JPH0225932B2 - - Google Patents
Info
- Publication number
- JPH0225932B2 JPH0225932B2 JP5723181A JP5723181A JPH0225932B2 JP H0225932 B2 JPH0225932 B2 JP H0225932B2 JP 5723181 A JP5723181 A JP 5723181A JP 5723181 A JP5723181 A JP 5723181A JP H0225932 B2 JPH0225932 B2 JP H0225932B2
- Authority
- JP
- Japan
- Prior art keywords
- polybutylene terephthalate
- acid
- fine particles
- terephthalate polymer
- polymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- -1 polybutylene terephthalate Polymers 0.000 claims description 40
- 229920001707 polybutylene terephthalate Polymers 0.000 claims description 32
- 229920000642 polymer Polymers 0.000 claims description 28
- 150000003951 lactams Chemical class 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 230000001376 precipitating effect Effects 0.000 claims description 5
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- 239000010419 fine particle Substances 0.000 description 19
- 238000000034 method Methods 0.000 description 11
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 8
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 8
- 238000001816 cooling Methods 0.000 description 6
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 6
- 239000003054 catalyst Substances 0.000 description 5
- 150000001991 dicarboxylic acids Chemical class 0.000 description 5
- 150000002009 diols Chemical class 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 229920000728 polyester Polymers 0.000 description 4
- 238000010298 pulverizing process Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 3
- 239000002667 nucleating agent Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical compound C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- QMKYBPDZANOJGF-UHFFFAOYSA-N benzene-1,3,5-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC(C(O)=O)=C1 QMKYBPDZANOJGF-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000003484 crystal nucleating agent Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000012760 heat stabilizer Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- YPFDHNVEDLHUCE-UHFFFAOYSA-N propane-1,3-diol Chemical compound OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 2
- CYIDZMCFTVVTJO-UHFFFAOYSA-N pyromellitic acid Chemical compound OC(=O)C1=CC(C(O)=O)=C(C(O)=O)C=C1C(O)=O CYIDZMCFTVVTJO-UHFFFAOYSA-N 0.000 description 2
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000005809 transesterification reaction Methods 0.000 description 2
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 2
- GGAUUQHSCNMCAU-ZXZARUISSA-N (2s,3r)-butane-1,2,3,4-tetracarboxylic acid Chemical compound OC(=O)C[C@H](C(O)=O)[C@H](C(O)=O)CC(O)=O GGAUUQHSCNMCAU-ZXZARUISSA-N 0.000 description 1
- QFGCFKJIPBRJGM-UHFFFAOYSA-N 12-[(2-methylpropan-2-yl)oxy]-12-oxododecanoic acid Chemical compound CC(C)(C)OC(=O)CCCCCCCCCCC(O)=O QFGCFKJIPBRJGM-UHFFFAOYSA-N 0.000 description 1
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- XCSGHNKDXGYELG-UHFFFAOYSA-N 2-phenoxyethoxybenzene Chemical compound C=1C=CC=CC=1OCCOC1=CC=CC=C1 XCSGHNKDXGYELG-UHFFFAOYSA-N 0.000 description 1
- UUAGPGQUHZVJBQ-UHFFFAOYSA-N Bisphenol A bis(2-hydroxyethyl)ether Chemical compound C=1C=C(OCCO)C=CC=1C(C)(C)C1=CC=C(OCCO)C=C1 UUAGPGQUHZVJBQ-UHFFFAOYSA-N 0.000 description 1
- ALQSHHUCVQOPAS-UHFFFAOYSA-N Pentane-1,5-diol Chemical compound OCCCCCO ALQSHHUCVQOPAS-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- XMUZQOKACOLCSS-UHFFFAOYSA-N [2-(hydroxymethyl)phenyl]methanol Chemical compound OCC1=CC=CC=C1CO XMUZQOKACOLCSS-UHFFFAOYSA-N 0.000 description 1
- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 1
- UKLDJPRMSDWDSL-UHFFFAOYSA-L [dibutyl(dodecanoyloxy)stannyl] dodecanoate Chemical compound CCCCCCCCCCCC(=O)O[Sn](CCCC)(CCCC)OC(=O)CCCCCCCCCCC UKLDJPRMSDWDSL-UHFFFAOYSA-L 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 150000007860 aryl ester derivatives Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- MNFORVFSTILPAW-UHFFFAOYSA-N azetidin-2-one Chemical compound O=C1CCN1 MNFORVFSTILPAW-UHFFFAOYSA-N 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 125000006267 biphenyl group Chemical group 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical class [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000006258 conductive agent Substances 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- QYQADNCHXSEGJT-UHFFFAOYSA-N cyclohexane-1,1-dicarboxylate;hydron Chemical compound OC(=O)C1(C(O)=O)CCCCC1 QYQADNCHXSEGJT-UHFFFAOYSA-N 0.000 description 1
- PDXRQENMIVHKPI-UHFFFAOYSA-N cyclohexane-1,1-diol Chemical compound OC1(O)CCCCC1 PDXRQENMIVHKPI-UHFFFAOYSA-N 0.000 description 1
- IGARGHRYKHJQSM-UHFFFAOYSA-N cyclohexylbenzene Chemical group C1CCCCC1C1=CC=CC=C1 IGARGHRYKHJQSM-UHFFFAOYSA-N 0.000 description 1
- FOTKYAAJKYLFFN-UHFFFAOYSA-N decane-1,10-diol Chemical compound OCCCCCCCCCCO FOTKYAAJKYLFFN-UHFFFAOYSA-N 0.000 description 1
- JGFBRKRYDCGYKD-UHFFFAOYSA-N dibutyl(oxo)tin Chemical compound CCCC[Sn](=O)CCCC JGFBRKRYDCGYKD-UHFFFAOYSA-N 0.000 description 1
- 239000000539 dimer Substances 0.000 description 1
- UHWHMHPXHWHWPX-UHFFFAOYSA-J dipotassium;oxalate;oxotitanium(2+) Chemical compound [K+].[K+].[Ti+2]=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O UHWHMHPXHWHWPX-UHFFFAOYSA-J 0.000 description 1
- LHLUQDDQLCJCFU-UHFFFAOYSA-L disodium;1-sulfocyclohexa-3,5-diene-1,3-dicarboxylate Chemical compound [Na+].[Na+].OS(=O)(=O)C1(C([O-])=O)CC(C([O-])=O)=CC=C1 LHLUQDDQLCJCFU-UHFFFAOYSA-L 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- YVIVRJLWYJGJTJ-UHFFFAOYSA-N gamma-Valerolactam Chemical compound CC1CCC(=O)N1 YVIVRJLWYJGJTJ-UHFFFAOYSA-N 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002440 hydroxy compounds Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229940046892 lead acetate Drugs 0.000 description 1
- 150000002611 lead compounds Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Chemical class 0.000 description 1
- 239000002184 metal Chemical class 0.000 description 1
- ITNVWQNWHXEMNS-UHFFFAOYSA-N methanolate;titanium(4+) Chemical class [Ti+4].[O-]C.[O-]C.[O-]C.[O-]C ITNVWQNWHXEMNS-UHFFFAOYSA-N 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- RXOHFPCZGPKIRD-UHFFFAOYSA-N naphthalene-2,6-dicarboxylic acid Chemical compound C1=C(C(O)=O)C=CC2=CC(C(=O)O)=CC=C21 RXOHFPCZGPKIRD-UHFFFAOYSA-N 0.000 description 1
- WPUMVKJOWWJPRK-UHFFFAOYSA-N naphthalene-2,7-dicarboxylic acid Chemical compound C1=CC(C(O)=O)=CC2=CC(C(=O)O)=CC=C21 WPUMVKJOWWJPRK-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- OTLDLKLSNZMTTA-UHFFFAOYSA-N octahydro-1h-4,7-methanoindene-1,5-diyldimethanol Chemical compound C1C2C3C(CO)CCC3C1C(CO)C2 OTLDLKLSNZMTTA-UHFFFAOYSA-N 0.000 description 1
- BBJSDUUHGVDNKL-UHFFFAOYSA-J oxalate;titanium(4+) Chemical compound [Ti+4].[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O BBJSDUUHGVDNKL-UHFFFAOYSA-J 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- XUWHAWMETYGRKB-UHFFFAOYSA-N piperidin-2-one Chemical compound O=C1CCCCN1 XUWHAWMETYGRKB-UHFFFAOYSA-N 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000000710 polymer precipitation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000003457 sulfones Chemical class 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004736 wide-angle X-ray diffraction Methods 0.000 description 1
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
Description
【発明の詳細な説明】
本発明は、ポリブチレンテレフタレート系重合
体微粒子の製造方法に関する。さらに詳しくは、
ラクタムを使用した、高結晶性ポリブチレンテレ
フタレート系重合体微粒子の製造方法に関するも
のである。
テレフタル酸および1,4−ブタンジオールを
必須成分とするポリブチレンテレフタレート系重
合体のごときポリエステルはその優れた結晶性等
の物理的性質、化学的性質および熱的性質を生か
して種々の用途分野、例えば、射出成形品、繊維
およびフイルム等として使用されている。
しかるに、かかるポリエステルの高結晶性微粒
子を要する高分子核剤用途等に使用する場合、そ
の優れた物理的性質および化学的性質のため微粉
体化が困難であるばかりではなく、高結晶性微粒
子が得られないという問題点を有している。例え
ば、機械的に微粉砕化する方法は、粗砕には適し
ているものの微粒子化には限度があるばかりでは
なく、高結晶性の微粒子は得られない。また、ハ
ロゲン化芳香族等の特定の溶媒に加熱溶解後冷
却・析出させ微粉化する方法も知られているが、
この方法は冷却析出時の重合体析出速度が極めて
遅く、収率良く微粒子化するためには極めて長時
間を要するという欠陥を有している。
そこで本発明者らは、ポリブチレンテレフタレ
ート系重合体の高結晶性微粒子を製造する方法に
つき、種々検討した結果、ポリブチレンテレフタ
レート系重合体をラクタムに加熱溶解後冷却する
ことによつて、高結晶性ポリブチレンテレフタレ
ート系微粒子が得られることを見い出し本発明に
到達した。
すなわち本発明は、ポリブチレンテレフタレー
ト系重合体微粒子の製造に際し、下記一般式のラ
クタムにポリブチレンテレフタレート系重合体を
溶解したのち、析出させることを特徴とするポリ
ブチレンテレフタレート系重合体微粒子の製造方
法を提供するものである。
(上式中のRは炭素数1〜5のアルキル基または
H原子、nは1〜10の整数。)
本発明におけるポリブチレンテレフタレート系
重合体とは、テレフタル酸および1,4−ブタン
ジオールを必須成分とする重合体である。更にそ
の他のジカルボン酸および/もしくはその他のジ
オールから成る50モル%まで、より好ましくは30
モル%までの共重合成分を含むことができるが、
共重合成分が50モル%をこえるとポリブチレンテ
レフタレートの優れた物理的性質を損うばかりで
はなく、結晶性が低下し本発明の方法を適用でき
なくなるため好ましくない。
テレフタル酸以外のジカルボン酸としてはイソ
フタル酸、フタル酸、ナフタレン−2,6−ジカ
ルボン酸、ナフタレン−2,7−ジカルボン酸、
ジフエニル−4,4′−ジカルボン酸、ジフエノキ
シエタンジカルボン酸、3−スルホイソフタル酸
ナトリウム等のごとき芳香族ジカルボン酸1,4
−シクロヘキサンジカルボン酸のごとき脂環族ジ
カルボン酸、ゴハク酸、シユウ酸、アジピン酸、
セバシン酸、ドデカンジ酸、ダイマー酸のごとき
脂肪族ジカルボン酸等を挙げることができる。も
ちろんジカルボン酸のエステル形成性誘導体たと
えば低級アルキルエステル、アリールエステル、
炭酸エステルさらには酸ハロゲン化物なども同等
に用いうる。また、1,4−ブタンジオール以外
のジオール成分としては、たとえばエチレングリ
コール、トリメチレングリコール、ペンタメチレ
ングリコール、ヘキサメチレングリコール、ネオ
ペンチルグリコール、デカメチレングリコールな
どの脂肪族ジオール、1,1−シクロヘキサンジ
メタノール、1,4−シクロヘキサンジメタノー
ル、トリシクロデカンジメタノールのごとき脂環
族ジオール、キシリレングリコール、ビス(p−
ヒドロキシ)ジフエニル、ビス(p−ヒドロキシ
フエニル)プロパン、2,2−ビス〔4−(2−
ヒドロキシエトキシ)フエニル〕プロパン、ビス
〔4−(2−ヒドロキシ)フエニル〕スルホン、
1,1−ビス〔4−(2−ヒドロキシエトキシ)
フエニル〕シクロヘキサンなどの芳香族基を含む
ジオールなどが挙げられる。かかるジオールもエ
ステル形成性誘導体たとえばアセチル体、アルカ
リ金属塩などの形でも用いうる。
前記ポリブチレンテレフタレート系重合体は公
知の方法で製造され得る。たとえばジカルボン酸
の低級アルコールジエステル、過剰量の低分子量
グリコールを触媒の存在下エステル交換反応せし
め、得られる反応生成物を重縮合する方法、ある
いはジカルボン酸とグリコールを触媒の存在下エ
ステル化反応せしめ得られる反応生成物を重縮合
する方法、また予めポリブチレンテレフタレート
を作つておき、これに他のジカルボン酸やジオー
ルを加えたり、もしくは他の共重合ポリエステル
を添加してエステル交換によりランダム化せしめ
る方法などいずれの方法をとつてもよい。
エステル交換反応またはエステル化反応と重縮
合反応に共通の触媒として、チタン触媒が良好な
結果を与える。特にテトラブチルチタネート、テ
トラメチルチタネートなどのごときテトラアルキ
ルチタネート、シユウ酸チタンカリのごときシユ
ウ酸チタン金属塩等が好ましい。またその他の触
媒としてはジブチルスズオキサイド、ジブチルス
ズラウレートのごときスズ化合物、酢酸鉛のごと
き鉛化合物があげられる。
また、ジカルボン酸やグリコールの一部として
ポリカルボン酸や多官能ヒドロキシ化合物、オキ
シ酸などが共重合されていてもよい。多官能成分
は高粘度化成分として有効に作用し、その共重合
しうる範囲は3モル%以下である。かかる多官能
成分として用いることができるものにはトリメリ
ツト酸、トリメシン酸、ピロメリツト酸、ペンゾ
フエノンテトラカルボン酸、ブタンテトラカルボ
ン酸、グリセリン、ペンタエリスリトールおよび
それらのエステル、酸無水物などを挙げることが
できる。
上記ポリブチレンテレフタレート系重合体以外
のポリエステル例えばポリエチレンテレフタレー
トに本発明の方法を適用した場合、微粒子化は可
能であるものの、ポリブチレンテレフタレート系
重合体程高結晶性の微粒子は得られず、ポリブチ
レンテレフタレート系重合体に本発明を適用する
ことによつて、始めて核剤用途に供するような高
結晶性微粒子とすることが可能となり本発明が達
成されるのである。
本発明のラクタムは下記一般式の化合物であ
り、
(上式中のRは炭素数1〜5のアルキル基または
H原子、nは1〜10の整数。)
具体的には、β−プロピオラクタム、γ−ブチ
ロラクタム、γ−バレロラクタム、δ−バレロラ
クタム、ε−カプロラクタム、ヘプトラクタム等
が挙げられ、これらの1種または2種以上を混合
して用いても良い。また、加熱溶解時に操作上支
障とならない程度の耐熱性および沸点を有し、上
記ラクタムと相溶性のある他の多くの溶媒を併用
して用いても良い。
ポリブチレンテレフタレート系重合体をラクタ
ムに溶解する方法は任意であり特に限定するもの
ではないが、例えば、密封容器中にラクタムを加
え150℃〜250℃に加熱後、撹拌下にポリブチレン
テレフタレート系重合体を加え、5〜30分加熱し
て溶解せしめれば良い。
溶解温度は、ポリブチレンテレフタレート系重
合体組成および添加量によつて変化するため特に
限定するものではないが、150℃〜ラクタムの沸
点以下の温度が好ましい。
なお、溶解時に種々の添加剤、例えば公知の結
晶核剤や滑剤などの成形助剤、公知の酸化防止
剤、紫外線吸収剤などの耐熱・耐光性の安定剤、
耐加水分解改良剤、着色剤(顔料、染料)、帯電
防止剤、導電剤、難燃剤、補強剤、充填剤、可塑
剤、離型剤などを任意添加溶解し、微粒子に含有
させることができる。
特に公知のヒンダードフエノール系、アミン系
等の耐熱安定剤を併用せしめれば耐熱エージング
性を改善することができる。また公知の結晶核剤
として、タルク等を添加することによつてより微
細な粒子の製造が可能となる。この場合添加量
は、ポリブチレンテレフタレート系重合体および
ラクタム総重量の0.005〜5.0重量%が好ましい。
本発明の方法において、微粒子の形状、結晶化
度等は、上記ポリブチレンテレフタレート系重合
体を溶解したラクタム溶液を冷却し、ポリブチレ
ンテレフタレート系重合体を析出する過程に依存
して変化させ得る。
例えば、冷却速度を遅くし高温で析出させれ
ば、大きな球晶状微粒子が得られまた急冷すれば
小さな球晶状微粒子が得られる。また剪断を付加
しながら析出されるとランダム形状かつ高結晶性
微粒子を製造することが可能である。更に、加圧
しながら析出させる等して任意の結晶化度、形状
および粒度分布を有する微粒子を製造することが
可能であり、すべて本発明の技術的範囲に包含さ
れる。
上記のように冷却されたポリブチレンテレフタ
レート系重合体含有スラリまたは固体を、次い
で、水等の溶媒中でラクタムを溶解後ろ過乾燥す
ることによつてポリブチレンテレフタレート系重
合体微粒子を得ることができる。この際使用する
溶媒は特に限定するものではなく、室温付近でラ
クタムを溶解しポリブチレンテレフタレート系重
合体を溶解しないものであればどれでも良く水以
外に、例えば、メタノール、エタノール、エーテ
ル、テトラハイドロフラン等を挙げることができ
る。
本発明のポリブチレンテレフタレート系重合体
微粒子は種々の用途に使用することができ、例え
ば、粉体塗装用樹脂粉末、充填剤、サスペンジヨ
ン、成形用核剤等が挙げられ、更に物理的あるい
は化学的処理により多くの用途への適用が可能で
ある。
以下実施例により本発明を説明する。
なお、実施例中「%」で表示したものはすべて
重量比率で表わしたものである。また、本文中お
よび例中に示す対数粘度はオルトクロロフエノー
ル中、30℃、0.5%濃度の条件で測定した値であ
る。また、例中の結晶化度は、理学電気社製広角
X線散乱装置を使用し、全散乱強度と結晶散乱強
度の比率から求めた。また粒子形状粒度分布は顕
微鏡観察から求めた。
実施例1〜8、比較例1
テレフタル酸および1,4−ブタンジオールか
ら得られた対数粘度0.60のポリブチレンテレフタ
レートを表1の重量%、210℃に加熱したε−カ
プロラクタム中に撹拌下添加し、約15分加熱し溶
解した。
溶解後表1の析出方法で室温まで冷却した。
得られた固体に蒸留水を加えε−カプロラクタ
ムを溶解後ろ過し更に水洗・乾燥しポリブチレン
テレフタレート微粒子を得た。
得られたポリブチレンテレフタレート微粒子の
性質を表1に示す。比較のため機械粉砕したポリ
ブチレンテレフタレート粉末の性質も付記した。
この粉末は、ペレツト状サンプルを液体窒素で冷
却しながら粉砕機で1時間粉砕後100メツシユの
ふるいを通過したものを使用した。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing polybutylene terephthalate polymer particles. For more details,
The present invention relates to a method for producing highly crystalline polybutylene terephthalate polymer particles using lactam. Polyesters such as polybutylene terephthalate polymers, which contain terephthalic acid and 1,4-butanediol as essential components, can be used in a variety of fields by taking advantage of their excellent physical properties such as crystallinity, chemical properties, and thermal properties. For example, it is used in injection molded products, fibers, films, etc. However, when using such polyester in applications such as polymer nucleating agents that require highly crystalline fine particles, it is not only difficult to pulverize it due to its excellent physical and chemical properties, but also the highly crystalline fine particles The problem is that it cannot be obtained. For example, mechanical pulverization is suitable for coarse pulverization, but not only is there a limit to pulverization, but also highly crystalline fine particles cannot be obtained. In addition, a method is known in which halogenated aromatics are heated and dissolved in a specific solvent, and then cooled and precipitated to form a fine powder.
This method has the drawback that the polymer precipitation rate during cooling precipitation is extremely slow and that it takes an extremely long time to form fine particles with good yield. Therefore, the present inventors conducted various studies on a method for producing highly crystalline fine particles of a polybutylene terephthalate polymer. As a result, the present inventors discovered a method for producing highly crystalline fine particles of a polybutylene terephthalate polymer by heating and dissolving the polybutylene terephthalate polymer in lactam and then cooling it. The inventors have discovered that polybutylene terephthalate-based fine particles can be obtained, and have arrived at the present invention. That is, the present invention provides a method for producing polybutylene terephthalate polymer fine particles, which comprises dissolving the polybutylene terephthalate polymer in a lactam having the following general formula and then precipitating the polybutylene terephthalate polymer fine particles. It provides: (R in the above formula is an alkyl group having 1 to 5 carbon atoms or an H atom, and n is an integer of 1 to 10.) In the present invention, the polybutylene terephthalate polymer refers to terephthalic acid and 1,4-butanediol. It is a polymer that is an essential component. up to 50 mol %, more preferably 30 mol %, further consisting of other dicarboxylic acids and/or other diols.
Although it can contain up to mol% of copolymerized components,
If the copolymerization component exceeds 50 mol%, it is not preferable because it not only impairs the excellent physical properties of polybutylene terephthalate but also reduces crystallinity, making it impossible to apply the method of the present invention. Dicarboxylic acids other than terephthalic acid include isophthalic acid, phthalic acid, naphthalene-2,6-dicarboxylic acid, naphthalene-2,7-dicarboxylic acid,
Aromatic dicarboxylic acids 1,4 such as diphenyl-4,4'-dicarboxylic acid, diphenoxyethane dicarboxylic acid, sodium 3-sulfoisophthalate, etc.
- cycloaliphatic dicarboxylic acids such as cyclohexanedicarboxylic acid, succinic acid, oxalic acid, adipic acid,
Examples include aliphatic dicarboxylic acids such as sebacic acid, dodecanedioic acid, and dimer acid. Of course, ester-forming derivatives of dicarboxylic acids such as lower alkyl esters, aryl esters,
Carbonic esters, acid halides, and the like can be equally used. Diol components other than 1,4-butanediol include aliphatic diols such as ethylene glycol, trimethylene glycol, pentamethylene glycol, hexamethylene glycol, neopentyl glycol, and decamethylene glycol, and 1,1-cyclohexane diol. Alicyclic diols such as methanol, 1,4-cyclohexanedimethanol, tricyclodecane dimethanol, xylylene glycol, bis(p-
hydroxy) diphenyl, bis(p-hydroxyphenyl)propane, 2,2-bis[4-(2-
hydroxyethoxy)phenyl]propane, bis[4-(2-hydroxy)phenyl]sulfone,
1,1-bis[4-(2-hydroxyethoxy)
Examples include diols containing aromatic groups such as [phenyl]cyclohexane. Such diols can also be used in the form of ester-forming derivatives such as acetyl derivatives, alkali metal salts, and the like. The polybutylene terephthalate polymer may be produced by a known method. For example, a lower alcohol diester of a dicarboxylic acid or an excess amount of a low molecular weight glycol may be transesterified in the presence of a catalyst, and the resulting reaction product may be polycondensed, or a dicarboxylic acid and a glycol may be esterified in the presence of a catalyst. A method in which polybutylene terephthalate is prepared in advance, and then other dicarboxylic acids or diols are added to it, or other copolymerized polyesters are added and randomization is performed by transesterification. Either method may be used. As a common catalyst for transesterification or esterification reactions and polycondensation reactions, titanium catalysts give good results. Particularly preferred are tetraalkyl titanates such as tetrabutyl titanate and tetramethyl titanate, and metal salts of titanium oxalate such as potassium titanium oxalate. Other catalysts include tin compounds such as dibutyltin oxide and dibutyltin laurate, and lead compounds such as lead acetate. Furthermore, a polycarboxylic acid, a polyfunctional hydroxy compound, an oxyacid, or the like may be copolymerized as part of the dicarboxylic acid or glycol. The polyfunctional component effectively acts as a viscosity increasing component, and the range in which it can be copolymerized is 3 mol % or less. Examples of compounds that can be used as such polyfunctional components include trimellitic acid, trimesic acid, pyromellitic acid, penzophenonetetracarboxylic acid, butanetetracarboxylic acid, glycerin, pentaerythritol and their esters and acid anhydrides. can. When the method of the present invention is applied to polyesters other than the above-mentioned polybutylene terephthalate-based polymers, for example, polyethylene terephthalate, it is possible to make them into fine particles, but fine particles as highly crystalline as the polybutylene terephthalate-based polymer cannot be obtained. By applying the present invention to a terephthalate polymer, it becomes possible to obtain highly crystalline fine particles that can be used as a nucleating agent, thereby achieving the present invention. The lactam of the present invention is a compound of the following general formula, (R in the above formula is an alkyl group having 1 to 5 carbon atoms or an H atom, and n is an integer of 1 to 10.) Specifically, β-propiolactam, γ-butyrolactam, γ-valerolactam, δ- Examples include valerolactam, ε-caprolactam, heptolactam, etc., and these may be used alone or in combination of two or more. In addition, many other solvents that have heat resistance and boiling point that do not cause operational problems during heating and dissolution, and are compatible with the above-mentioned lactams may be used in combination. The method of dissolving the polybutylene terephthalate polymer in the lactam is arbitrary and is not particularly limited. Add the mixture and heat for 5 to 30 minutes to dissolve. The melting temperature is not particularly limited as it changes depending on the composition of the polybutylene terephthalate polymer and the amount added, but a temperature of 150° C. to the boiling point of the lactam is preferred. In addition, various additives may be added during dissolution, such as forming aids such as known crystal nucleating agents and lubricants, known antioxidants, heat-resistant and light-resistant stabilizers such as ultraviolet absorbers,
Hydrolysis resistance improvers, colorants (pigments, dyes), antistatic agents, conductive agents, flame retardants, reinforcing agents, fillers, plasticizers, mold release agents, etc. can be optionally added and dissolved and incorporated into fine particles. . In particular, the heat aging resistance can be improved by using a known heat stabilizer such as a hindered phenol type or an amine type heat stabilizer. Further, by adding talc or the like as a known crystal nucleating agent, it becomes possible to produce finer particles. In this case, the amount added is preferably 0.005 to 5.0% by weight based on the total weight of the polybutylene terephthalate polymer and lactam. In the method of the present invention, the shape, crystallinity, etc. of the fine particles can be changed depending on the process of cooling the lactam solution in which the polybutylene terephthalate polymer is dissolved and precipitating the polybutylene terephthalate polymer. For example, by slowing down the cooling rate and precipitating at a high temperature, large spherulite particles can be obtained, and by rapid cooling, small spherulite particles can be obtained. Furthermore, if the particles are precipitated while applying shear, it is possible to produce randomly shaped and highly crystalline fine particles. Furthermore, it is possible to produce fine particles having any degree of crystallinity, shape, and particle size distribution by precipitating while applying pressure, and all of these are included within the technical scope of the present invention. The slurry or solid containing the polybutylene terephthalate polymer cooled as described above is then overdried after dissolving the lactam in a solvent such as water to obtain fine particles of the polybutylene terephthalate polymer. . The solvent used at this time is not particularly limited, and any solvent may be used as long as it dissolves the lactam at around room temperature and does not dissolve the polybutylene terephthalate polymer. Furan etc. can be mentioned. The polybutylene terephthalate polymer particles of the present invention can be used for various purposes, such as resin powder for powder coating, fillers, suspensions, and nucleating agents for molding. It can be applied to many uses through physical processing. The present invention will be explained below with reference to Examples. In the examples, all percentages expressed as "%" are expressed as weight ratios. Further, the logarithmic viscosity shown in the text and examples is a value measured in orthochlorophenol at 30°C and at a concentration of 0.5%. Further, the degree of crystallinity in the examples was determined from the ratio of the total scattering intensity to the crystal scattering intensity using a wide-angle X-ray scattering device manufactured by Rigaku Denki. In addition, the particle shape and size distribution was determined from microscopic observation. Examples 1 to 8, Comparative Example 1 Polybutylene terephthalate with a logarithmic viscosity of 0.60 obtained from terephthalic acid and 1,4-butanediol was added in the weight percent shown in Table 1 to ε-caprolactam heated to 210°C under stirring. , heated for about 15 minutes to dissolve. After dissolution, the solution was cooled to room temperature using the precipitation method shown in Table 1. Distilled water was added to the obtained solid to dissolve ε-caprolactam, followed by filtration, washing with water, and drying to obtain polybutylene terephthalate fine particles. Table 1 shows the properties of the obtained polybutylene terephthalate fine particles. For comparison, the properties of mechanically pulverized polybutylene terephthalate powder are also included.
This powder was obtained by pulverizing a pelleted sample in a pulverizer for one hour while cooling it with liquid nitrogen, and then passing it through a 100-mesh sieve. 【table】
Claims (1)
の製造に際し、下記一般式のラクタムにポリブチ
レンテレフタレート系重合体を溶解したのち析出
させることを特徴とするポリブチレンテレフタレ
ート系微粒子の製造方法。 (上式中のRは炭素数1〜5のアルキル基または
H原子、nは1〜10の整数。)[Scope of Claims] 1. A method for producing polybutylene terephthalate polymer particles, which comprises dissolving a polybutylene terephthalate polymer in a lactam having the following general formula and then precipitating the polybutylene terephthalate polymer particles. (R in the above formula is an alkyl group having 1 to 5 carbon atoms or an H atom, and n is an integer of 1 to 10.)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5723181A JPS57172923A (en) | 1981-04-17 | 1981-04-17 | Production of polybutylene terephthalate polymer fine particle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5723181A JPS57172923A (en) | 1981-04-17 | 1981-04-17 | Production of polybutylene terephthalate polymer fine particle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57172923A JPS57172923A (en) | 1982-10-25 |
| JPH0225932B2 true JPH0225932B2 (en) | 1990-06-06 |
Family
ID=13049750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5723181A Granted JPS57172923A (en) | 1981-04-17 | 1981-04-17 | Production of polybutylene terephthalate polymer fine particle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57172923A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7268143B2 (en) | 2001-08-31 | 2007-09-11 | Inotek Pharmaceuticals Corporation | Isoquinoline derivatives and methods of use thereof |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5055328A (en) * | 1989-06-16 | 1991-10-08 | Viskase Corporation | Differentially cross-linked multilayer film |
| KR0148831B1 (en) * | 1994-09-29 | 1998-10-15 | 김은영 | Process for producing crystalline polyester powder |
| WO2018096964A1 (en) * | 2016-11-25 | 2018-05-31 | 東レ株式会社 | Method for producing polybutylene terephthalate resin particles, and polybutylene terephthalate resin particles |
| EP3546502A1 (en) * | 2018-03-27 | 2019-10-02 | Friedrich-Alexander-Universität Erlangen-Nürnberg | Method for producing a population of particles of polyethylene terephthalate or polybutylene terephthalate or of a copolymer comprising pet and/or pbt |
-
1981
- 1981-04-17 JP JP5723181A patent/JPS57172923A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7268143B2 (en) | 2001-08-31 | 2007-09-11 | Inotek Pharmaceuticals Corporation | Isoquinoline derivatives and methods of use thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57172923A (en) | 1982-10-25 |
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