JP2860182B2 - Method for producing polyester containing urethane bond - Google Patents
Method for producing polyester containing urethane bondInfo
- Publication number
- JP2860182B2 JP2860182B2 JP19681291A JP19681291A JP2860182B2 JP 2860182 B2 JP2860182 B2 JP 2860182B2 JP 19681291 A JP19681291 A JP 19681291A JP 19681291 A JP19681291 A JP 19681291A JP 2860182 B2 JP2860182 B2 JP 2860182B2
- Authority
- JP
- Japan
- Prior art keywords
- polyester
- molecular weight
- weight
- parts
- diisocyanate
- 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 - Fee Related
Links
- 229920000728 polyester Polymers 0.000 title claims description 54
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 125000005442 diisocyanate group Chemical group 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 12
- 125000001931 aliphatic group Chemical group 0.000 claims description 9
- 229920003232 aliphatic polyester Polymers 0.000 claims description 9
- 150000002291 germanium compounds Chemical class 0.000 claims description 9
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 9
- 229920005989 resin Polymers 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 7
- 230000002194 synthesizing effect Effects 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 3
- 239000004645 polyester resin Substances 0.000 claims description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 21
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 8
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 229910001385 heavy metal Inorganic materials 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- -1 polyethylene terephthalate Polymers 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 4
- 239000001384 succinic acid Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 3
- 230000032050 esterification Effects 0.000 description 3
- 238000005886 esterification reaction Methods 0.000 description 3
- YBMRDBCBODYGJE-UHFFFAOYSA-N germanium oxide Inorganic materials O=[Ge]=O YBMRDBCBODYGJE-UHFFFAOYSA-N 0.000 description 3
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 3
- PVADDRMAFCOOPC-UHFFFAOYSA-N oxogermanium Chemical compound [Ge]=O PVADDRMAFCOOPC-UHFFFAOYSA-N 0.000 description 3
- 229920000139 polyethylene terephthalate Polymers 0.000 description 3
- 239000005020 polyethylene terephthalate Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- WXYNMTGBLWPTNQ-UHFFFAOYSA-N tetrabutoxygermane Chemical compound CCCCO[Ge](OCCCC)(OCCCC)OCCCC WXYNMTGBLWPTNQ-UHFFFAOYSA-N 0.000 description 3
- FKTHNVSLHLHISI-UHFFFAOYSA-N 1,2-bis(isocyanatomethyl)benzene Chemical compound O=C=NCC1=CC=CC=C1CN=C=O FKTHNVSLHLHISI-UHFFFAOYSA-N 0.000 description 2
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 2
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000005058 Isophorone diisocyanate Substances 0.000 description 2
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 2
- 229910052787 antimony Inorganic materials 0.000 description 2
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 150000002334 glycols Chemical class 0.000 description 2
- ACCCMOQWYVYDOT-UHFFFAOYSA-N hexane-1,1-diol Chemical compound CCCCCC(O)O ACCCMOQWYVYDOT-UHFFFAOYSA-N 0.000 description 2
- 150000002484 inorganic compounds Chemical class 0.000 description 2
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 2
- NIMLQBUJDJZYEJ-UHFFFAOYSA-N isophorone diisocyanate Chemical compound CC1(C)CC(N=C=O)CC(C)(CN=C=O)C1 NIMLQBUJDJZYEJ-UHFFFAOYSA-N 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 150000007519 polyprotic acids Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 239000005060 rubber Substances 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
- 239000002904 solvent Substances 0.000 description 2
- TYFQFVWCELRYAO-UHFFFAOYSA-N suberic acid Chemical compound OC(=O)CCCCCCC(O)=O TYFQFVWCELRYAO-UHFFFAOYSA-N 0.000 description 2
- GXMNGLIMQIPFEB-UHFFFAOYSA-N tetraethoxygermane Chemical compound CCO[Ge](OCC)(OCC)OCC GXMNGLIMQIPFEB-UHFFFAOYSA-N 0.000 description 2
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 2
- HFVMEOPYDLEHBR-UHFFFAOYSA-N (2-fluorophenyl)-phenylmethanol Chemical compound C=1C=CC=C(F)C=1C(O)C1=CC=CC=C1 HFVMEOPYDLEHBR-UHFFFAOYSA-N 0.000 description 1
- SBJCUZQNHOLYMD-UHFFFAOYSA-N 1,5-Naphthalene diisocyanate Chemical compound C1=CC=C2C(N=C=O)=CC=CC2=C1N=C=O SBJCUZQNHOLYMD-UHFFFAOYSA-N 0.000 description 1
- JPSKCQCQZUGWNM-UHFFFAOYSA-N 2,7-Oxepanedione Chemical compound O=C1CCCCC(=O)O1 JPSKCQCQZUGWNM-UHFFFAOYSA-N 0.000 description 1
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- MRLQSGZHMHONNG-UHFFFAOYSA-K P(=O)([O-])([O-])[O-].[Ge+3] Chemical compound P(=O)([O-])([O-])[O-].[Ge+3] MRLQSGZHMHONNG-UHFFFAOYSA-K 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-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
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000001361 adipic acid Substances 0.000 description 1
- 235000011037 adipic acid Nutrition 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 150000008064 anhydrides Chemical class 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
- 239000003086 colorant Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- FOTKYAAJKYLFFN-UHFFFAOYSA-N decane-1,10-diol Chemical compound OCCCCCCCCCCO FOTKYAAJKYLFFN-UHFFFAOYSA-N 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 210000003743 erythrocyte Anatomy 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000465 moulding Methods 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
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000000144 pharmacologic effect Effects 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229940014800 succinic anhydride Drugs 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- HDVLQIDIYKIVRE-UHFFFAOYSA-N tetrabutylgermane Chemical compound CCCC[Ge](CCCC)(CCCC)CCCC HDVLQIDIYKIVRE-UHFFFAOYSA-N 0.000 description 1
- ILEXMONMGUVLRM-UHFFFAOYSA-N tetraphenylgermane Chemical compound C1=CC=CC=C1[Ge](C=1C=CC=CC=1)(C=1C=CC=CC=1)C1=CC=CC=C1 ILEXMONMGUVLRM-UHFFFAOYSA-N 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- RUELTTOHQODFPA-UHFFFAOYSA-N toluene 2,6-diisocyanate Chemical compound CC1=C(N=C=O)C=CC=C1N=C=O RUELTTOHQODFPA-UHFFFAOYSA-N 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 229940045860 white wax Drugs 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Polyesters Or Polycarbonates (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、実用上十分な高分子量
をもった、少量のウレタン結合を含む飽和の脂肪族ポリ
エステル(脂環式グリコールを含む、以下単にポリエス
テルと略称する)の製造方法に関するものであり、特に
淡色が要求され、その上有害な重金属を含まないポリエ
ステルの製造にかかわるものである。The present invention relates to a process for producing a saturated aliphatic polyester having a practically sufficient high molecular weight and containing a small amount of urethane bonds (including alicyclic glycol, hereinafter simply referred to as polyester). In particular, the present invention relates to the production of a polyester which requires a light color and is free from harmful heavy metals.
【0002】[0002]
【従来の技術および課題】実用上十分な分子量をもった
ポリエチレンテレフタレートを合成する際、脱グリコー
ル反応の触媒として、チタン、亜鉛、マンガン、鉄、
鉛、アンチモン等の重金属の有機アルコキシ化合物、な
らびに有機酸の金属塩を触媒に利用することはよく知ら
れている。これらの触媒が十分な量用いられるのであれ
ば、短時間に必要な分子量迄高めることができるかも知
れず、そうであれば問題はないが、例えば食品関係に用
いられる包装材料には、これら触媒量は極力少ないこと
が望まれている。然し、ゲルマニウム化合物は活性が小
さいとの報告がみられる(例えば、朝倉書店発行“合成
高分子、第5巻”214頁参照)。反面、ゲルマニウム
化合物は、鉛、錫、アンチモン等で代表される各種重金
属が示す毒性がないとされ、例えば二酸化物は赤血球の
形成を促進する薬理作用のあることが知られている
(“ザックス”有害物質データブック、藤原鎮男監訳、
丸善株式会社出版、197頁)例もみられる。したがっ
て、ゲルマニウム化合物を用いて実用性のある高分子量
ポリエステルを合成出来るならば、食品関係の包装材料
用として頗る望ましいことが期待される。2. Description of the Related Art When synthesizing polyethylene terephthalate having a practically sufficient molecular weight, titanium, zinc, manganese, iron,
It is well known to use organic alkoxy compounds of heavy metals such as lead and antimony, and metal salts of organic acids as catalysts. If these catalysts are used in a sufficient amount, it may be possible to increase the molecular weight to the required molecular weight in a short time, and there is no problem if such a catalyst is used. It is desired that the amount be as small as possible. However, it has been reported that germanium compounds have low activity (for example, see “Synthetic Polymers, Vol. 5,” p. 214, published by Asakura Shoten). On the other hand, germanium compounds are not considered to have the toxicity shown by various heavy metals typified by lead, tin, antimony and the like, and for example, dioxide is known to have a pharmacological action to promote the formation of red blood cells ("Zachs"). Hazardous Substances Data Book, translated by Norio Fujiwara,
Maruzen Co., Ltd., p.197). Therefore, if a practical high-molecular-weight polyester can be synthesized using a germanium compound, it is expected to be very desirable for food-related packaging materials.
【0003】例えば従来から、末端基がヒドロキシル基
である分子量2,000〜2,500程度のポリエステル
を、ポリウレタン樹脂の原料成分とし、ジイソシアナー
トと反応させて、ゴム、フォーム、塗料、接着剤とする
ことは広く行われている。然し、既存のポリウレタンに
用いられるポリエステルは、分子量2,000〜2,50
0の、いわばプレポリマーであり、この低分子量ポリエ
ステル100重量部(以下重量を省略)に対して、実用
的な物性を得るためには、ジイソシアナートの分子量に
もよるが、ジイソシアナートの使用量は10部以上15
〜20部にも及ぶ必要がある。しかしながら、例えば1
0部以上のジイソシアナートを熔融ポリエステル(種類
にもよるがほぼ150℃以上)に添加すると、低分子量
ポリエステルであると、高分子量ポリエステルであると
に拘わらず、必ずゲル化して、取扱可能な樹脂は得られ
ない。実際には、10部以上のジイソシアナートの添加
は、溶剤に溶解した溶液状態で行われるか、或はフォー
ム或はRIM成形にみられるように、一度で最終硬化樹
脂を得るか、である。またゴムの場合、ヒドロキシル基
をイソシアナート基に転換し(ジイソシアナートを加え
て)、さらにグリコールで分子量を増大することも行わ
れているが、イソシアナートの量は前記のように10部
以上という多さである。このような場合、ポリエステル
の合成に重金属系の触媒を用いると、これがイソシアナ
ート基の反応性を著しく促進して、保存性不良、望まし
からざる架橋(分岐)をもたらすことから、一般にポリ
ウレタン樹脂原料の低分子量ポリエステルは、無触媒で
合成されている。従って、分子量は高くても2,500
位が限界である。For example, conventionally, a polyester having a hydroxyl group at the terminal group and having a molecular weight of about 2,000 to 2,500 has been used as a raw material component of a polyurethane resin and reacted with diisocyanate to form a rubber, foam, paint, adhesive or the like. Is widely practiced. However, the polyester used for the existing polyurethane has a molecular weight of 2,000 to 2,500.
0, a so-called prepolymer. With respect to 100 parts by weight (hereinafter, weight is omitted) of this low molecular weight polyester, in order to obtain practical physical properties, although it depends on the molecular weight of the diisocyanate, 10 to 15 copies
It needs to reach ~ 20 parts. However, for example, 1
When 0 parts or more of diisocyanate is added to the molten polyester (almost 150 ° C. or more, depending on the type), if it is a low molecular weight polyester, it always gels and can be handled regardless of the high molecular weight polyester. No resin is obtained. In practice, the addition of 10 parts or more of the diisocyanate is carried out in solution in a solvent or to obtain the final cured resin at one time, as in foam or RIM molding. . In the case of rubber, the hydroxyl group is converted to an isocyanate group (by adding diisocyanate), and the molecular weight is further increased with glycol. However, the amount of isocyanate is 10 parts or more as described above. That's a lot. In such a case, when a heavy metal-based catalyst is used in the synthesis of the polyester, it greatly promotes the reactivity of the isocyanate group, resulting in poor storage stability and undesired crosslinking (branching). The raw material low molecular weight polyester is synthesized without a catalyst. Therefore, the molecular weight is at most 2,500
Place is the limit.
【0004】[0004]
【課題を解決するための手段】本発明者らは、ゲルマニ
ウム化合物を脱グリコール反応の触媒に用いて、数平均
分子量5,000以上、望ましくは10,000以上のポ
リエステルを合成し、さらに該ポリエステルの熔融状態
で、0.01重量部以上5重量部以下のジイソシアナー
トを加えることによって、ポリエステルの分子量を2〜
5倍に高め、これによりゲルマニウム触媒の活性の乏し
さと、それに基づくポリエステルの分子量を希望の水準
迄高めることの困難な点を解消することを見出して、本
発明を完成することができた。すなわち本発明は、
(a)飽和脂肪族ポリエステル樹脂の合成過程で、生成
する樹脂100重量部に対して0.01〜3重量部のゲ
ルマニウム化合物を脱グリコール触媒として用いて、末
端基が実質的にヒドロキシル基である数平均分子量5,
000以上の飽和脂肪族ポリエステルを合成し、(b)
熔融状態の該飽和脂肪族ポリエステルに0.1〜5重量
部のジイソシアナートを加えることよりなる、数平均分
子量10,000以上のウレタン結合を含むポリエステ
ルの製造方法を提供するものである。以下、本発明をさ
らに詳細に説明する。Means for Solving the Problems The present inventors have synthesized a polyester having a number average molecular weight of 5,000 or more, preferably 10,000 or more, using a germanium compound as a catalyst for a deglycolization reaction. By adding 0.01 to 5 parts by weight of diisocyanate in the molten state of the above, the molecular weight of the polyester becomes 2 to 2.
The present invention has been completed by finding that the activity is increased by a factor of five, thereby eliminating the poor activity of the germanium catalyst and the difficulty of increasing the molecular weight of the polyester based thereon to a desired level. That is, the present invention
(A) In the course of synthesizing a saturated aliphatic polyester resin, 0.01 to 3 parts by weight of a germanium compound is used as a deglycolization catalyst with respect to 100 parts by weight of a produced resin, and the terminal group is substantially a hydroxyl group. Number average molecular weight 5,
(B) synthesizing 000 or more saturated aliphatic polyesters;
An object of the present invention is to provide a method for producing a polyester containing a urethane bond having a number average molecular weight of 10,000 or more, comprising adding 0.1 to 5 parts by weight of diisocyanate to the saturated aliphatic polyester in a molten state. Hereinafter, the present invention will be described in more detail.
【0005】(飽和ポリエステル)本発明においては、
ジイソシアナートと反応させる飽和ポリエステルは、末
端基が実質的にヒドロキシル基である、数平均分子量
5,000以上、好ましくは10.000以上の飽和ポリ
エステルでなければならない。これが低分子量ポリエス
テル、例えば数平均分子量が2,500程度であると、
本発明で利用する0.1〜5重量部のジイソシアナート
を用いても、良好な物性を有する最終樹脂を得ることが
出来ないばかりか、熔融添加にあっては、前出した0.
1〜5重量部でも、量によっては反応中にゲル化を生ず
ることが認められる等の不都合がある。したがって、末
端ヒドロキシル基の単位重量当たりの数(即ち分子の大
きさ)がほぼ30以下位でなければ、安全な反応が行え
ない。本発明の分子量5,000以上ポリエステルは必
然的にこのレベルまたは以下のヒドロキシル価であり、
少量のジイソシアナートの使用で、熔融状態といった苛
酷な条件下でも、安全に高分子量ポリエステルを合成す
ることができる。したがって、本発明でいうポリエステ
ルは、少なくとも分子量5,000当たり1個のウレタ
ン結合を含むことになる。本発明により得られる分子量
10,000以上、望ましくは20,000以上のポリエ
ステルは、融点が60℃以上で結晶性があれば、強靭な
フィルムとすることが出来、包装材料として利用するこ
とが可能である。このために用いられるグリコール類と
しては、例えばエチレングリコール、ブタンジオール
1,4、ヘキサンジオール1,6、デカメチレングリコー
ル、ネオペンチルグリコール、1,4−シクロヘキサン
ジメタノール等があげられる。エチレンオキシドも利用
することができる。これらグリコールと反応してポリエ
ステルを形成する多塩基酸(またはその酸無水物)に
は、コハク酸、アジピン酸、スベリン酸、セバシン酸、
ドデカン酸、無水コハク酸、無水アジピン酸、などが一
般に市販されており、本発明に利用することができる。
特に、ブタンジオール1,4とコハク酸(融点110〜
115℃)、ならびにエチレングリコールとコハク酸
(融点約105℃)の組合せが、ポリエチレンと類似の
融点を示し、本発明にとっては、最も望ましい組合せと
いえる。当然のことながら、目的を損なわない範囲で、
グリコール、多塩基酸相互の併用は可能である。本発明
の飽和ポリエステルは、末端基が実質的にヒドロキシル
基であるが、そのためには、合成反応に使用するグリコ
ール成分および酸成分の割合は、グルコールを幾分過剰
に使用する必要がある。ポリエステルを合成する方法は
特別なものではなく、一般にエステル化に続く脱グリコ
ール反応により高分子量化される。(Saturated polyester) In the present invention,
The saturated polyester to be reacted with the diisocyanate must be a saturated polyester having a number average molecular weight of 5,000 or more, preferably 10.000 or more, wherein the terminal groups are substantially hydroxyl groups. If this is a low molecular weight polyester, for example, the number average molecular weight is about 2500,
Even with the use of 0.1 to 5 parts by weight of the diisocyanate used in the present invention, not only is it not possible to obtain a final resin having good physical properties, but also in the case of melt addition, the aforementioned 0.1 resin is used.
Even in the case of 1 to 5 parts by weight, there is an inconvenience that gelation occurs during the reaction depending on the amount. Therefore, unless the number of terminal hydroxyl groups per unit weight (ie, the size of the molecule) is about 30 or less, a safe reaction cannot be performed. The 5,000 or higher molecular weight polyesters of the present invention necessarily have a hydroxyl number at this level or below,
By using a small amount of diisocyanate, a high molecular weight polyester can be synthesized safely even under severe conditions such as a molten state. Therefore, the polyester referred to in the present invention contains at least one urethane bond per 5,000 molecular weight. Polyester having a molecular weight of 10,000 or more, preferably 20,000 or more, obtained by the present invention can be made into a tough film as long as it has a melting point of 60 ° C. or more and is crystalline, and can be used as a packaging material. It is. Glycols used for this purpose include, for example, ethylene glycol, butanediol 1,4, hexanediol 1,6, decamethylene glycol, neopentyl glycol, 1,4-cyclohexanedimethanol and the like. Ethylene oxide can also be used. Polybasic acids (or their anhydrides) that react with these glycols to form polyesters include succinic acid, adipic acid, suberic acid, sebacic acid,
Dodecanoic acid, succinic anhydride, adipic anhydride, and the like are generally commercially available and can be used in the present invention.
In particular, butanediol 1,4 and succinic acid (melting point 110-
115 ° C.), and a combination of ethylene glycol and succinic acid (melting point about 105 ° C.) shows a melting point similar to that of polyethylene, and is the most desirable combination for the present invention. Naturally, as long as the purpose is not impaired,
Glycol and polybasic acid can be used together. In the saturated polyester of the present invention, the terminal group is substantially a hydroxyl group. For this purpose, the proportion of the glycol component and the acid component used in the synthesis reaction requires a slight excess of glycol. The method for synthesizing the polyester is not particularly limited, and is generally increased in molecular weight by a deglycolization reaction following esterification.
【0006】(触媒)本発明の飽和脂肪族ポリエステル
合成に、触媒として使用されるゲルマニウム化合物は、
無機ならびに有機の化合物があるが、実際には入手性、
コスト、安定性、などから市販されている種類は限定さ
れている。それらの例としては、例えば無機化合物では
酸化ゲルマニウム、酸性リン酸ゲルマニウムが、有機化
合物では、テトラブチルゲルマニウム、テトラフェニル
ゲルマニウム、テトラエトキシゲルマニウム、テトラブ
トキシゲルマニウムなどがあげられる。取扱性、価格、
触媒としての活性などを考慮すると、テトラエトキシゲ
ルマニウム、テトラブトキシゲルマニウム、酸化ゲルマ
ニウムなどが適当である。ゲルマニウム化合物の使用割
合は、生成する飽和脂肪族ポリエステル100重量部に
対して0.01〜3重量部、望ましくは0.5〜2重量部
である。ゲルマニウム化合物はエステル化の最初から加
えてもよく、また脱グリコール反応の直前に加えてもよ
い。(Catalyst) The germanium compound used as a catalyst in the synthesis of the saturated aliphatic polyester of the present invention is as follows:
There are inorganic and organic compounds, but in fact availability,
Commercially available types are limited due to cost, stability, and the like. Examples thereof include germanium oxide and germanium phosphate as inorganic compounds, and tetrabutylgermanium, tetraphenylgermanium, tetraethoxygermanium and tetrabutoxygermanium as organic compounds. Handling, price,
Taking into account the activity as a catalyst, tetraethoxygermanium, tetrabutoxygermanium, germanium oxide and the like are suitable. The usage ratio of the germanium compound is 0.01 to 3 parts by weight, preferably 0.5 to 2 parts by weight, based on 100 parts by weight of the saturated aliphatic polyester to be produced. The germanium compound may be added from the beginning of the esterification or may be added immediately before the deglycolization reaction.
【0007】(ジイソシアナート成分)さらに、本発明
の構成要素である生成した分子量5,000以上、望ま
しくは10,000以上の末端基が実質的にヒドロキシ
ル基であるポリエステルに、さらに分子量を高めるため
に加えられるジイソシアナート類には特に制限はない
が、例えば市販の次の種類があげられる。2,4−トリ
レンジイソシアナート、2,4−トリレンジイソシアナ
ートと2,6−トリレンジイソシアナートとの混合体、
ジフェニルメタンジイソシアナート、1,5−ナフチレ
ンジイソシアナート、キシリレンジイソシアナート、水
素化キシリレンジイソシアナート、ヘキサメチレンジイ
ソシアナート、イソホロンジイソシアナート、特に、ヘ
キサメチレンジイソシアナートが、生成樹脂の色相、ポ
リエステル添加時の反応性、などの点から好ましい。こ
れらジイソシアナートの添加量は、分子量にもよるが、
ポリエステル100部に対して0.1〜5重量部、望ま
しくは0.5〜3重量部である。添加は、ポリエステル
が均一な熔融状態で溶剤を含まず、容易に撹拌可能な条
件下で行われることが望ましい。別に、固形状のポリエ
ステルに添加し、エクストルーダーを通して熔融、混合
することも不可能ではないが、一般にはポリエステル製
造装置内か、或は熔融状態のポリエステル(例えばニー
ダー内での)に添加することが実用的である。本発明に
よる少量のウレタン結合を含むポリエステルはフィル
ム、シートなどに成形可能で、主として色装関係に利用
されるが、使用に際して滑剤、着色剤、他ポリマー、離
型剤、フィラー、補強材、などを必要に応じ使用出来る
ことは勿論である。(Diisocyanate component) Further, the molecular weight of the resulting polyester, which is a constituent element of the present invention and has a molecular weight of 5,000 or more, preferably 10,000 or more, is substantially a hydroxyl group, is further increased. The diisocyanates added for this purpose are not particularly limited, and examples thereof include the following commercially available types. 2,4-tolylene diisocyanate, a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate,
Diphenylmethane diisocyanate, 1,5-naphthylene diisocyanate, xylylene diisocyanate, hydrogenated xylylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate, particularly hexamethylene diisocyanate, the color of the formed resin It is preferable from the viewpoint of the reactivity at the time of adding the polyester. The amount of these diisocyanates depends on the molecular weight,
The amount is 0.1 to 5 parts by weight, preferably 0.5 to 3 parts by weight based on 100 parts of the polyester. The addition is desirably performed under conditions in which the polyester is in a homogeneous molten state, does not contain a solvent, and can be easily stirred. Separately, it is not impossible to add to a solid polyester and melt and mix through an extruder, but generally, it is added to a polyester manufacturing apparatus or to a molten polyester (for example, in a kneader). Is practical. The polyester containing a small amount of urethane bonds according to the present invention can be formed into films, sheets, etc., and is mainly used for coloring. However, when used, lubricants, coloring agents, other polymers, release agents, fillers, reinforcing materials, etc. Can be used if necessary.
【0008】[0008]
【実施例】次に本発明の理解を助けるために、以下に実
施例を示す。実施例 1 撹拌機、分溜コンデンサー、温度計、ガス導入管を付し
た1lセパラブルフラスコに、ブタンジオール1,4を
315g、コハク酸を348gを仕込み、190〜200
℃窒素ガス気流中にエステル化して酸価8.1とした
後、(数平均分子量約2,600)、日本化学産業
(株)社製テトラn−ブトキシゲルマニウム2gを加
え、200〜205℃で、約18時間、最終的には0.
6Torr迄減圧し、脱グリコール反応による高分子量化を
はかった。得られたポリエステル(A)の数平均分子量は
16,200室温では白色の固いワックス状で、融点は
110〜115℃であった。分子量の測定は、“Shocle
x GPC SYSTEM-11”を用い、溶離液5mM CF3COONa4HFTP
で行った。さらに、ポリエステル(A)の206℃におけ
る熔融状態で、ヘキサメチレンジイソシアナート6gを
加え、撹拌、反応させた。ゲル化は生じなかった。生成
した少量のウレタン結合を含むポリエステル(B)の数平
均分子量は33,000となった。130℃の離型剤を
塗布した熱板上に5gのポリエステル(A)ならびに(B)
を10Kg/cm2でプレス成形し、不透明な円板状に成形
し、室温で3cm×3cmに切断した。これを縦、横、5倍
づつの2軸延伸機にかけ、温度80℃で延伸したとこ
ろ、ポリエステル(A)は途中で引裂かれ、延伸フィルム
が得られなかったのに反して、ポリエステル(B)から
は、厚さ約30μの透明に延伸された強靭なフィルムが
得られ、その引張り強さは500Kg/cm2であった。EXAMPLES Next, examples will be shown below to facilitate understanding of the present invention. Example 1 315 g of butanediol 1,4 and 348 g of succinic acid were charged into a 1 liter separable flask equipped with a stirrer, a fractionating condenser, a thermometer, and a gas inlet tube, and then heated to 190 to 200.
After esterification in a nitrogen gas stream to give an acid value of 8.1 (number average molecular weight of about 2,600), 2 g of tetra-n-butoxygermanium manufactured by Nippon Kagaku Sangyo Co., Ltd. was added, and the mixture was heated at 200 to 205 ° C. About 18 hours and finally 0.1
The pressure was reduced to 6 Torr to increase the molecular weight by a glycol removal reaction. The obtained polyester (A) had a number-average molecular weight of 16,200 at room temperature and was a white hard wax, and the melting point was 110 to 115 ° C. For the measurement of molecular weight, refer to “Shocle
x GPC SYSTEM-11 ”and eluent 5mM CF 3 COONa4HFTP
I went in. Further, 6 g of hexamethylene diisocyanate was added to the polyester (A) in a molten state at 206 ° C., and the mixture was stirred and reacted. No gelling occurred. The number average molecular weight of the resulting polyester (B) containing a small amount of urethane bonds was 33,000. 5 g of polyester (A) and (B) on a hot plate coated with a release agent at 130 ° C.
Was press-molded at 10 kg / cm 2 to form an opaque disk and cut into 3 cm × 3 cm at room temperature. When this was stretched at a temperature of 80 ° C. in a biaxial stretching machine of 5 × length and width, the polyester (A) was torn in the middle and a stretched film could not be obtained. Gave a transparent stretched tough film having a thickness of about 30 μm, and its tensile strength was 500 kg / cm 2 .
【0009】実施例 2 撹拌機、分溜コンデンサー、温度計、ガス導入管を付し
た1lセパラブルフラスコに、エチレングリコール21
5g,コハク酸354g、酸化ゲルマニウム1.2gを仕込
み、195〜200℃にエステル化して酸価9.2とし
た後、温度205〜210℃で合計16時間、最終的に
は0.4Torrの減圧下で脱グリコールを行った。室温で
は白色固形のポリエステル(C)が、数平均分子量15,
000で得られた。ポリエステル(C)全体に201℃
で、ジフェニルメタンジイソシアナート5.7gを加え、
ウレタン化を行った。10分間反応後の数平均分子量
は、39,000となり、室温迄冷却すると淡黄色ワッ
クス状の少量のウレタン結合を含むポリエステル(D)が
得られた。ポリエステル(C)、ポリエステル(D)各5g
を、厚さ100μのポリエチレンテレフタレートフィル
ムにはさみ、10Kg/cm2の圧力下130℃で厚さ約1
50μの不透明な円板状に成形した。ポリエステル(C)
はこの状態で容易に手で引裂くことが出来、もろい感じ
を与えたのに反して、少量のウレタン結合を含むポリエ
ステル(D)は非常に強靭で、人手では引裂くことができ
ず、80℃の縦、横各5倍の延伸で厚さ約30μの透明
なフィルムとなり、その引張り強さは560Kg/cm2で
あった。 Example 2 Ethylene glycol 21 was placed in a 1 l separable flask equipped with a stirrer, a distillation condenser, a thermometer and a gas inlet tube.
5 g, 354 g of succinic acid and 1.2 g of germanium oxide were charged and esterified at 195 to 200 ° C. to an acid value of 9.2, and then at a temperature of 205 to 210 ° C. for a total of 16 hours, and finally a reduced pressure of 0.4 Torr. Deglycolization was performed below. At room temperature, a white solid polyester (C) has a number average molecular weight of 15,
000. 201 ° C for polyester (C)
Then, 5.7 g of diphenylmethane diisocyanate is added,
Urethane conversion was performed. After the reaction for 10 minutes, the number average molecular weight was 39,000, and upon cooling to room temperature, a light yellow wax-like polyester (D) containing a small amount of urethane bonds was obtained. 5 g each of polyester (C) and polyester (D)
Is sandwiched between polyethylene terephthalate films having a thickness of 100 μm and a thickness of about 1 at 130 ° C. under a pressure of 10 kg / cm 2.
It was formed into a 50μ opaque disk. Polyester (C)
In this state, polyester (D) containing a small amount of urethane bonds is very tough, and can not be torn by hand, while it can be easily torn by hand and gives a fragile feeling. A transparent film having a thickness of about 30 μm was obtained by stretching 5 times each in the vertical and horizontal directions at ℃, and its tensile strength was 560 kg / cm 2 .
【0010】実施例 3 撹拌機、分溜コンデンサー、温度計を付した1lセパラ
ブルフラスコに、ヘキサンジオール1,6を272g、ド
デカン酸460gを仕込み、200〜205℃、窒素気
流中でエステル化して酸価7.3とした後、日本化学産
業(社)製テトラ−n−エトキシゲルマニウムを1.5g
加え、210〜215℃で最終的には0.4Torrの減圧
とし、18時間脱グリコールを行って、数平均分子量1
6,100のポリエステル(E)が、常温では白色ワック
ス状のポリマーで得られた。融点は約80〜85℃であ
った。温度を200℃に下げ、イソホロンジイソシアナ
ートを10g加えたところ、粘度は急速に増大した。1
0分間同温度で撹拌し、少量のウレタン結合を含むポリ
エステル(F)が、分子量約45,000、室温でやや黄
味を帯びた白色ワックス状で得られた。実施例2同様、
ポリエチレンテレフタレートフィルム間で120℃、1
0Kg/cm2でプレスし、円板上、120〜130μのシ
ートを得た。ポリエステル(E)からのシートは容易に手
で引裂くことができたが、ウレタン結合を含むポリエス
テル(F)は人力では引裂くことはできなかった。5×5
倍に延伸して、透明な厚さ約30μとしたフィルムの引
張り強さは、410Kg/cm2であった。 Example 3 Into a 1 l separable flask equipped with a stirrer, a distillation condenser and a thermometer, 272 g of hexanediol 1.6 and 460 g of dodecanoic acid were charged and esterified at 200 to 205 ° C. in a nitrogen stream. After adjusting the acid value to 7.3, 1.5 g of tetra-n-ethoxygermanium manufactured by Nippon Chemical Industry Co., Ltd.
In addition, the pressure was finally reduced to 0.4 Torr at 210 to 215 ° C., and the mixture was deglycolized for 18 hours to obtain a number average molecular weight of 1
At room temperature, 6,100 polyesters (E) were obtained as white waxy polymers. Melting point was about 80-85 ° C. When the temperature was lowered to 200 ° C. and 10 g of isophorone diisocyanate was added, the viscosity increased rapidly. 1
After stirring at the same temperature for 0 minutes, a polyester (F) containing a small amount of urethane bonds was obtained as a slightly yellowish white wax at room temperature at a molecular weight of about 45,000. As in Example 2,
120 ° C, 1 between polyethylene terephthalate films
Pressing was performed at 0 kg / cm 2 to obtain a 120 to 130 μ sheet on a disk. Sheets from polyester (E) could be easily torn by hand, but polyester (F) containing urethane linkages could not be torn manually. 5x5
The tensile strength of the transparent stretched film having a thickness of about 30 μm was 410 kg / cm 2 .
【0011】[0011]
【発明の効果】本発明は上記のように構成したので、有
害な重金属を含まない高分子量のポリエステルを製造す
ることができ、食品関係の包装等に用途を拡大すること
ができる。As described above, the present invention is constructed as described above, so that high-molecular-weight polyester containing no harmful heavy metals can be produced, and its use can be expanded to food-related packaging and the like.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C08G 18/42 C08G 63/685 C08G 63/91──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) C08G 18/42 C08G 63/685 C08G 63/91
Claims (1)
成過程で、生成する樹脂100重量部に対して0.01
〜3重量部のゲルマニウム化合物を脱グリコール触媒と
して用いて、末端基が実質的にヒドロキシル基である数
平均分子量5,000以上の飽和脂肪族ポリエステルを
合成し、 (b)熔融状態の該飽和脂肪族ポリエステルに0.1〜
5重量部のジイソシアナートを加えることよりなる、数
平均分子量10,000以上のウレタン結合を含むポリ
エステルの製造方法。(1) In the process of synthesizing a saturated aliphatic polyester resin, 0.01 parts by weight based on 100 parts by weight of a resin formed.
A saturated aliphatic polyester having a number-average molecular weight of 5,000 or more whose terminal group is substantially a hydroxyl group by using 3 parts by weight of a germanium compound as a deglycolization catalyst; (b) the saturated aliphatic polyester in a molten state; Group polyester
A method for producing a polyester containing a urethane bond having a number average molecular weight of 10,000 or more, comprising adding 5 parts by weight of a diisocyanate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19681291A JP2860182B2 (en) | 1991-08-06 | 1991-08-06 | Method for producing polyester containing urethane bond |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19681291A JP2860182B2 (en) | 1991-08-06 | 1991-08-06 | Method for producing polyester containing urethane bond |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0539350A JPH0539350A (en) | 1993-02-19 |
| JP2860182B2 true JP2860182B2 (en) | 1999-02-24 |
Family
ID=16364069
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19681291A Expired - Fee Related JP2860182B2 (en) | 1991-08-06 | 1991-08-06 | Method for producing polyester containing urethane bond |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2860182B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5624730B2 (en) * | 2009-04-24 | 2014-11-12 | 株式会社日立製作所 | Polyester synthesis method and apparatus |
-
1991
- 1991-08-06 JP JP19681291A patent/JP2860182B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0539350A (en) | 1993-02-19 |
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| JPS6339913A (en) | Production of polyethylene vinyl ester polyurethane |
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