CN1480478A - Method for preparing polyether ester elastomer in blow molding grade - Google Patents
Method for preparing polyether ester elastomer in blow molding grade Download PDFInfo
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- CN1480478A CN1480478A CNA021322775A CN02132277A CN1480478A CN 1480478 A CN1480478 A CN 1480478A CN A021322775 A CNA021322775 A CN A021322775A CN 02132277 A CN02132277 A CN 02132277A CN 1480478 A CN1480478 A CN 1480478A
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- polyether ester
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Abstract
A process for preparing the blow moulding class polyether ester elastomer includes fusion polycondensating to obtain polyether ester elastomer, adding polyisocyanate and epoxy resin, and dual-screen reaction and extruding-out. The resultant elastomer has smooth surface and low strength index and fusion index less than 3 for its molten body.
Description
Technical field
The present invention relates to a kind of method for preparing polyether ester elastomer in blow molding grade.
Background technology
Linear thermoplastic polyether ester elastomer is got by di-carboxylic acid, dibasic alcohol and polyalkylene ether glycols copolymerization, and its shore hardness scope 30-75D has filled up the neutral gear between plastics and the rubber well.As a kind of engineering level elastomerics, have good physics and mechanical property, as toughness, fatigue resistance, high strength, wear resistance, oil-proofness and resistance to chlorine, therefore consumption constantly increases in recent years.
But the melt strength of polyester elastomer is lower, and the elastomerics of high rigidity especially can't satisfy melting index and melt strength index less than 3 blowing requirement.Therefore people have taked many methods improving the melt strength of polyether ester, as with the ionic polymer blend, react and extrude with Resins, epoxy/phenol sodium system, extrude etc. with the polycarbodiimide reaction.
But aforesaid method all has big defective, and the addition of ionic polymer can not be too big, otherwise easily phase-splitting, mis-behave; React and extrude with Resins, epoxy/phenol sodium system, though can improve melt strength preferably, product surface is very coarse; Comparatively speaking, extruding with the polycarbodiimide reaction is pretty good selection, but the synthetic very difficulty of polycarbodiimide.
The present inventor in view of the above problems, find after deliberation, in polyester elastomer, add 1) vulcabond of 0.3-5 part, 2) Resins, epoxy of 0.3-5 part, extrude by the twin screw reaction, can obtain the blowing level polyester elastomer of smooth surface, high fondant-strength.
Summary of the invention
The objective of the invention is to by add vulcabond and Resins, epoxy in polyester elastomer, the method for using the twin screw reaction to extrude is to obtain the blowing level polyester elastomer of smooth surface, high fondant-strength.
According to a first aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that, this polyester elastomer is by di-carboxylic acid, dibasic alcohol, polyalkylene ether dibasic alcohol melt phase polycondensation and get, and extrude by the twin screw reaction with an amount of polyisocyanates and Resins, epoxy, obtain the blowing level polyester elastomer of high fondant-strength.
According to a second aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that, wherein said thermoplastic polyether ester elastomer contains hard section of the polyester that the repetition short-chain ester units that accounts for polyether ester gross weight 20-90% forms.Described short-chain ester units can be represented by following general formula (I):
To be molecular weight remove remaining divalent radical behind the dihydroxyl less than 250 dibasic alcohol to D in the formula; To be molecular weight remove remaining divalent radical behind the dicarboxyl less than 300 di-carboxylic acid to R.
According to a third aspect of the invention we, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that, wherein said thermoplastic polyether ester elastomer contains soft section of the polyether ester that the repetition long-chain ester units that accounts for polyether ester gross weight 10-80% forms.Described long-chain ester units can be represented by general formula (II):
R is remaining divalent radical after molecular weight is removed dicarboxyl less than 300 di-carboxylic acid in the formula.G is remaining divalent radical after the polyalkylene ether glycol is removed dihydroxyl.
According to a forth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described di-carboxylic acid is an aromatic binary carboxylic acid.
According to a fifth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described aromatic binary carboxylic acid is terephthalic acid and derivative thereof.
According to a sixth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described terephthalic acid and derivative thereof account for more than 80% of total carboxylic acid's content.
According to a seventh aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described dibasic alcohol carbonatoms is between 2-8.
According to an eighth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that, 1,4 butyleneglycol accounts for 80 moles of total dibasic alcohol more than the % in the described dibasic alcohol.
According to a ninth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described alkylene ether dibasic alcohol molecular weight is preferably 1000-4000 between 400-6000.
According to the tenth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described polyisocyanates is a ditan-4,4 '-vulcabond (MDI).
According to an eleventh aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described polyisocyanates is the MDI (liquefied mdi) of carbodiimide modification.
According to a twelfth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described polyisocyanates is poly methylene poly phenyl poly isocyanate (PAPI).
According to a thirteenth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that the addition of described polyisocyanates is 0.3-5 part.
According to a fourteenth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described Resins, epoxy is bisphenol A type epoxy resin.
According to a fifteenth aspect of the invention, method for preparing polyether ester elastomer in blow molding grade of the present invention is characterised in that described Resins, epoxy addition is 0.3-5 part.
Embodiment
Thermoplastic polyether ester elastomer of the present invention contains the hard section of polyester that the repetition short-chain ester units forms and repeats soft section of the polyether ester that long-chain ester units forms, and both connect by ester bond.
Described short-chain ester units can be represented by following general formula (I):
And described long-chain ester units can be represented by general formula (II):
Wherein: D is remaining divalent radical after molecular weight is removed dihydroxyl less than 250 dibasic alcohol; R is remaining divalent radical after molecular weight is removed dicarboxyl less than 300 dicarboxylic acid; G is remaining divalent radical after the polyalkylene ether glycol is removed dihydroxyl, and molecular weight is between 400-6000.
In this polyether ester, by hard section 20 ~ 90wt% that accounts for the polyether ester gross weight of polyester that above-mentioned general formula (I) is formed, all the other are made up of for soft section the long-chain polyether ester of general formula (II).If the shared ratio of the hard section of short chain polyester is below 20%, and it is very low that the fusing point of polyester elastomer and intensity can become, and has no value for use.
The short-chain ester units of above-mentioned general formula (I) means that molecular weight is lower than the resultant of reaction that 250 dibasic alcohol and molecular weight are lower than 300 dicarboxylic acid.In the low molecular weight diol, 1, the 4-butyleneglycol must account for more than the 80mol%, and remaining 20mol% comprises can react aliphatics, the alicyclic and aromatic dihydroxy compound that forms short-chain ester units, wherein again with C
2-C
8Dibasic alcohol is good.Ethylene glycol, 1 for example, ammediol, 1,3-isobutyl glycol, 1,5-pentanediol, 2,2-dimethyl propylene glycol, 1,6-hexylene glycol, 1,4-dihydroxyl hexanaphthene, 1,4-cyclohexyl dimethanol etc.Most preferably be C
2-C
8Aliphatic dihydroxy alcohol.
The long-chain ester units of above-mentioned general formula (II) means that polyalkylene ether glycols and molecular weight are lower than the resultant of reaction of 300 dicarboxylic acid.Described polyalkylene ether glycols, can select to use polyethylene oxide glycol, poly-1,2 epoxy prapane glycol, poly-1 glycol, polytetrahydrofuran diol, or above-mentioned several multipolymer, and polybutadiene diol, Polybutadiene-acrylonitrile glycol etc.The number-average molecular weight of polyalkylene ether glycols must be between 400 ~ 6000 among the present invention, if number-average molecular weight less than 400, easily forms homopolymer but not segmented copolymer during polymerization, make elastomeric poor flexibility, physical strength lower.If number-average molecular weight greater than 6000, can produce during polymerization be separated, melt is white in color, and the difficult segmented copolymer that generates also can cause elastomer performance not good.Therefore the molecular weight of polyalkylene ether glycols is preferably 1000-4000.
React to form the dicarboxylic acid of polyester elastomer of the present invention with above-mentioned low molecular weight diol and polyalkylene ether glycols, can be aromatic series, aliphatics or alicyclic dicarboxylic acid, also comprise the dicarboxylic acid derivatives that can form the ester chain at this dicarboxylic acid.The available aromatics comprises: terephthalic acid, m-phthalic acid, phthalic acid, 2,6-naphthalic acid, 2,7-naphthalic acid and ester class thereof.The available non-aromatic compounds can be oxalic acid, propanedioic acid, Succinic Acid, pentanedioic acid, hexanodioic acid, nonane diacid, 1,3-cyclohexane dicarboxylic acid, 1,4-cyclohexane dicarboxylic acid etc.Terephthalic acid and ester class thereof must account for more than 80% of dicarboxylic acid total mole number in the present invention.
Polyester elastomer of the present invention can prepare with traditional transesterification reaction.Preferable methods is that the 4-butyleneglycol is heated to 150 ~ 270 ℃ of reactions in the presence of catalyzer, will react the methyl alcohol that generates simultaneously and promptly get prepolymer with dimethyl terephthalate (DMT), polyalkylene ether glycols and excessive 1.The gained prepolymer further distilled remove excessively 1, behind the 4-butyleneglycol, the reaction appropriate time promptly gets polyester elastomer.
For shortening the reaction times, avoid polymkeric substance in hot environment, to overstay and thermal destruction takes place, can in reaction, add suitable catalyzer,, reach alkoxide lithium, alkoxide magnesium etc. as the mixture of organic titanate, inorganic titanate, calcium acetate and antimonous oxide.
Hindered phenol or hindered amine oxidation inhibitor if can be in polyether ester, added, the thermal stability of product can be improved effectively.The addition of oxidation inhibitor is 0.05-2%, is preferably 0.1-1.5%.If addition is less than 0.05%, DeGrain; If addition is greater than 2%, the flexibility decrease of product, cost increases.
Available polyisocyanates of the present invention can be tolylene diisocyanate (TDI), ditan-4,4 '-vulcabond (MDI), liquefied mdi, poly methylene poly phenyl poly isocyanate (PAPI), 1, hexamethylene-diisocyanate (HDI), isophorone diisocyanate (IPDI), naphthalene diisocyanate (NDI), phenylene diisocyanate (XDI) etc., consider thermostability, reactive behavior and the source complexity of raw material, the present invention's preferred ditan-4,4 '-vulcabond (MDI), liquefied mdi, poly methylene poly phenyl poly isocyanate (PAPI).
Available Resins, epoxy has glycidyl ether type, glycidyl ester type, glycidic amine type, aliphatic epoxy and alicyclic epoxy etc., the preferred dihydroxyphenyl propane glycidyl ether of the present invention type epoxy.
Embodiment
Following illustrated embodiment is of the present invention specifying, and does not limit invention scope of the present invention.Each reactant of embodiment and the employed umber of additive are all parts by weight, and the following method of the performance of polyester elastomer is measured:
Tensile strength, elongation are pressed the GB/T528-92 standard test; Hardness is pressed the GB/T531-92 standard test; Melting index is pressed the GB3682-83 standard test.
Melt strength index (MSI) was tested on the instrument as follows in molten the finger:
Synthesizing of the elution time polyester elastomer of elution time/the second of first 10cm of a MSI=10cm:
In the 10L polymeric kettle, add 1405.3 parts of dimethyl terephthalate (DMT), 1,977.9 parts of 4-butyleneglycols, molecular weight are 993.8 parts of 1000 PTMG, 5 parts of antioxidant 1010s, 4.5 parts of tetrabutyl titanates.Open stirring, be warming up to 160 ~ 220 ℃ gradually, the fractional column temperature is set at 65 ℃, treats that the methyl alcohol quantity of distillate reaches 90% of theoretical amount, can think that transesterification reaction finishes.The still temperature is risen to 240 ~ 280 ℃ gradually, and in 1 hour the still internal pressure is reduced to below the 1mmHg, power of agitator reaches discharging after the maximum value.Comparative example 1:
Polyester elastomer is squeezed one time screw speed 100rpm, temperature 210-240 ℃, pelletizing, drying in twin screw.
Embodiment 1:
100 parts of elastomericss add 3 parts of MDI and react and extrude, and condition is with comparative example 1.
Embodiment 2:
100 parts of elastomericss add 3 parts of liquefied mdis and react and extrude, and condition is with comparative example 1.
Embodiment 3:
100 parts of elastomericss add 3 parts of PAPI and react and extrude, and condition is with comparative example 1.
Embodiment 4:
100 parts of elastomericss add 10 part of 618 epoxy and react and extrude, and condition is with comparative example 1.
Embodiment 5:
100 parts of elastomericss add 2 part of 618 epoxy, and 1.5 parts of liquefied mdis react and extrude, and condition is with comparative example 1.Experimental result sees Table 1.
Table 1
| Project | Comparative example 1 | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 |
| Shore hardness (D) | ????55 | ????55 | ????55 | ????55 | ????55 | ????55 |
| Tensile strength (MPa) | ????28 | ????31 | ????31 | ????32 | ????27 | ????34 |
| Extension at break (%) | ????550 | ????500 | ????500 | ????500 | ????450 | ????480 |
| Melting index (g/10min) | ????30 | ????2.8 | ????2.0 | ????1.8 | ????28 | ????1.8 |
| The melt strength index | ????12 | ????2.7 | ????2.5 | ????1.9 | ????13 | ????2.0 |
| The spline surfaces situation | Smooth | Bubble | Bubble | Bubble | Show slightly crude | Smooth |
As seen from Table 1, select polyisocyanates and epoxy cpd for use, can obtain smooth surface, melting index and melt strength index are all less than the polyester elastomer of 3 blowing level.
Claims (11)
1. method for preparing polyether ester elastomer in blow molding grade, it is characterized in that, this polyester elastomer is by di-carboxylic acid, dibasic alcohol, polyalkylene ether dibasic alcohol melt phase polycondensation and get, and extrude by the twin screw reaction with an amount of polyisocyanates and Resins, epoxy, obtain the blowing level polyester elastomer of high fondant-strength.
2. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, wherein said thermoplastic polyether ester elastomer contains hard section of the polyester that the repetition short-chain ester units that accounts for polyether ester gross weight 20-90% forms.Described short-chain ester units can be represented by following general formula (I):
To be molecular weight remove remaining divalent radical behind the dihydroxyl less than 250 dibasic alcohol to D in the formula; To be molecular weight remove remaining divalent radical behind the dicarboxyl less than 300 di-carboxylic acid to R.
3. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, wherein said thermoplastic polyether ester elastomer contains soft section of the polyether ester that the repetition long-chain ester units that accounts for polyether ester gross weight 10-80% forms.Described long-chain ester units can be represented by general formula (II):
R is remaining divalent radical after molecular weight is removed dicarboxyl less than 300 di-carboxylic acid in the formula.G is remaining divalent radical after the polyalkylene ether glycol is removed dihydroxyl.
4. method for preparing polyether ester elastomer in blow molding grade according to claim 1, it is characterized in that, described di-carboxylic acid is an aromatic binary carboxylic acid, and described aromatic binary carboxylic acid is terephthalic acid and derivative thereof, and described terephthalic acid and derivative thereof account for more than 80% of total carboxylic acid's content.
5. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, in the described dibasic alcohol, carbonatoms is between 2-8, and 1,4 butyleneglycol accounts for 80 moles of total dibasic alcohol more than the %.
6. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, described alkylene ether dibasic alcohol molecular weight is preferably 1000-4000 between 400-6000.
7. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, described polyisocyanates is a ditan-4,4 '-vulcabond (MDI).
8. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, described polyisocyanates is the MDI (liquefied mdi) of carbodiimide modification.
9. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, described polyisocyanates is poly methylene poly phenyl poly isocyanate (PAPI).
10. according to claim 1,7,8 or 9 described method for preparing polyether ester elastomer in blow molding grade is characterized in that, the addition of described polyisocyanates is 0.3-5 part.
11. method for preparing polyether ester elastomer in blow molding grade according to claim 1 is characterized in that, described Resins, epoxy is bisphenol A type epoxy resin, and described Resins, epoxy addition is 0.3-5 part.
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013060089A1 (en) * | 2011-10-27 | 2013-05-02 | 山东东大一诺威聚氨酯有限公司 | Polyether-ester polyol and usage thereof |
| CN103642017A (en) * | 2013-11-04 | 2014-03-19 | 金发科技股份有限公司 | Polyester elastomer for blow molding and preparation method thereof |
| CN103788584A (en) * | 2013-12-31 | 2014-05-14 | 金发科技股份有限公司 | Thermoplastic polyether ester elastomer composition as well as preparation method and application thereof |
| CN103788585A (en) * | 2013-12-31 | 2014-05-14 | 金发科技股份有限公司 | Thermoplastic polyether ester elastomer composition as well as preparation method and application thereof |
| CN105175925A (en) * | 2015-10-27 | 2015-12-23 | 上海锦湖日丽塑料有限公司 | Ultrahigh melt strength blow-molded ABS resin composition and preparation method thereof |
| CN105732967A (en) * | 2016-03-07 | 2016-07-06 | 美瑞新材料股份有限公司 | Method for preparing thermoplastic copolyester elastomer by using chain extension method |
| CN109111725A (en) * | 2018-07-20 | 2019-01-01 | 滁州市玉林聚氨酯有限公司 | A kind of preparation method of elastane |
| CN112724348A (en) * | 2020-12-28 | 2021-04-30 | 会通新材料(上海)有限公司 | Heat-resistant high-viscosity polyether ester elastomer composition and preparation method thereof |
| CN113621132A (en) * | 2021-07-22 | 2021-11-09 | 会通新材料(上海)有限公司 | High-melt-strength low-melt-index thermoplastic polyester elastomer and preparation method thereof |
-
2002
- 2002-09-04 CN CN 02132277 patent/CN1281658C/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013060089A1 (en) * | 2011-10-27 | 2013-05-02 | 山东东大一诺威聚氨酯有限公司 | Polyether-ester polyol and usage thereof |
| CN103642017A (en) * | 2013-11-04 | 2014-03-19 | 金发科技股份有限公司 | Polyester elastomer for blow molding and preparation method thereof |
| CN103642017B (en) * | 2013-11-04 | 2016-03-30 | 金发科技股份有限公司 | A kind of blowing polyester elastomer and preparation method thereof |
| CN103788585B (en) * | 2013-12-31 | 2016-08-17 | 金发科技股份有限公司 | A kind of thermoplastic polyether ester elastomer compositions and its preparation method and application |
| CN103788584A (en) * | 2013-12-31 | 2014-05-14 | 金发科技股份有限公司 | Thermoplastic polyether ester elastomer composition as well as preparation method and application thereof |
| CN103788585A (en) * | 2013-12-31 | 2014-05-14 | 金发科技股份有限公司 | Thermoplastic polyether ester elastomer composition as well as preparation method and application thereof |
| CN103788584B (en) * | 2013-12-31 | 2016-08-17 | 金发科技股份有限公司 | A kind of thermoplastic polyether ester elastomer compositions and its preparation method and application |
| CN105175925B (en) * | 2015-10-27 | 2018-01-26 | 上海锦湖日丽塑料有限公司 | A kind of superelevation melt strength blowing ABS resin composition and preparation method thereof |
| CN105175925A (en) * | 2015-10-27 | 2015-12-23 | 上海锦湖日丽塑料有限公司 | Ultrahigh melt strength blow-molded ABS resin composition and preparation method thereof |
| CN105732967A (en) * | 2016-03-07 | 2016-07-06 | 美瑞新材料股份有限公司 | Method for preparing thermoplastic copolyester elastomer by using chain extension method |
| CN109111725A (en) * | 2018-07-20 | 2019-01-01 | 滁州市玉林聚氨酯有限公司 | A kind of preparation method of elastane |
| CN112724348A (en) * | 2020-12-28 | 2021-04-30 | 会通新材料(上海)有限公司 | Heat-resistant high-viscosity polyether ester elastomer composition and preparation method thereof |
| CN113621132A (en) * | 2021-07-22 | 2021-11-09 | 会通新材料(上海)有限公司 | High-melt-strength low-melt-index thermoplastic polyester elastomer and preparation method thereof |
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