CS196011B1 - Process for the stabilization of phenolic monomers - Google Patents
Process for the stabilization of phenolic monomers Download PDFInfo
- Publication number
- CS196011B1 CS196011B1 CS582077A CS582077A CS196011B1 CS 196011 B1 CS196011 B1 CS 196011B1 CS 582077 A CS582077 A CS 582077A CS 582077 A CS582077 A CS 582077A CS 196011 B1 CS196011 B1 CS 196011B1
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- CS
- Czechoslovakia
- Prior art keywords
- phosphite
- stabilization
- phenolic monomers
- oxidative
- thermo
- Prior art date
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- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 title claims description 8
- 239000000178 monomer Substances 0.000 title claims description 6
- 238000000034 method Methods 0.000 title claims description 3
- 230000006641 stabilisation Effects 0.000 title description 2
- 238000011105 stabilization Methods 0.000 title description 2
- NXXYKOUNUYWIHA-UHFFFAOYSA-N 2,6-Dimethylphenol Chemical compound CC1=CC=CC(C)=C1O NXXYKOUNUYWIHA-UHFFFAOYSA-N 0.000 claims description 10
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 230000000087 stabilizing effect Effects 0.000 claims description 3
- 125000001424 substituent group Chemical group 0.000 claims description 3
- 230000032683 aging Effects 0.000 claims description 2
- 125000003118 aryl group Chemical group 0.000 claims description 2
- 125000005504 styryl group Chemical group 0.000 claims description 2
- CRSOQBOWXPBRES-UHFFFAOYSA-N neopentane Chemical compound CC(C)(C)C CRSOQBOWXPBRES-UHFFFAOYSA-N 0.000 claims 1
- 239000003381 stabilizer Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 239000004721 Polyphenylene oxide Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229920006380 polyphenylene oxide Polymers 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000001590 oxidative effect Effects 0.000 description 4
- 238000006068 polycondensation reaction Methods 0.000 description 4
- 238000002835 absorbance Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- AQSJGOWTSHOLKH-UHFFFAOYSA-N phosphite(3-) Chemical class [O-]P([O-])[O-] AQSJGOWTSHOLKH-UHFFFAOYSA-N 0.000 description 3
- -1 tetramethylene methane Chemical compound 0.000 description 3
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000007859 condensation product Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002903 organophosphorus compounds Chemical class 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 125000004151 quinonyl group Chemical group 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- HVLLSGMXQDNUAL-UHFFFAOYSA-N triphenyl phosphite Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)OC1=CC=CC=C1 HVLLSGMXQDNUAL-UHFFFAOYSA-N 0.000 description 2
- 150000003739 xylenols Chemical class 0.000 description 2
- YJTKZCDBKVTVBY-UHFFFAOYSA-N 1,3-Diphenylbenzene Chemical group C1=CC=CC=C1C1=CC=CC(C=2C=CC=CC=2)=C1 YJTKZCDBKVTVBY-UHFFFAOYSA-N 0.000 description 1
- ADRNSOYXKABLGT-UHFFFAOYSA-N 8-methylnonyl diphenyl phosphite Chemical compound C=1C=CC=CC=1OP(OCCCCCCCC(C)C)OC1=CC=CC=C1 ADRNSOYXKABLGT-UHFFFAOYSA-N 0.000 description 1
- FKFNTCXLGNGOCE-UHFFFAOYSA-N CCCCCCCCCC(C=CC=C1)=C1OP(C1=CC=CC=C1)(O)OC1=C(CCCCCCCCC)C=CC=C1 Chemical compound CCCCCCCCCC(C=CC=C1)=C1OP(C1=CC=CC=C1)(O)OC1=C(CCCCCCCCC)C=CC=C1 FKFNTCXLGNGOCE-UHFFFAOYSA-N 0.000 description 1
- 241000360590 Erythrites Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Substances C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- SXXILWLQSQDLDL-UHFFFAOYSA-N bis(8-methylnonyl) phenyl phosphite Chemical compound CC(C)CCCCCCCOP(OCCCCCCCC(C)C)OC1=CC=CC=C1 SXXILWLQSQDLDL-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- MPTQRFCYZCXJFQ-UHFFFAOYSA-L copper(II) chloride dihydrate Chemical compound O.O.[Cl-].[Cl-].[Cu+2] MPTQRFCYZCXJFQ-UHFFFAOYSA-L 0.000 description 1
- 150000001896 cresols Chemical class 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- UNXHWFMMPAWVPI-ZXZARUISSA-N erythritol Chemical compound OC[C@H](O)[C@H](O)CO UNXHWFMMPAWVPI-ZXZARUISSA-N 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920002852 poly(2,6-dimethyl-1,4-phenylene oxide) polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000004053 quinones Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000003385 ring cleavage reaction Methods 0.000 description 1
- 239000011885 synergistic combination Substances 0.000 description 1
- WGKLOLBTFWFKOD-UHFFFAOYSA-N tris(2-nonylphenyl) phosphite Chemical compound CCCCCCCCCC1=CC=CC=C1OP(OC=1C(=CC=CC=1)CCCCCCCCC)OC1=CC=CC=C1CCCCCCCCC WGKLOLBTFWFKOD-UHFFFAOYSA-N 0.000 description 1
- SBBXVZWBYVVVBN-UHFFFAOYSA-N tris[2-(2-phenylethenyl)phenyl] phosphite Chemical compound P(OC1=C(C=CC=C1)C=CC1=CC=CC=C1)(OC1=C(C=CC=C1)C=CC1=CC=CC=C1)OC1=C(C=CC=C1)C=CC1=CC=CC=C1 SBBXVZWBYVVVBN-UHFFFAOYSA-N 0.000 description 1
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- Compositions Of Macromolecular Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Vynález sé týká. stabilizace enolických monomerů, používaných zejména k přípravě polyfenylenoxidů oxidační polykondenzací.The invention relates. stabilization of enolic monomers, used in particular for the preparation of polyphenylene oxides by oxidative polycondensation.
Fenol, kresoly a xylenoly podléhají velmi snadno termooxidaci, urychlované přítomností kovu, například materiálu třídy 11 - ocel.Phenol, cresols and xylenols are very easily subject to thermooxidation, accelerated by the presence of metal, such as class 11 material - steel.
Výsledkem je tvorba barevných netěkavých oxidačně-kondenzačních produktů, jejichž množství s rostoucí teploto,u a délkou expozice rychle vzrůstá /až do jednotek procent/ a znehodnoeuje tím surovinu Často tak značně, že je třeba provádět před využitím opětovné čistění, například destilací, nebo je nutno volit speciální konstrukční materiály, které nejsou katalyzátory termooxidačníoh reakcí.The result is the formation of colored, non-volatile oxidation-condensation products, whose amount increases rapidly (up to one percent) with increasing temperature, and exposure time, and thus depreciates the raw material often so much that re-purification, for example by distillation, is necessary choose special construction materials which are not catalysts of thermo-oxidative reactions.
Nestálost fenolů je způsobena oxidační labilitou fenolické skupiny - OH. Vznikající fenoxyraikál je jednak schopen přenosovou reakcí poškodit substituenty, jednak vede k’ tvorbě chinonových struktur. Oxidační kondenzací, štěpením chinonového kruhu a dalšími reakcemi Vznikají polykonjugované produkty s molekulovou hmotností řádově 1θ\ Přítomnost chinonů je na závadu zejména při výrobě polyfenylenoxidů, kde tyto příměsi zhoršují podstatně mechanické vlastnosti produktu.Phenol instability is caused by the oxidative lability of the phenolic group - OH. The resulting phenoxyraical is capable of damaging substituents on the one hand and leads to the formation of quinone structures. Oxidative condensation, quinone ring cleavage and other reactions Polyconjugated products with molecular weights of the order of 1θ are formed. The presence of quinones is particularly detrimental in the production of polyphenylene oxides, where these impurities substantially impair the mechanical properties of the product.
Dosud není záámo technické řešení uvedeného problému. Oxidačně kondenzačním reakcím lze zpravidla zabránit přidáním vhodných stabilizátorů. U fenoliokých monomerů je volba stabilázátoru omezena podmínkou, že použitý stabilizátor nesmí zhoršovat žádoucí vlast196 011The technical solution to this problem is not yet desirable. Oxidation condensation reactions can generally be prevented by the addition of suitable stabilizers. For phenolocylene monomers, the choice of stabilizer is limited by the condition that the stabilizer used must not impair the desired homeland.
196 011 nosti monomeru a bránit průběhu oxidační polykondenzace.196 011 to prevent the course of oxidative polycondensation.
Bylo. zjištěno, že se žádoucího účinku dosáhne pomocí termooxidačních stabilizátorů na bázi organických sloučenin fosforu.It was. It has been found that the desired effect is obtained by means of thermo-oxidizing stabilizers based on organic phosphorus compounds.
Předmětem vynálezu je způsob stabilizace fenolických monomerů, jako je 2,6 dimetylfenol, proti termooxidačnímu stárnutí, při kterém se k fenolickému monomeru používá přídavku 0,1 až 5 % hmotnostních fosfitu obecného vzorceSUMMARY OF THE INVENTION The present invention provides a process for stabilizing phenolic monomers such as 2,6 dimethylphenol against thermo-oxidative aging by adding 0.1-5% by weight of a phosphite of the formula
kde n je 1 nebo 2, R^ je alkyl se 4 až 20 uhlíkovými atomy, aryl, popřípadě substituovaný p alkylem se 4 až 20 uhlíkovými atomy nebo styrylem, R značí dva navzájem stejné nebo různé substituenty R^ , kde R^ má shora uvedený význam, nebo tetrametylenmetan.wherein n is 1 or 2, R1 is alkyl of 4 to 20 carbon atoms, aryl optionally substituted with p alkyl of 4 to 20 carbon atoms or styryl, R is two mutually identical or different substituents R ^, wherein R ^ has the above or tetramethylene methane.
Fosfity se používají jako termooxidační stabilizátory pro plasty, většinou v synergických kombinacích se substituovanými fenoly, které samy o sobě jsou účinnými termooxidačními stabilizátory, zejména polyolefinů.Phosphites are used as thermo-oxidizing stabilizers for plastics, mostly in synergistic combinations with substituted phenols, which are themselves effective thermo-oxidizing stabilizers, especially polyolefins.
Bylo zjištěno, že při přidáni fosfitů do fenolických monomerů se podstatně sníží tvorba nežádoucích oxidačních produktů. Množství těchto produktů lze kvantifikovat spektroskopicky; vhodně lze charakterizovat stupeň poškozeni polymeru např. absorpčním pikem v oblasti 320 až 340 mm. Absorbance roztoku fenolu je pak úměrná množství ne těkavých kondenzačních produktů. Tímto způsobem lze vyhodnotit i účinnost termooxidačních stabilizátorů na bázi organických sloučenin fosforu na o±id9Ční polykondenzaci lze vyhodnotit i preparací polyfenylenoxidu za srovnatelných podmínek. Případné zbytky fosfitu v produktu nemohou být na závadu, protože tyto fosfity se používají jako stabilizační přísady do polyfenylenoxidu, kde jsou tyto zbytky žádoucí.It has been found that the formation of undesired oxidation products is substantially reduced when phosphites are added to phenolic monomers. The amount of these products can be quantified spectroscopically; suitably the degree of deterioration of the polymer can be characterized by, for example, an absorption peak in the region of 320 to 340 mm. The absorbance of the phenol solution is then proportional to the amount of non-volatile condensation products. In this way, the efficacy of thermo-oxidative stabilizers based on organic phosphorus compounds on polycondensation can also be evaluated by preparing polyphenylene oxide under comparable conditions. Possible phosphite residues in the product cannot be impeded, as these phosphites are used as stabilizing additives in polyphenylene oxide, where these residues are desirable.
Vynález objasní následující příklady, které však předmět vynálezu nijak neomezují. Přiklad 1The invention is illustrated by the following non-limiting examples. Example 1
Do taveniny 2,6-xylenolu byly přidány ocelové třísky a různé množství trifenyl90 styrylfosfitu. Směs byla po dobu 120 hodin vystavena teplotě 70 °C. Sledované změny barevnosti jsou uvedeny v tabulce:Steel chips and varying amounts of triphenyl 90 styrylphosphite were added to the 2,6-xylenol melt. The mixture was exposed to 70 ° C for 120 hours. Monitored color changes are listed in the table:
198 011198 011
Příklad 2 ml roztoku 15 g 2,6-xylenolu v azeotropní směsi etylalkohol-benzen /64:36 % objemových/ bylo dávkováno 20 minut do 100 ml roztoku 225 mg dihydrátu chloridu měánatého a 3 ml moříolinu v azeotropní směsi. Směs byla probublévána kyslíkem a reakce ukončena po 33 minutách od počátku dávkování. Vzniklý polymer byl filtrován a promyt azeotropní směsí a vysušen.Example 2 ml of a solution of 15 g of 2,6-xylenol in an azeotropic mixture of ethyl alcohol-benzene (64: 36% by volume) was metered into a 100 ml solution of 225 mg of copper (II) chloride dihydrate and 3 ml of morpholine in azeotropic mixture. The mixture was bubbled with oxygen and the reaction terminated 33 minutes after the start of dosing. The resulting polymer was filtered and washed with an azeotropic mixture and dried.
Produktem reakce bylo 13,5 g póly /2,6-dimetyl-l,4-fenylenoxidu/ o molekulové hmotnosti 51 000.The product of the reaction was 13.5 g of poly (2,6-dimethyl-1,4-phenylene oxide) having a molecular weight of 51,000.
Přiklad 3Example 3
Polymerace byla prováděna podle příkladu 2, do reakční směsi přidáno 0,75 g /5 %/ trifenylstyrylfosfitu. Produktem reakce bylo 13,2 g polyfenylenoxidu o molekulové hmotnosti 49 000. Přítomnost 5 % fosfitu neovlivnila polykondenzační reakci.The polymerization was carried out according to Example 2, and 0.75 g (5%) triphenylstyrylphosphite was added to the reaction mixture. The reaction product was 13.2 g of polyphenylene oxide having a molecular weight of 49,000. The presence of 5% phosphite did not affect the polycondensation reaction.
Přiklad 4Example 4
Podmínky bvly stejné jako v příkladu 1 a v množství 0,2 % a 3 % byly ke xylenolu přidány různé osfity. Následující tabulka ukazuje vliv těchto foefitů na relativní změny barevnosti 2,6-xylenolu.The conditions were the same as in Example 1 and in the amount of 0.2% and 3% various osphites were added to the xylenol. The following table shows the effect of these foefits on the relative color changes of 2,6-xylenol.
fosfit . · relativní změna absorbancephosphite. · Relative absorbance change
předmět vynálezuobject of the invention
Claims (1)
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Application Number | Priority Date | Filing Date | Title |
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CS582077A CS196011B1 (en) | 1977-09-07 | 1977-09-07 | Process for the stabilization of phenolic monomers |
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CS582077A CS196011B1 (en) | 1977-09-07 | 1977-09-07 | Process for the stabilization of phenolic monomers |
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CS196011B1 true CS196011B1 (en) | 1980-02-29 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2818257A1 (en) | 2013-06-27 | 2014-12-31 | Vladimir Zakaryan | Equipment for thermal decomposition of organic material and gas production used to generate heat and electricity |
-
1977
- 1977-09-07 CS CS582077A patent/CS196011B1/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2818257A1 (en) | 2013-06-27 | 2014-12-31 | Vladimir Zakaryan | Equipment for thermal decomposition of organic material and gas production used to generate heat and electricity |
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