CS229038B3 - Method of polymerizing and copolymerizing lactams of om - Google Patents
Method of polymerizing and copolymerizing lactams of om Download PDFInfo
- Publication number
- CS229038B3 CS229038B3 CS87583A CS87583A CS229038B3 CS 229038 B3 CS229038 B3 CS 229038B3 CS 87583 A CS87583 A CS 87583A CS 87583 A CS87583 A CS 87583A CS 229038 B3 CS229038 B3 CS 229038B3
- Authority
- CS
- Czechoslovakia
- Prior art keywords
- polymerization
- lactams
- initiated
- copolymerization
- copolymerizing
- Prior art date
Links
- 150000003951 lactams Chemical class 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims description 6
- 230000000379 polymerizing effect Effects 0.000 title 1
- 238000006116 polymerization reaction Methods 0.000 claims description 21
- 238000007334 copolymerization reaction Methods 0.000 claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 5
- 229940000488 arsenic acid Drugs 0.000 claims description 3
- DJHGAFSJWGLOIV-UHFFFAOYSA-N Arsenic acid Chemical compound O[As](O)(O)=O DJHGAFSJWGLOIV-UHFFFAOYSA-N 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 description 9
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000004952 Polyamide Substances 0.000 description 5
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 5
- 229920002647 polyamide Polymers 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000003301 hydrolyzing effect Effects 0.000 description 3
- 239000003999 initiator Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Substances OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000010538 cationic polymerization reaction Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- RLSSMJSEOOYNOY-UHFFFAOYSA-N m-cresol Chemical compound CC1=CC=CC(O)=C1 RLSSMJSEOOYNOY-UHFFFAOYSA-N 0.000 description 2
- -1 phosphoric acid compound Chemical class 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 102100026189 Beta-galactosidase Human genes 0.000 description 1
- 108010059881 Lactase Proteins 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 239000003708 ampul Substances 0.000 description 1
- 238000010539 anionic addition polymerization reaction Methods 0.000 description 1
- 230000000922 anti-bactericidal effect Effects 0.000 description 1
- YDLSUFFXJYEVHW-UHFFFAOYSA-N azonan-2-one Chemical compound O=C1CCCCCCCN1 YDLSUFFXJYEVHW-UHFFFAOYSA-N 0.000 description 1
- 108010005774 beta-Galactosidase Proteins 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 229940116108 lactase Drugs 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
Landscapes
- Polyamides (AREA)
Description
Vynólez se týká způsobu polymerace a kopolymerace laktamů omege-aminokyselin.The invention relates to a process for the polymerization and copolymerization of omege-amino acid lactams.
Polymeraci a kopolymeraci laktamů obecného vzorce fíH-ÍCHgJ^^-ÓO lze provádět několika postupy, které se liSí podle použitých kalatyzátorů mechanismem polymerace. Tzv. hydrolytické polymerace je katslyzovaná omega-eminokyselinami, vodou nebo látkami vodu uvolňujícími a trvá několik hodin až několik stovek hodin v závislosti na použitém laktamů, teplotě, koncentraci a typu katalyzátoru. Aniontová polymerace laktamů je naproti tomu katalyzována silnými bázemi a probíhá v přítomnosti aktivátorů s N-acyllaktamovou strukturou o několik řádů rychleji než hydrolytická polymerace, a to i při nízkých teplotách pod teplotou tání polymeru. Oba uvedené způsoby jsou technologicky využívány.The polymerization and copolymerization of the lactams of the general formula (H-CH3) -O-O can be carried out in several ways, which differ according to the polymerization mechanism used according to the catalysts used. Tzv. The hydrolytic polymerization is catalysed by omega-emino acids, water or water-releasing agents and lasts from several hours to several hundred hours depending on the lactams used, the temperature, the concentration and the type of catalyst. By contrast, anionic polymerization of lactams is catalyzed by strong bases and proceeds in the presence of activators with an N-acyllactam structure several orders of magnitude faster than hydrolytic polymerization, even at low temperatures below the melting point of the polymer. Both methods are used technologically.
Naproti tomu kationtová polymerace laktamů, katalyzované organickými nebo anorganickými kyselinami nebo jejich solemi s laktemy nenašla dosud technologické využití pro pomelou rychlost a složitý průběh jednotlivých fází reakce.In contrast, the cationic polymerization of lactams catalysed by organic or inorganic acids or their lactase salts has not yet found technological application for the slow speed and complexity of the individual phases of the reaction.
V současné době byly popsány nové iniciátory kationtové polymerace laktamů - ekvimolární sloučeniny bezvodé kyseliny fosforečné s laktamy .omege-aminokyselin obecného vzorce H^PO^ . Polymerace laktamů omege-aminokyselin, iniciované těmito sloučeninami, probíhá v závislosti ne typu laktamů, koncentraci iniciátoru a teplotě rychlostí stejnou nebo vyšší nežli hydrolytická polymerace, kromě toho část kyseliny fosforečné zůstává chemicky vázána v řetězci polyamidu a je nositelem některých zlepšených vlastností polymeru, např. snížení hořlavosti, zvýšení hydrofilnosti.Recently, novel initiators of cationic polymerization of lactams - equimolar anhydrous phosphoric acid compound with lactams of the homogeneous amino acids of the formula H 2 PO 4 have been described. The polymerization of omege-amino acid lactams initiated by these compounds, depending on the type of lactams, the initiator concentration and the temperature, is at a rate equal to or higher than the hydrolytic polymerization. In addition, a portion of phosphoric acid remains chemically bound in the polyamide reduced flammability, increased hydrophilicity.
Tento vynález nevazuje ne uvedené výsledky. Jeho podstatě spočívá v tom, že se pólymerece a kopolymerace laktamů iniciuje 0,1 ež 20 mol SK ekvimolární sloučeniny bezvodé kyseliny arseničné s laktamy omega-aminokyselin obecného vzorce H^AsO^ . ŇH-(CHg)x-fco, kde x je 3 až 11, podle če. autorského osvědčeni č. 227784 při teplotách 200 sž 330 °C.The present invention does not bind the above results. In essence, the polymerization and copolymerization of lactams is initiated with 0.1 to 20 moles SK of the equimolar anhydrous arsenic acid compound with the lactams of the omega-amino acids of the formula H 2 AsO 4. HH- (CHg) x -fco, where x is 3 to 11, according to Art. No. 227784 at temperatures of 200 to 330 ° C.
Účinek způsobu podle vynálezu spočívá v tom, že polymerece e kopolymerece laktamů iniciovaná sloučeninami probíhá při teplotách, běžných např. pro hydrolytickou polymeraci, v závislosti ne typu lektamu stejnou nebo vyěěí rychlostí než hydrolytické polymerace ze obdobných podmínek (teplota, koncentrace iniciátoru). Polymerační stupeň vznikajících polymerů stoupá s klesajícím obsahem iniciátoru, takže lze tímto způsobem připravit polyamidy a kopolyamidy od nízkomolekulárníoh, vhodných pro přípravu polyamidových prášků pro sorpční materiály a disperze, až po vysokomolekulární typy, vhodné pro zvlékňovéní, vstřikování a vytlačování.The effect of the process according to the invention is that the polymerization or copolymerization of the lactams initiated by the compounds takes place at temperatures common, e.g. The polymerization degree of the resulting polymers increases with decreasing initiator content so that polyamides and copolyamides can be prepared from low molecular weight, suitable for preparing polyamide powders for sorption materials and dispersions, to high molecular weight, suitable for spinning, injection molding and extrusion.
Kromě iniciačního účinku mají sloučeniny H^AsO^ . ΝΗ-(ΟΗ2)χ-<}θ ještě další výhodnou vlastnost. Kyselina arseničné zůstává totiž z části zabudována do řetězce polyamidu nebo kopolyamidu a je tedy nositelkou nových vlastností těchto polymerů, nepř. antibaktericidníoh apod.In addition to the initiating effect, the compounds have H 2 AsO 4. ΝΗ- (ΟΗ 2 ) χ - <} θ yet another advantageous property. Indeed, arsenic acid remains partially incorporated into the polyamide or copolyamide chain and is therefore the carrier of the novel properties of these polymers, e.g. antibactericidal, etc.
Způsob podle vynálezu je dále blíže popsán na několika příkladech provedení.The process according to the invention is described in more detail below on several exemplary embodiments.
PřikladlHe did
6-Kaprolaktam byl polymerován v přítomnosti 2 mol. % sloučeniny HytsO^ . ŇH-(CH2)5-ČO při 260 °C v zatavené evakuovené skleněné ampuli. Po 1 hodině bylo získáno 40 % polymeru o viskozimetrickém polymeračním stupni Pg = 36, po 3 hodinách 78 X polymeru o Pg = 66. Rovnovážný polymer o P-, = 67 byl získán po 8 hodinách polymerace. (Obsah polymeru byl stanoven po extrakci vodou.)6-Caprolactam was polymerized in the presence of 2 mol. % of the compound HytsO4. HH- (CH 2 ) 5 -CO at 260 ° C in a sealed evacuated glass vial. After 1 hour 40% of the polymer having a viscosimetric polymerization degree of Pg = 36 was obtained, after 3 hours 78% of the polymer with Pg = 66. An equilibrium polymer of P- = 67 was obtained after 8 hours of polymerization. (The polymer content was determined after extraction with water.)
Příklad 2Example 2
Polymerace 6-kaprolaktamu, iniciované 20 mol X H^AsO^ . ŇH-(CH2)^-ČO byla provedena způsobem popsaným v příkladu 1. Po 30 minutách polymerace byla ampule ochlazena, obsah extrahován vodou, zfiltrovén a vysušen. Bylo získáno 70 X práškového polymeru o P^ = 15.Polymerization of 6-caprolactam, initiated with 20 moles of XH ^O AsO ^. NH- (CH2) ^ - has been performed as described in Example 1. After 30 min of polymerization, the ampoule was cooled and the contents extracted with water, and dried zfiltrovén. 70% of the polymer powder with P = 15 were obtained.
Přiklad 3Example 3
Polymerace 8-oktanlaktamu, iniciované 2 mol X H^AsO^ . ÍtH-(CH2)?-ČO při teplotě 200 °C byla provedena způsobem podle příkladu 1. Rovnovážný polyamid 8 o Pf; = 70 byl získán po 100 hodinách polymerace.Polymerization of 8-octanlactam, initiated with 2 moles of XH ^O AsO ^. 1 H- (CH 2 ) 2 -CO at 200 ° C was carried out as in Example 1. Equilibrium polyamide 8 o P f; = 70 was obtained after 100 hours of polymerization.
Příklad 4Example 4
Polymerace 12-dodekenlektemu, iniciovaná 0,1 mol X H^AsO^ . áH-(CH2)^,-ČO při teplotě 330 °C byle provedena způsobem podle příkladu 1 s tím rozdílem, že obsah polymeru byl stanoven po extrakci reakční směsi methanolem. Po třech hodinách polymerace bylo získáno 90 X polyamidu 12 o P^ = 320.Polymerization of 12-dodecenlektem, initiated with 0.1 mol XH2O2O4. The? - (CH 2 ) 4 -CO 2 at 330 ° C was carried out as in Example 1 except that the polymer content was determined after the reaction mixture was extracted with methanol. After three hours of polymerization, 90% of polyamide 12 having P = 320 were obtained.
Příklad 5Example 5
Kopolymerace ekvimolární směsi 6-kaprolaktamu a li-dodekanlektamu, iniciovaná 2 mol X HjAsO^ . ŇH-(CH2)j-ČO při 260 °C byla provedena podle příkladu 4, Rovnovážný kopolymer o vnitřní viskozitě [7] = 1,0 (m-kresol, 25 °C) byl získán po 20 hodinách.Copolymerization of an equimolar mixture of 6-caprolactam and li-dodecanlectam, initiated with 2 mol X of HjAsO ^. 1 H- (CH 2 ) i -CO at 260 ° C was carried out according to Example 4, an equilibrium copolymer with an intrinsic viscosity [7] = 1.0 (m-cresol, 25 ° C) was obtained after 20 hours.
Příklad 6Example 6
Terpolymerace ekvimolérní směsi 6-kaprolaktamu, 12-dodekalaktamu a směsi C-methylizomerů 6-kaprolaktamu, iniciované 10 mol X H^AsO^ . ÁH-CCHg)^-00 byla provedena postupem, popsaným v příkladu 4. Po 90 minutách polymerace při 260 °C a extrakci methanolem byl získán préěkový terpolyamid o [>?] 0,4 ve výtěžku 48 %.Terpolymerization of an equimolar mixture of 6-caprolactam, 12-dodecalactam and a mixture of 6-caprolactam C-methyl isomers, initiated with 10 mole of H HA AsO ^. The -H-CHg)) ^-00 was carried out as described in Example 4. After 90 minutes of polymerization at 260 ° C and extraction with methanol, the resulting terpolyamide was> [?] 0.4 in a yield of 48%.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS87583A CS229038B3 (en) | 1983-02-08 | 1983-02-08 | Method of polymerizing and copolymerizing lactams of om |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS87583A CS229038B3 (en) | 1983-02-08 | 1983-02-08 | Method of polymerizing and copolymerizing lactams of om |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CS229038B3 true CS229038B3 (en) | 1984-05-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CS87583A CS229038B3 (en) | 1983-02-08 | 1983-02-08 | Method of polymerizing and copolymerizing lactams of om |
Country Status (1)
| Country | Link |
|---|---|
| CS (1) | CS229038B3 (en) |
-
1983
- 1983-02-08 CS CS87583A patent/CS229038B3/en unknown
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