique many employings system solid content left and right in 20 ~ 25% scopes of existing production polyaryl ether sulphone resin, producing one ton of polyaryl ether sulphone resin needs to add 3 tons of tetramethylene sulfone.There is following defect in this kind of technique: under (1) identical device condition, the production capacity of polyether sulphone is low; (2) due to tetramethylene sulfone unstable at high temperature, thus make the rate of recovery of whole technical process sulfolan only about 80%, that is often produce 1 ton of polyether sulphone and will lose 600.00KG tetramethylene sulfone, increase production of resins cost.If directly improve the solid content of polymerization system, if design system solid content is in 30 ~ 40% scopes, we find that speed of response is not accelerated along with the increase of concentration in Sulfolane System, on the contrary along with the increase speed of response of concentration declines, when solid content is 30 ~ 35% time, speed of response is dropped by nearly half, and increases production cost.
Summary of the invention
The object of the invention is to overcome above-mentioned prior art defect, a kind of high workability, easily processing, chemical solvent resistance polyphenylene ether sulfone ketone resin are provided.
A kind of high-flow polyphenylene ether sulfone ketone resin of the present invention, its structural formula is
Wherein Ar representative
;
Wherein a:(b+c)=5 ~ 9:1,0≤c≤0.1b.
Preferably, 0.75<a<0.9,0.1<b<0.25,0<c<0.05.
Work as c=0, during a/b >=99, be biphenyl bis-phenol, benzene sulfone and Benzophenone membered copolymer, molecular structure is close to PPSU, and molecule macroscopic properties is suitable with polyphenylene ether sulfone.
Work as c=0, during 1 < a/b < 99, molecular structure is polyethersulfone ketone multipolymer.
Another object of the present invention is to provide a kind of industrialized producing technology improving production capacity, reduce the above-mentioned high-flow polyphenylene ether sulfone ketone resin of production cost, comprises the following steps:
(1) salt-forming reaction
With 4,4'-'-biphenyl diphenol, 4,4'-dichloro diphenyl sulfones, 4,4'-dihalo-benzophenone and 3,4'-dihalo-benzophenone for reaction monomers,
In the reactor of nitrogen filled protection, 4 are added in turn in non-proton intensive polar solvent, 4'-'-biphenyl diphenol, 4, 4'-dichloro diphenyl sulfone, 4, 4'-dihalo-benzophenone, system solid content is 20 ~ 45%, and start stirring heating, after temperature reaches 65 ~ 80 DEG C, continue to be stirred to after monomer all dissolves, be warmed up to 100 DEG C again to add in system than added 4, the alkaline carbonate salt forming agent of 4'-'-biphenyl diphenol mole number excessive 5 ~ 20%, and add a point aqua subsequently, under agitation continue to heat up, system starts salt-forming reaction, temperature controls between 190 ~ 220 DEG C, after system aquifer yield reaches theoretical value, discharge water and point aqua, again system is increased the temperature between 230 ~ 240 DEG C,
Be 20% ~ 25% at the solid content of salt-forming reaction stage system.
(2) polyreaction
Above-mentioned reaction mixture is proceeded to and is full of nitrogen and has been warming up in the reactor of 220 DEG C ~ 240 DEG C, start to stir with the stirring velocity of 50 ~ 70 turns/min, constant temperature strengthens stirring velocity to 70 ~ 90 turn/min after 0.5 ~ 1.0 hour, add 3,4'-dihalo-benzophenone, continue constant temperature and within 0.5 ~ 1.0 hour, arrive setting viscosity, obtain polymerization mucus; Wherein, the monomer molar number sum of 4,4'-dichloro diphenyl sulfone, 4,4'-dihalo-benzophenone and 3,4'-dihalo-benzophenone is identical with 4,4'-'-biphenyl diphenol mole number;
Wherein, be 35 ~ 45% at the solid content of polymerization stage system;
(3) aftertreatment
After stopped reaction, polymkeric substance mucus is ground into powder through water cooling, filters and obtain containing polymkeric substance, water-soluble solvent and salt; And then the powder containing polymkeric substance is removed desolventizing and salt with deionized water boiling washing again, drier, namely obtain multiple copolymer.
Described 4,4'-dihalo-benzophenone are contraposition aromatic ketone monomer, and its structural formula is
wherein, X=F or Cl, Y=F or Cl, be specially 4,4'-difluoro benzophenone, 4,4'-dichloro benzophenones or 4-chloro-4'-fluorine benzophenone.
Described 3,4'-dihalo-benzophenone are aromatic ketone monomer in position between isomery, and its structural formula is
, wherein, X=F or Cl, Y=F or Cl, be specially 3-fluoro-4'-fluorine benzophenone, 3-chloro-4'-chlorobenzophenone, 3-fluoro-4'-chlorobenzophenone or 3-chloro-4'-fluorine benzophenone.
Described non-proton strong polar organic solvent is tetramethylene sulfone, sulfobenzide, dimethyl sulfoxide (DMSO), N,N-dimethylacetamide or N-Methyl pyrrolidone, preferred tetramethylene sulfone.
Described alkaline carbonate salt forming agent is Na
2cO
3or K
2cO
3or the mixture of its different ratios, preferred domestic Na
2cO
3.
Described point of aqua, containing the aromatic hydrocarbon derivative of alkyl, comprises a kind of or this several mixture in toluene, dimethylbenzene, trimethylbenzene, durene, ethylbenzene, p-Diethylbenzene, partially diethylbenzene.Described point of aqua preferably 160 ° of C< boiling point <, 200 ° of C and density is less than hypotoxicity organic point of aqua of water, is specially the mixture of one or more in sym-trimethylbenzene, hemimellitol, a trimethylbenzene, p-Diethylbenzene, partially diethylbenzene or durene.Adopt high boiling point of aqua, reaction heat-up rate, obviously faster than adopting lower boiling dimethylbenzene to be the heat-up rate of point aqua, can shorten 1 ~ 2 hour reaction time single batch in the industrial production, reducing production energy consumption, reduction material local temperature.
The present invention is in 200 ~ 210 ° of C at salt-forming stage system temperature, completes prepolymerisation stage simultaneously, namely forms low-molecular-weight performed polymer at salt-forming stage, the number of performed polymer molecular chain and the concentration residing for monomer directly related.Along with the increase pre-polymerization scale of construction of monomer concentration increases, when performed polymer is increased to the monomer concentration step-down to a certain degree in system, later stage polymerization velocity is caused to weaken, there is the phenomenon that the too high speed of response of solid content is slack-off on the contrary, therefore, the present invention is preferred, controls to be 20% ~ 25% at salt-forming reaction stage system solid content, control to be 35 ~ 45% at polymerization stage system solid content, thus ensure the concentration of polymerization stage monomer.Polymerization stage high solids content is conducive to polyreaction, greatly can reduce the consumption of crucial solvent sulfolane, reduces energy consumption, cost-saving.
The present invention compared with prior art, has following beneficial effect:
1) the invention provides one and introduce aromatic ketone monomer in PPSU polymkeric substance, especially isomery aromatic ketone monomer copolymerization, aromatic ketone monomer accounts for 10 ~ 25% of fragrant sulfone monomer molar total amount, containing polyether sulphone and polyaryletherketone random copolymerization structure on the polyphenylene ether sulfone ketone resin molecular backbone chain prepared, wherein
group with
the mol ratio of group is between 5 ~ 9:1, and the fusing point of resulting product is between 305 ~ 340 DEG C, and its machine-shaping temperature is not usually higher than 350 DEG C; Melting index, between 28.0 ~ 36g/10min, has higher mobility, is easy to processing, can be widely used in various thin-gage goods;
2) the present invention is by being controlled to the solid content of salt phase and polymerization stage, greatly can reduce the consumption of crucial solvent sulfolane,
Improve production capacity nearly 1/3rd.In 40% solid content, often producing 1 ton of polyaryl ether sulphone resin only needs, with tetramethylene sulfone 1.5 tons, by the rate of recovery of tetramethylene sulfone 80%, directly to lose 300KG tetramethylene sulfone less, greatly saved cost compared with 25% solid content technique;
3) present invention process adopts the pattern of two still series connection, after salify completes, proceeds to polymeric kettle again after steaming whole point aquas,
The production cycle of the technique of producing stage by stage and the system production cycle of 25% solid content basically identical, two still tandem process can improve production capacity one times, can realize production capacity maximize;
4) the present invention adopts high boiling point of aqua energy Reaction time shorten, improves production capacity;
5) salt forming agent of the present invention adopts the Na that is produced from China's Mainland
2cO
3, save purchase cost; In addition excessive Na
2cO
3be present in the form of a powder in system, hydrolyzed alkaline is obviously than KOH, NaOH and K
2cO
3system is low, weak to the toxic side effect of system, and adopts domestic Na
2cO
3the polyether sulphone product of explained hereafter and use import Na
2cO
3the product produced for salt forming agent is distinguished without color and luster;
6) polymkeric substance prepared by the present invention has excellent solvent resistance energy, expands product applications, is especially applicable to application
In various petrochemicals; Polymkeric substance prepared by the present invention also has excellent resistance to x radiation x performance, can be widely used in medicine equipment goods and food, health rank goods; Polymkeric substance prepared by the present invention has excellent impact resistance and high-temperature behavior, can be applicable to motor car engine periphery goods, is particularly useful for automobile oil pipe.
Embodiment
Further illustrate the present invention below by embodiment, following examples are the concrete embodiment of the present invention, but embodiments of the present invention are by the restriction of following embodiment.
Embodiment 1
In 300 liters of stainless steel cauldrons that logical nitrogen tube and condensation water trap and high-efficiency stirrer are housed, start stirring after first adding 75.00 KG tetramethylene sulfone and be warming up to 80 DEG C, add 31.5 KG 4 in turn, 4'-dichloro diphenyl sulfone, 2.5KG 4, 4'-difluoro benzophenone, 22.50 KG 4, 4'-'-biphenyl diphenol, after monomer all dissolves, in system, 14.0 KG sodium carbonate are added again when being warming up to 100 DEG C, add 60.0 liters of durenes subsequently, 200 DEG C are warming up under continuing stirring, salt-forming reaction starts, the water generated in system and durene azeotropic, start have water coolant to drip in prolong, layering in water trap, treating to become clarification from muddiness by upper strata durene, to continue backflow 20 minutes more complete to ensure salt-forming reaction, salt-forming stage 1 hour, the system solid content in salt-forming reaction stage is 25%, whole durene is steamed after salify completes, be warming up to 230 DEG C again, squeeze into and utilize purity nitrogen to replace in advance and with in be warming up to 230 DEG C 200 liters of stainless steel cauldrons, start to stir with the stirring velocity of per minute 60 turns, constant temperature adds 160.0g 3,4'-difluoro benzophenone after 1.0 hours, strengthen stirring velocity to per minute 80 turns, continue constant temperature and within 0.5 ~ 1.0 hour, arrive setting viscosity, obtain polymerization mucus, the system solid content of polymerization stage is 35%, to be polymerized mucus directly to pulverize after film forming cooling on Stainless Steel Band water cooler, then the powder after filtering is added new deionized water and boils 1 hour, 8 ~ 10 times so repeatedly, in water, chloride ion content is till below 5ppm.By filter after polymkeric substance vacuum-drying to moisture weight content lower than 0.5%, obtain polyphenylene ether sulfone ketone (PPSUK) virgin resin.
Gained PPSUK resin melting index M I=28.5 g/10min (350.0 DEG C, 5KG).
Fusing point is: 319 DEG C
Embodiment 2
With embodiment 1, the amount being 29.75KG and 4,4'-difluoro benzophenone except the amount adding 4,4'-dichloro diphenyl sulfone is 3.75KG, and p-Diethylbenzene replaces durene, and the system solid content of polymerization stage is 40%, and other conditions are identical.
Gained PPSUK resin melting index M I=36.2 g/10min (350.0 DEG C, 5KG);
Fusing point is: 315 DEG C
Embodiment 3
With embodiment 1, except the amount adding 4,4'-dichloro diphenyl sulfone is 29.75KG and 4, the amount of 4'-difluoro benzophenone is 3.65KG, the amount of 3,4'-difluoro benzophenones is 260.0 g, and inclined diethylbenzene replaces outside durene, the system solid content of polymerization stage is 38%, and other conditions are identical.
Gained PPSUK resin melting index M I=36.0 g/10min (350.0 DEG C, 5KG);
Fusing point is: 315 DEG C
Embodiment 4
With embodiment 1, the amount except 4,4'-dichloro diphenyl sulfone is that the amount of 28.0KG and 4,4'-difluoro benzophenone is 5.0KG, the amount of 3,4 ￠-difluoro benzophenone is outside 400.0 g, and the system solid content of polymerization stage is 40%, and other conditions are identical.
Gained PPSUK resin melting index M I=32.2 g/10min (350.0 DEG C, 5KG).
Fusing point is: 310 DEG C
Embodiment 5
With embodiment 1, the amount except 4,4'-dichloro diphenyl sulfone is that the amount of 28.0KG and 4,4'-difluoro benzophenone is 5.0KG, the amount of 3,4'-difluoro benzophenones is outside 300.0 g, and the system solid content of polymerization stage is 39%, and other conditions are identical.
Gained PPSUK resin melting index M I=32.0 g/10min (350.0 DEG C, 5KG).
Fusing point is: 310 DEG C.
Claims (11)
1. a high-flow polyphenylene ether sulfone ketone resin, its structural formula is
Wherein Ar representative;
Wherein a:(b+c)=5 ~ 9:1,0<c≤0.1b.
2. high-flow polyphenylene ether sulfone ketone resin according to claim 1, it is characterized in that, 0.75<a<0.9,0.1<b<0.25,0<c<0.05.
3. the industrialized producing technology of the high-flow polyphenylene ether sulfone ketone resin described in any one of claim 1 ~ 2, is characterized in that, comprise the following steps:
(1) salt-forming reaction
With 4, 4'-'-biphenyl diphenol, 4, 4'-dichloro diphenyl sulfone, 4, 4'-dihalo-benzophenone and 3, 4'-dihalo-benzophenone is reaction monomers, in the reactor of nitrogen filled protection, 4 are added in turn in non-proton intensive polar solvent, 4'-'-biphenyl diphenol, 4, 4'-dichloro diphenyl sulfone, 4, 4'-dihalo-benzophenone, and start stirring heating, after temperature reaches 65 ~ 80 DEG C, continue to be stirred to after monomer all dissolves, be warmed up to 100 DEG C again to add in system than added 4, the alkaline carbonate salt forming agent of 4'-'-biphenyl diphenol mole number excessive 5 ~ 20%, and add a point aqua subsequently, under agitation continue to heat up, system starts salt-forming reaction, temperature controls between 190 ~ 220 DEG C, after system aquifer yield reaches theoretical value, discharge water and point aqua, again system is increased the temperature between 230 ~ 240 DEG C, be 20% ~ 25% at the solid content of salt-forming reaction stage system,
(2) polyreaction
The reaction mixture of step (1) is proceeded to and is full of nitrogen and has been warming up in the reactor of 220 DEG C ~ 240 DEG C, start to stir with the stirring velocity of 50 ~ 70 turns/min, constant temperature strengthens stirring velocity to 70 ~ 90 turn/min after 0.5 ~ 1.0 hour, add 3,4'-dihalo-benzophenone, continue constant temperature and within 0.5 ~ 1.0 hour, arrive setting viscosity, obtain polymerization mucus; Wherein, the monomer molar number sum of 4,4'-dichloro diphenyl sulfone, 4,4'-dihalo-benzophenone and 3,4'-dihalo-benzophenone is identical with 4,4'-'-biphenyl diphenol mole number;
Wherein, be 35 ~ 45% at the solid content of polymerization stage system;
(3) aftertreatment
After stopped reaction, polymkeric substance mucus is ground into powder through water cooling, filters and obtain containing polymkeric substance, water-soluble solvent and salt; And then the powder containing polymkeric substance is removed desolventizing and salt with deionized water boiling washing again, drier, namely obtain multiple copolymer.
4. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 3, is characterized in that, described 4,4'-dihalo-benzophenone are 4,4'-difluoro benzophenone, 4,4'-dichloro benzophenones or 4-chloro-4'-fluorine benzophenone.
5. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 3, it is characterized in that, described 3,4'-dihalo-benzophenone are 3-fluoro-4'-fluorine benzophenone, 3-chloro-4'-chlorobenzophenone, 3-fluoro-4'-chlorobenzophenone or 3-chloro-4'-fluorine benzophenone.
6. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 3, it is characterized in that, described non-proton strong polar organic solvent is tetramethylene sulfone, sulfobenzide, dimethyl sulfoxide (DMSO), N,N-dimethylacetamide or N-Methyl pyrrolidone.
7. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 6, is characterized in that, described non-proton strong polar organic solvent is tetramethylene sulfone.
8. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 3, is characterized in that, described alkaline carbonate salt forming agent is Na
2cO
3or K
2cO
3or the mixture of its different ratios.
9. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 8, is characterized in that, described alkaline carbonate salt forming agent is domestic Na
2cO
3.
10. the industrialized producing technology of high-flow polyphenylene ether sulfone ketone resin according to claim 3, is characterized in that, described point of aqua is the mixture of one or more comprised in toluene, dimethylbenzene, trimethylbenzene, durene, ethylbenzene or diethylbenzene.
The industrialized producing technology of 11. high-flow polyphenylene ether sulfone ketone resins according to claim 10, it is characterized in that, described point of aqua is 160 DEG C of < boiling point < 200 DEG C and density is less than hypotoxicity organic point of aqua of water, is specially the mixture of one or more in hemimellitol, a trimethylbenzene, p-Diethylbenzene or durene.
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| CN104497300A (en) * | 2014-12-17 | 2015-04-08 | 江门市优巨新材料有限公司 | High-liquidity poly(phenylene ether sulfone ketone) resin and preparation method thereof |
| CN104497301A (en) * | 2014-12-17 | 2015-04-08 | 江门市优巨新材料有限公司 | High-fluidity polysulfone ketone resin and production process thereof |
| JP2023553775A (en) * | 2020-08-24 | 2023-12-26 | ビーエーエスエフ ソシエタス・ヨーロピア | polyphenylene sulfone |
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| CN101544760A (en) * | 2009-04-28 | 2009-09-30 | 吉林大学 | Random copolymer containing biphenyl structural polyether sulfone and polyether ketone sulfone and preparation method thereof |
| CN101701067A (en) * | 2009-11-18 | 2010-05-05 | 吉林大学 | Tetramethyl-diphenol type polyarylether ketone (polyarylether sulphone) containing bromine at phenmethyl position and preparation method thereof |
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| CN101544760A (en) * | 2009-04-28 | 2009-09-30 | 吉林大学 | Random copolymer containing biphenyl structural polyether sulfone and polyether ketone sulfone and preparation method thereof |
| CN101701067A (en) * | 2009-11-18 | 2010-05-05 | 吉林大学 | Tetramethyl-diphenol type polyarylether ketone (polyarylether sulphone) containing bromine at phenmethyl position and preparation method thereof |
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