JPH0329099B2 - - Google Patents
Info
- Publication number
- JPH0329099B2 JPH0329099B2 JP23395883A JP23395883A JPH0329099B2 JP H0329099 B2 JPH0329099 B2 JP H0329099B2 JP 23395883 A JP23395883 A JP 23395883A JP 23395883 A JP23395883 A JP 23395883A JP H0329099 B2 JPH0329099 B2 JP H0329099B2
- Authority
- JP
- Japan
- Prior art keywords
- stabilizer
- pvc
- plasticizer
- dispersion
- composition
- 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
- 239000003381 stabilizer Substances 0.000 claims description 36
- 239000000203 mixture Substances 0.000 claims description 22
- 239000004014 plasticizer Substances 0.000 claims description 21
- 239000006185 dispersion Substances 0.000 claims description 20
- 238000005245 sintering Methods 0.000 claims description 14
- 239000000843 powder Substances 0.000 claims description 11
- 239000002245 particle Substances 0.000 claims description 9
- 238000002156 mixing Methods 0.000 claims description 7
- 229920005989 resin Polymers 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 5
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000011342 resin composition Substances 0.000 claims 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 claims 1
- 229920002554 vinyl polymer Polymers 0.000 claims 1
- 239000004800 polyvinyl chloride Substances 0.000 description 35
- 229920000915 polyvinyl chloride Polymers 0.000 description 35
- 238000000034 method Methods 0.000 description 7
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- -1 polyethylene Polymers 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 3
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 3
- 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 3
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- AGXUVMPSUKZYDT-UHFFFAOYSA-L barium(2+);octadecanoate Chemical compound [Ba+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O AGXUVMPSUKZYDT-UHFFFAOYSA-L 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000006084 composite stabilizer Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- OCWMFVJKFWXKNZ-UHFFFAOYSA-L lead(2+);oxygen(2-);sulfate Chemical compound [O-2].[O-2].[O-2].[Pb+2].[Pb+2].[Pb+2].[Pb+2].[O-]S([O-])(=O)=O OCWMFVJKFWXKNZ-UHFFFAOYSA-L 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 150000003606 tin compounds Chemical class 0.000 description 2
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- GGSRTHRSSCWGGK-UHFFFAOYSA-L 2,2-dibutyl-5-hydroxy-1,3,2-dioxastannepane-4,7-dione Chemical compound CCCC[Sn]1(CCCC)OC(=O)CC(O)C(=O)O1 GGSRTHRSSCWGGK-UHFFFAOYSA-L 0.000 description 1
- PRIUALOJYOZZOJ-UHFFFAOYSA-L 2-ethylhexyl 2-[dibutyl-[2-(2-ethylhexoxy)-2-oxoethyl]sulfanylstannyl]sulfanylacetate Chemical compound CCCCC(CC)COC(=O)CS[Sn](CCCC)(CCCC)SCC(=O)OCC(CC)CCCC PRIUALOJYOZZOJ-UHFFFAOYSA-L 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- UKWUOTZGXIZAJC-UHFFFAOYSA-N 4-nitrosalicylic acid Chemical compound OC(=O)C1=CC=C([N+]([O-])=O)C=C1O UKWUOTZGXIZAJC-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- XTJFFFGAUHQWII-UHFFFAOYSA-N Dibutyl adipate Chemical compound CCCCOC(=O)CCCCC(=O)OCCCC XTJFFFGAUHQWII-UHFFFAOYSA-N 0.000 description 1
- 241000156978 Erebia Species 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001278 adipic acid derivatives Chemical class 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- CEGOLXSVJUTHNZ-UHFFFAOYSA-K aluminium tristearate Chemical compound [Al+3].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CEGOLXSVJUTHNZ-UHFFFAOYSA-K 0.000 description 1
- 229940063655 aluminum stearate Drugs 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- ZFMQKOWCDKKBIF-UHFFFAOYSA-N bis(3,5-difluorophenyl)phosphane Chemical compound FC1=CC(F)=CC(PC=2C=C(F)C=C(F)C=2)=C1 ZFMQKOWCDKKBIF-UHFFFAOYSA-N 0.000 description 1
- GWOWVOYJLHSRJJ-UHFFFAOYSA-L cadmium stearate Chemical compound [Cd+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O GWOWVOYJLHSRJJ-UHFFFAOYSA-L 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- HIAAVKYLDRCDFQ-UHFFFAOYSA-L calcium;dodecanoate Chemical compound [Ca+2].CCCCCCCCCCCC([O-])=O.CCCCCCCCCCCC([O-])=O HIAAVKYLDRCDFQ-UHFFFAOYSA-L 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- UQLDLKMNUJERMK-UHFFFAOYSA-L di(octadecanoyloxy)lead Chemical compound [Pb+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O UQLDLKMNUJERMK-UHFFFAOYSA-L 0.000 description 1
- 229940100539 dibutyl adipate Drugs 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- UMKARVFXJJITLN-UHFFFAOYSA-N lead;phosphorous acid Chemical compound [Pb].OP(O)O UMKARVFXJJITLN-UHFFFAOYSA-N 0.000 description 1
- HGPXWXLYXNVULB-UHFFFAOYSA-M lithium stearate Chemical compound [Li+].CCCCCCCCCCCCCCCCCC([O-])=O HGPXWXLYXNVULB-UHFFFAOYSA-M 0.000 description 1
- 235000019359 magnesium stearate Nutrition 0.000 description 1
- 229940049920 malate Drugs 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N malic acid Chemical compound OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- SJOCPYUKFOTDAN-ZSOIEALJSA-N methyl (4z)-4-hydroxyimino-6,6-dimethyl-3-methylsulfanyl-5,7-dihydro-2-benzothiophene-1-carboxylate Chemical compound C1C(C)(C)C\C(=N\O)C=2C1=C(C(=O)OC)SC=2SC SJOCPYUKFOTDAN-ZSOIEALJSA-N 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- ZMHZSHHZIKJFIR-UHFFFAOYSA-N octyltin Chemical compound CCCCCCCC[Sn] ZMHZSHHZIKJFIR-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 150000003021 phthalic acid derivatives Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
本発明は焼結用塩化ビニル系樹脂(以下PVC
ということがある)組成物の製造法に関し、更に
詳しくは安定剤が均一に分散した熱安定性に優れ
た焼結用PVC組成物の製造法に関するものであ
る。
従来、粉末樹脂を直接加熱して成形する方法は
フエノール樹脂等の熱硬化性樹脂、ポリエチレン
等の熱可塑性樹脂でかなり広範に利用されている
が、PVCではその原料供給形態が粉体であるに
もかかわらず、ペースト用PVCを使用した流動
浸漬法による塗膜成形等が極く部分的に実施され
ているにすぎない。なぜなら、硬質PVCの場合
は粒子間の融着を図るために高熱と高圧を加えね
ばならず、このためPVCの熱分解や生産性の低
下をきたすばかりでなく、得られた成形品の物性
も極めて低いからである。
また、重合度の低いPVCが酢酸ビニル等の共
重合された低軟化点のPVCを使用し、可塑剤を
大量に添加すれば、当然加熱時の溶融流動性は改
良され、粉末の加熱、加圧等による焼結は可能と
なる。しかし、PVC粉末の焼結においては機械
的混練を行わないので、安定剤の分散が不均一と
なりがちであり、そのため、加熱成形時の熱安定
性が問題となる。
従つて、熱安定性を向上させるべく、安定剤を
極力均一分散させることが重要であり、そのため
一般的には液状安定剤を用いて分散不良を防止す
る方法がとられている。ところが液状安定剤は、
臭気、揮発性、熱老化性等の点で不都合なため高
融点の安定剤を使うことが好ましいとされてい
る。
そこで本発明者は、熱安定性の優れた焼結用
PVC組成物を得るために、高融点の安定剤をよ
り均一分散させる方法について検討を重ねた結
果、安定剤を特定の分散液としてPVCに特定の
温度で混合することによつて所期の目的が達成さ
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、PVC粉末に固形安定剤及
び可塑剤を添加混合して焼結用組成物を製造する
に際し、該安定剤をその平均粒径が30μ以下とな
るよう調整した可塑剤分散液としてPVC粉末に
添加混合することを特徴とする焼結用PVC組成
物の製造法を提供するものである。
本発明における焼結用組成物の成分として用い
られるPVC粉末とは、塩化ビニルの単独重合体
又は塩化ビニル50重量%以上と他の共重合可能な
単量体、例えば酢酸ビニル、エチレン等50重量%
以下との共重合体の粉末のことである。これらの
PVCと他の合成樹脂との混合体であつて、PVC
部分が50重量%以上の粉末状樹脂混合体も同様に
用いることができる。PVCの重合度は特には限
定されず、本発明の組成物の焼結条件あるいは使
用条件等により選択すればよいが、通常平均重合
度で500〜1500、好ましくは700〜1000程度のもの
が使用しやすい。また、その粉末の粒径および粒
径分布も限定されるものではなく、通常40〜300
メツシユ、好ましくは80〜200メツシユのものが
使用しやすい。
本発明においては、焼結性組成物の一成分とし
て、一般のPVC用可塑剤が使用される。その具
体例として、ジオクチルフタレート、ジブチルフ
タレートのようなフタル酸エステル類、ジオクチ
ルアジペート、ジブチルアジペートのようなアジ
ピン酸エステル類、トリクレジルフオスフエート
のようなリン酸エステル類、オレイン酸、トリメ
リツト酸、セバチン酸等の有機酸の高級アルコー
ルエステル類等が挙げられる。可塑剤の添加量は
通常はPVC100重量部(PHR)に対して30〜
130PHRである。30PHR未満では焼結温度を高
くする必要があり、樹脂の熱安定性の問題から好
ましくなく、また130PHRを越えると配合成分を
混合、撹拌する際、組成物の凝集あるいはブロツ
キング等の不都合が生じる。
本発明における固形安定剤の可塑剤への分散液
を調製する方法は、要するに安定剤の平均粒径が
30μ以下、好ましくは15μ以下となるような方法
であれば特に制限されない。例えば、あらかじめ
リボンブレンダー、バタフライミキサー等で固形
安定剤と可塑剤とを混合し、インクミルで強制分
散させる方法、安定剤をハンマーミル、ジエツト
ミル、ボールミル、ローラーミル等で粉砕したの
ち、混合機中で可塑剤と混合しインクミルで強制
分散させる方法などを採用することができる。安
定剤の平均粒径が30μを越える状態の分散液とし
てPVCに添加しても均一分散が不十分なため熱
安定性の改良効果は乏しい。
固形安定剤としては通常のPVC用のものであ
れば特に制限されず、例えば、ステアリン酸リチ
ウム、ステアリン酸マグネシウム、ステアリン酸
アルミニウム、ステアリン酸カルシウム、ラウリ
ン酸カルシウム、ステアリン酸バリウム、ラウリ
ン酸バリウム、ステアリン酸亜鉛、ステアリン酸
カドミウム、ステアリン酸鉛、二塩基性ステアリ
ン酸鉛などの金属石けん;三塩基性硫酸鉛、塩基
性亜硫酸鉛、二塩基性亜りん酸鉛などの無機酸
塩;ジブチル錫マレート、オクチル錫マレート、
ジブチル錫メルカプチド、重合有機錫化合物など
の有機錫化合物;及び二種以上を組合せた複合安
定剤などが挙げられる。
安定剤の分散媒として使用される可塑剤の種類
は限定されないが、均一分散性の点からは、
PVC組成物成分として使用される可塑剤と同じ
ものが好ましく、その具体例は前掲のとおりであ
る。
安定剤の濃度は可塑剤分散液中、通常は5〜90
重量%とされる。90重量%を越えると粘度が上が
るため可塑剤への均質分散が不完全となり、5重
量%未満では分散液の粘度が低いため、インクミ
ルによる粉砕が困難で、安定剤が分離凝集して分
散不良となり熱安定性が低下する。
得られた安定剤分散液のPVCへと添加は通常
可塑剤の添加前に行われる。その添加部数は、通
常PVC100PHR当たり安定剤量として1〜
10PHR好ましくは1.5〜5PHR程度である。また、
この分散液のPVCへの添加温度は安定剤の融点
以下とすることが必要である。融点を越えると
PVCへの安定剤の吸収が急激過ぎて部分的なむ
らが発生し均一分散がむずかしい。ただし安定剤
分散液がPVCに均一分散した後、可塑剤を添加
する際は、組成物の凝集、ブロツキングが生じな
いような温度、一般には80℃以上とすることが好
ましい。この温度未満では、安定剤が可塑剤と共
にPVC中に吸収されにくいため熱安定性の向上
効果が少ない。
また安定剤分散液及び可塑剤のPVCへの添加
混合は、ヘンシエルミキサー、リボンブレンダー
等通常の混合機を用いて行われる。混合時間は回
転速度、温度、機械的条件により異なるが、通常
は5〜60分程度である。なお、PVC、安定剤分
散液、可塑剤の他に、所望により通常の充てん
剤、難燃剤、老化防止剤、紫外線吸収剤、安定化
助剤、顔料等を適宜使用できることはもちろんで
ある。
この様にして得られる本発明の組成物の焼結方
法は特に限定されるものではなく、(1)流動浸漬法
による被膜の形成、(2)平滑なベルト状スチール上
に本組成物を均一に散布し加熱炉の中を通すこと
による軟質PVCシートの成形、(3)フエルト上に
本組成物を散布し加熱炉を通して溶融させること
による積層シートの成形、(4)本組成物を直接加熱
した金型に散布することによる型物の成形等各種
の成形方法が適用可能である。なお、焼結成形に
あたつては、加圧しなくても成形は可能である
が、特に表面の平滑性、エンボス模様等を要求す
る際には若干の加圧を行えばよくまたそれによつ
て成形温度の低下溶融時間の短縮も可能となる。
成形条件は通常150〜300℃で数秒〜20分程度の範
囲内で成形品の形状、組成物の溶融性等により選
択される。300℃を越えた温度で成形すると、
PVCの熱安定性に問題が生じる場合がある。
以下実施例にもとずき、本発明を説明する。な
お、配合成分の部数及び%は重量基準である。
実施例 1
平均粒径75μのステアリン酸バリウム/ステア
リン酸亜鉛(70/30)複合安定剤をバタフライミ
キサーに投入し、次いで安定剤濃度が10、20及び
50%となるようジオクチルフタレートを投入して
混合した後、採り出して50〜60℃のインクミルで
安定剤を粉砕し混合することによつてペースト状
の分散液を得た。この際の安定剤の粒径はインク
ミルによる通し回数で調節した。
次にポリ塩化ビニル(平均重合度700)100部、
上記で得られた安定剤分散液を安定剤として3部
及びエポキシ化大豆油5部を20ヘンシエルミキ
サーに30℃で投入して混合撹拌し、100℃に昇温
したときジオクチルフタレート60部を徐々に添加
し、120℃まで昇温した後50℃に冷却することに
よつてPVC組成物を得た。
この組成物を2mmのアルミ板上に散布し、ドク
ターブレードで2mm厚に調整し230℃オーブン中
で10分間焼結し、5cm2中に発生した黒点の数で熱
安定性を評価した。結果を第1表に示す。なお、
安定剤を可塑剤分散液としない場合(実験番号
7、8)の結果も併記する。
The present invention is based on polyvinyl chloride resin (hereinafter referred to as PVC) for sintering.
The present invention relates to a method for producing a composition, and more specifically to a method for producing a PVC composition for sintering that has a uniformly dispersed stabilizer and has excellent thermal stability. Conventionally, the method of directly heating and molding powdered resin has been widely used for thermosetting resins such as phenolic resin and thermoplastic resins such as polyethylene, but for PVC, the raw material supply form is powder. However, coating film formation using the fluidized dipping method using PVC for paste has only been carried out in a limited number of areas. This is because in the case of hard PVC, high heat and high pressure must be applied to fuse the particles, which not only causes thermal decomposition of the PVC and decreases productivity, but also deteriorates the physical properties of the resulting molded product. This is because it is extremely low. In addition, if PVC with a low degree of polymerization is copolymerized with vinyl acetate or other low softening point PVC, and if a large amount of plasticizer is added, the melt flowability during heating will naturally be improved, and the heating and processing of the powder will improve. Sintering by pressure etc. becomes possible. However, since mechanical kneading is not performed in the sintering of PVC powder, the dispersion of the stabilizer tends to be non-uniform, and therefore thermal stability during hot molding becomes a problem. Therefore, in order to improve thermal stability, it is important to disperse the stabilizer as uniformly as possible, and for this reason, a method is generally used to prevent poor dispersion by using a liquid stabilizer. However, liquid stabilizers
It is said that it is preferable to use a stabilizer with a high melting point because it is disadvantageous in terms of odor, volatility, heat aging, etc. Therefore, the inventor developed a sintering material with excellent thermal stability.
In order to obtain a PVC composition, we have repeatedly investigated ways to more uniformly disperse a stabilizer with a high melting point. By mixing the stabilizer as a specific dispersion into PVC at a specific temperature, it is possible to achieve the desired purpose. The inventors have discovered that this can be achieved and have arrived at the present invention. That is, the present invention, when producing a sintering composition by adding and mixing a solid stabilizer and a plasticizer to PVC powder, uses the stabilizer as a plasticizer dispersion in which the average particle size is adjusted to be 30μ or less. The present invention provides a method for producing a PVC composition for sintering, which is characterized in that it is added to and mixed with PVC powder. The PVC powder used as a component of the sintering composition in the present invention is a homopolymer of vinyl chloride or 50% by weight or more of vinyl chloride and other copolymerizable monomers, such as vinyl acetate, ethylene, etc. %
It is a powder of a copolymer with: these
A mixture of PVC and other synthetic resins, PVC
Powdered resin mixtures with a fraction of 50% or more by weight can likewise be used. The degree of polymerization of PVC is not particularly limited and may be selected depending on the sintering conditions or usage conditions of the composition of the present invention, but the average degree of polymerization used is usually about 500 to 1500, preferably about 700 to 1000. It's easy to do. In addition, the particle size and particle size distribution of the powder are not limited, and are usually 40 to 300.
A mesh of 80 to 200 mesh is easy to use. In the present invention, a general plasticizer for PVC is used as one component of the sinterable composition. Specific examples include phthalic acid esters such as dioctyl phthalate and dibutyl phthalate, adipic acid esters such as dioctyl adipate and dibutyl adipate, phosphoric acid esters such as tricresyl phosphate, oleic acid, and trimellitic acid. , higher alcohol esters of organic acids such as sebacic acid, and the like. The amount of plasticizer added is usually 30 to 100 parts by weight (PHR) of PVC.
It is 130PHR. If it is less than 30 PHR, it is necessary to raise the sintering temperature, which is undesirable due to problems with the thermal stability of the resin, and if it exceeds 130 PHR, problems such as agglomeration or blocking of the composition will occur when the ingredients are mixed and stirred. In short, the method for preparing a dispersion of a solid stabilizer in a plasticizer in the present invention is such that the average particle size of the stabilizer is
There are no particular limitations as long as the method results in a thickness of 30μ or less, preferably 15μ or less. For example, the solid stabilizer and plasticizer are mixed in advance using a ribbon blender, butterfly mixer, etc. and forcedly dispersed using an ink mill, or the stabilizer is pulverized using a hammer mill, jet mill, ball mill, roller mill, etc., and then mixed in a mixer. A method such as mixing with a plasticizer and forcibly dispersing it with an ink mill can be adopted. Even if the stabilizer is added to PVC in the form of a dispersion with an average particle size of more than 30μ, the effect of improving thermal stability is poor because uniform dispersion is insufficient. The solid stabilizer is not particularly limited as long as it is used for ordinary PVC, and examples include lithium stearate, magnesium stearate, aluminum stearate, calcium stearate, calcium laurate, barium stearate, barium laurate, and zinc stearate. , metallic soaps such as cadmium stearate, lead stearate, and dibasic lead stearate; inorganic acid salts such as tribasic lead sulfate, basic lead sulfite, and dibasic lead phosphite; dibutyltin malate, octyltin malate,
Examples include organic tin compounds such as dibutyltin mercaptide and polymerized organic tin compounds; and composite stabilizers in which two or more types are combined. The type of plasticizer used as a dispersion medium for the stabilizer is not limited, but from the point of view of uniform dispersibility,
The same plasticizers as those used as components of the PVC composition are preferred, specific examples of which are listed above. The concentration of stabilizer in the plasticizer dispersion is usually between 5 and 90
% by weight. If it exceeds 90% by weight, the viscosity will increase and homogeneous dispersion into the plasticizer will be incomplete, and if it is less than 5% by weight, the viscosity of the dispersion will be low, making it difficult to grind with an ink mill, and the stabilizer will separate and coagulate, resulting in poor dispersion. As a result, thermal stability decreases. Addition of the resulting stabilizer dispersion to the PVC is usually carried out before addition of the plasticizer. The number of parts added is usually 1 to 1 as the amount of stabilizer per 100 PHR of PVC.
It is about 10 PHR, preferably about 1.5 to 5 PHR. Also,
The temperature at which this dispersion is added to PVC needs to be below the melting point of the stabilizer. When the melting point is exceeded
The absorption of the stabilizer into PVC is too rapid, causing local unevenness and making uniform dispersion difficult. However, when adding a plasticizer after the stabilizer dispersion is uniformly dispersed in PVC, it is preferable to maintain the temperature at a temperature that does not cause aggregation or blocking of the composition, generally 80° C. or higher. Below this temperature, the stabilizer and the plasticizer are not easily absorbed into the PVC, so the effect of improving thermal stability is small. Further, the stabilizer dispersion and the plasticizer are added and mixed to the PVC using a conventional mixer such as a Henschel mixer or a ribbon blender. The mixing time varies depending on the rotation speed, temperature, and mechanical conditions, but is usually about 5 to 60 minutes. In addition to PVC, the stabilizer dispersion, and the plasticizer, it is of course possible to use ordinary fillers, flame retardants, anti-aging agents, ultraviolet absorbers, stabilizing aids, pigments, etc. as desired. The method of sintering the composition of the present invention obtained in this way is not particularly limited. (3) Forming a laminated sheet by spreading the composition on felt and melting it through a heating furnace; (4) Directly heating the composition. Various molding methods can be applied, such as molding a molded article by spraying the powder onto a mold. It should be noted that sintering can be performed without applying pressure, but if a smooth surface, embossed pattern, etc. are required, a slight amount of pressure may be sufficient. It is also possible to lower the molding temperature and shorten the melting time.
The molding conditions are usually 150 to 300° C. and several seconds to 20 minutes, and are selected depending on the shape of the molded product, the meltability of the composition, etc. When molded at temperatures exceeding 300℃,
Problems may arise with the thermal stability of PVC. The present invention will be explained below based on Examples. Note that the parts and percentages of the ingredients are based on weight. Example 1 A barium stearate/zinc stearate (70/30) composite stabilizer with an average particle size of 75μ was charged into a butterfly mixer, and then stabilizer concentrations of 10, 20 and
After adding and mixing dioctyl phthalate to give a concentration of 50%, the mixture was taken out, and the stabilizer was crushed in an ink mill at 50 to 60°C and mixed to obtain a paste-like dispersion. The particle size of the stabilizer at this time was adjusted by the number of times the ink was passed through the ink mill. Next, 100 parts of polyvinyl chloride (average degree of polymerization 700),
3 parts of the stabilizer dispersion obtained above as a stabilizer and 5 parts of epoxidized soybean oil were mixed and stirred in a 20 Henschel mixer at 30°C, and when the temperature was raised to 100°C, 60 parts of dioctyl phthalate was added. A PVC composition was obtained by gradually adding the mixture, raising the temperature to 120°C, and then cooling it to 50°C. This composition was spread on a 2 mm aluminum plate, adjusted to a thickness of 2 mm using a doctor blade, and sintered in an oven at 230°C for 10 minutes, and thermal stability was evaluated by the number of black spots generated in 5 cm 2 . The results are shown in Table 1. In addition,
The results when the stabilizer is not a plasticizer dispersion (experiment numbers 7 and 8) are also shown.
【表】
に混合した。
実施例 2
安定剤として三塩基性硫酸鉛、可塑剤としてト
リメリツト酸エステル(アデカ・アーガス化学(株)
製、アデカサイザーC−8)を用いたほかは実施
例1と同様の実験を行つた。結果を第2表に示
す。[Table]
Example 2 Tribasic lead sulfate as a stabilizer and trimellitic acid ester as a plasticizer (Adeka Argus Chemical Co., Ltd.)
The same experiment as in Example 1 was conducted except that Adekasizer C-8 (manufactured by Adekasizer C-8) was used. The results are shown in Table 2.
【表】
に混合した。
[Table]
Claims (1)
剤を添加混合して焼結用組成物を製造するに際
し、該安定剤をその平均粒径が30μ以下となるよ
う調整した可塑剤分散液として塩化ビニル系樹脂
粉末に添加混合することを特徴とする焼結用塩化
ビニル系樹脂組成物の製造法。1. When producing a sintering composition by adding and mixing a solid stabilizer and a plasticizer to vinyl chloride resin powder, the stabilizer is chlorinated as a plasticizer dispersion adjusted to have an average particle size of 30μ or less. A method for producing a vinyl chloride resin composition for sintering, which comprises adding and mixing it to vinyl resin powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23395883A JPS60124628A (en) | 1983-12-12 | 1983-12-12 | Manufacturing method of vinyl chloride resin composition for sintering |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23395883A JPS60124628A (en) | 1983-12-12 | 1983-12-12 | Manufacturing method of vinyl chloride resin composition for sintering |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60124628A JPS60124628A (en) | 1985-07-03 |
| JPH0329099B2 true JPH0329099B2 (en) | 1991-04-23 |
Family
ID=16963287
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23395883A Granted JPS60124628A (en) | 1983-12-12 | 1983-12-12 | Manufacturing method of vinyl chloride resin composition for sintering |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60124628A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2513461B2 (en) * | 1985-10-30 | 1996-07-03 | 日瀝化学工業 株式会社 | Bituminous vinyl chloride resin composition and method for producing the same |
-
1983
- 1983-12-12 JP JP23395883A patent/JPS60124628A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60124628A (en) | 1985-07-03 |
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