JPH02206636A - Resin composition for cleaning - Google Patents
Resin composition for cleaningInfo
- Publication number
- JPH02206636A JPH02206636A JP1024061A JP2406189A JPH02206636A JP H02206636 A JPH02206636 A JP H02206636A JP 1024061 A JP1024061 A JP 1024061A JP 2406189 A JP2406189 A JP 2406189A JP H02206636 A JPH02206636 A JP H02206636A
- Authority
- JP
- Japan
- Prior art keywords
- cleaning
- resin
- resin composition
- carboxylic acid
- 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.)
- Granted
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 40
- 239000011342 resin composition Substances 0.000 title claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 33
- 150000001875 compounds Chemical class 0.000 claims abstract description 12
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 11
- 239000002253 acid Substances 0.000 claims abstract description 10
- 230000007935 neutral effect Effects 0.000 claims abstract description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 6
- -1 Pentaerythritol tetracarboxylic acid ester Chemical class 0.000 claims description 24
- 239000004793 Polystyrene Substances 0.000 claims description 16
- 229920002223 polystyrene Polymers 0.000 claims description 16
- 239000004698 Polyethylene Substances 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 229920000573 polyethylene Polymers 0.000 claims description 6
- 239000004327 boric acid Substances 0.000 claims description 3
- 159000000007 calcium salts Chemical class 0.000 claims description 3
- 229920002545 silicone oil Polymers 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 claims 2
- 239000000155 melt Substances 0.000 claims 1
- 229920006351 engineering plastic Polymers 0.000 abstract description 5
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 abstract 2
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 abstract 1
- 235000011187 glycerol Nutrition 0.000 abstract 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 abstract 1
- 229920005989 resin Polymers 0.000 description 28
- 239000011347 resin Substances 0.000 description 28
- 238000001746 injection moulding Methods 0.000 description 16
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 12
- 239000006229 carbon black Substances 0.000 description 8
- 239000004721 Polyphenylene oxide Substances 0.000 description 7
- 229920000139 polyethylene terephthalate Polymers 0.000 description 7
- 239000005020 polyethylene terephthalate Substances 0.000 description 7
- 229920006380 polyphenylene oxide Polymers 0.000 description 7
- 235000019359 magnesium stearate Nutrition 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 238000005520 cutting process Methods 0.000 description 4
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- OCKWAZCWKSMKNC-UHFFFAOYSA-N [3-octadecanoyloxy-2,2-bis(octadecanoyloxymethyl)propyl] octadecanoate Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(COC(=O)CCCCCCCCCCCCCCCCC)(COC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC OCKWAZCWKSMKNC-UHFFFAOYSA-N 0.000 description 3
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229930182556 Polyacetal Natural products 0.000 description 2
- 239000004734 Polyphenylene sulfide Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical class OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 229920001519 homopolymer Polymers 0.000 description 2
- 229920006324 polyoxymethylene Polymers 0.000 description 2
- 229920000069 polyphenylene sulfide Polymers 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- LDMOEFOXLIZJOW-UHFFFAOYSA-N 1-dodecanesulfonic acid Chemical compound CCCCCCCCCCCCS(O)(=O)=O LDMOEFOXLIZJOW-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
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- QHZLMUACJMDIAE-UHFFFAOYSA-N Palmitic acid monoglyceride Natural products CCCCCCCCCCCCCCCC(=O)OCC(O)CO QHZLMUACJMDIAE-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- VBICKXHEKHSIBG-UHFFFAOYSA-N beta-monoglyceryl stearate Natural products CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 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
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- OOCMUZJPDXYRFD-UHFFFAOYSA-L calcium;2-dodecylbenzenesulfonate Chemical compound [Ca+2].CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O.CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O OOCMUZJPDXYRFD-UHFFFAOYSA-L 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- OQXSVLMHUIVNRJ-UHFFFAOYSA-L magnesium;2-dodecylbenzenesulfonate Chemical compound [Mg+2].CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O.CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O OQXSVLMHUIVNRJ-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000010137 moulding (plastic) Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 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
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- VLCLHFYFMCKBRP-UHFFFAOYSA-N tricalcium;diborate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]B([O-])[O-].[O-]B([O-])[O-] VLCLHFYFMCKBRP-UHFFFAOYSA-N 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/37—Polymers
- C11D3/3746—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C11D3/3749—Polyolefins; Halogenated polyolefins; Natural or synthetic rubber; Polyarylolefins or halogenated polyarylolefins
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/02—Anionic compounds
- C11D1/12—Sulfonic acids or sulfuric acid esters; Salts thereof
- C11D1/22—Sulfonic acids or sulfuric acid esters; Salts thereof derived from aromatic compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、熱可塑性樹脂の成形機における、樹脂切り酔
え時に使用する洗浄用樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a cleaning resin composition for use in a thermoplastic resin molding machine when the resin gets sick.
プラスチックの成形加工において、品種切り替えの際に
は、先行品種の影響を排除するために幾つかの処置が取
られている。In plastic molding and processing, when changing products, several measures are taken to eliminate the influence of the previous product.
特に着色品の加工では、青色、黒色などの濃色系のグレ
ードから白色などの淡色系のグレードに切り替えの際に
、成形機の分解掃除、洗浄用樹脂による成形機内の洗浄
などの煩雑な作業と、これに伴う生産停止を余儀なくさ
れるのが実情である。Particularly in the processing of colored products, when switching from dark-colored grades such as blue and black to light-colored grades such as white, complicated work such as disassembling and cleaning the molding machine and cleaning the inside of the molding machine with cleaning resin is required. The reality is that we are forced to suspend production due to this.
例えば押出造粒成形における切り替えの場合、押出機を
停止し、スクリューを抜き出した後、スクリュー及びシ
リンダー内部をブラッシング等の方法で清浄にして、再
びスクリューを組み込む等の作業が必要である。スクリ
ューを抜かずに樹脂を使用して先行品種を置換する処置
では、洗浄に多階の樹脂を要し、また押出機内部の複雑
な構造部の汚れが除去できないために後続する樹脂に着
色が生じるなどの問題がある。これらの問題を解消する
方法として、洗浄用コンパウンドで押出機内部の残留物
を除去しやすくして少量の置換用樹脂の使用で品種切り
替えをする方法がある。For example, when changing extrusion granulation molding, it is necessary to stop the extruder, remove the screw, clean the inside of the screw and cylinder by brushing, etc., and then reinstall the screw. Using resin to replace the preceding product without removing the screw requires multiple layers of resin for cleaning, and the inability to remove dirt from the complex structure inside the extruder may result in coloring of the subsequent resin. There are problems such as the occurrence of One way to solve these problems is to use a cleaning compound to easily remove the residue inside the extruder, and use a small amount of replacement resin to change product types.
本発明者らは、先に特開昭62−195045月公報に
よって、熱可塑性樹脂、アルキルベンゼンスルホン酸中
性塩及びはつ水化合物からなる熱硬化性樹脂組成物が洗
浄能力が優れていることを開示している。The present inventors previously discovered in Japanese Unexamined Patent Publication No. 1985-1950 that a thermosetting resin composition consisting of a thermoplastic resin, a neutral salt of alkylbenzenesulfonic acid, and a water-repellent compound has excellent cleaning ability. Disclosed.
ポリフェニレンオキサイド、ボリフエニレンサルフフイ
ド、ポリブチルテレフタレート、ふっ素樹脂、ナイロン
等の高温度で加工するエンジニアリングプラスチックの
品種切り替えでは、従来のものより更に洗浄能力の優れ
たコンパウンドの開発が必要である。When changing types of engineering plastics that are processed at high temperatures, such as polyphenylene oxide, polyphenylene sulfide, polybutyl terephthalate, fluororesin, and nylon, it is necessary to develop compounds with even better cleaning performance than conventional ones.
本発明の目的は、生態の置換用樹脂を使用することによ
り、高温度で加工するエンジニアリングプラスチックの
成形機内に残存する先行品種の除去を簡単な操作で達成
できるような洗浄用樹脂組成物を提供することである。An object of the present invention is to provide a cleaning resin composition that uses an ecological replacement resin to allow removal of previous products remaining in a molding machine for engineering plastics processed at high temperatures with a simple operation. It is to be.
本発明者らは、成形機の洗浄方法を種々検討した結果、
ポリスチレン、アルキルベンゼンスルホン酸中性塩に加
えて離型性化合物を混合して造粒した組成物が高温度で
優れた洗浄能力を有することを見い出し本発明を完成し
た。As a result of various studies on cleaning methods for molding machines, the present inventors found that
The present invention was completed based on the discovery that a granulated composition obtained by mixing polystyrene, a neutral salt of alkylbenzenesulfonic acid, and a mold release compound has excellent cleaning ability at high temperatures.
すなわち本発明は、ポリスチレンにアルキルベンゼンス
ルホン酸中性塩及び離型性化合物を配合してなる組成物
を含む洗浄用樹脂組成物である。That is, the present invention is a cleaning resin composition containing a composition in which polystyrene is blended with a neutral salt of alkylbenzenesulfonic acid and a mold release compound.
配合割合としては、ポリスチレン50〜95重量%に、
アルキルベンゼンスルホン酸中性塩2〜40重量%及び
離型性化合物1.5〜15遁臘%を配合してなる組成物
を含む洗浄用樹脂組成物である。The blending ratio is 50 to 95% by weight of polystyrene,
A cleaning resin composition containing 2 to 40% by weight of a neutral salt of alkylbenzenesulfonic acid and 1.5 to 15% by weight of a releasing compound.
ポリスチレンとしては、メルトフローインデックス(!
?/10分)(JISK6870)が7.0以下のもの
が好ましい。7.0を超えると流動性が強すぎて、先行
エンジニアリングプラスチックの剥離が困難になり好ま
しくない。For polystyrene, melt flow index (!
? /10 minutes) (JISK6870) is preferably 7.0 or less. If it exceeds 7.0, the fluidity will be too strong and it will be difficult to peel off the preceding engineering plastic, which is not preferable.
離型性化合物としては、200℃以上のFi4温度で分
解または揮発しないものが好ましくカルボン酸の炭素数
が10〜22のペンタエリスリトールテトラカルボン酸
エステル、カルボン酸の炭素数が12〜22のカルボン
酸モノグリセライドのホウ酸エステル、カルボン酸の炭
素数が12〜22のカルボン酸モノグリセライドのホウ
酸エステルのカルシウム塩、ポリエチレンワックス、シ
リコンオイルからなる群より選んで1種又は2種以上を
挙げることができる。The releasing compound is preferably one that does not decompose or volatilize at a Fi4 temperature of 200°C or higher, such as pentaerythritol tetracarboxylic acid ester in which the carboxylic acid has 10 to 22 carbon atoms, or a carboxylic acid in which the carboxylic acid has 12 to 22 carbon atoms. One or more types selected from the group consisting of boric acid esters of monoglycerides, calcium salts of boric acid esters of carboxylic acid monoglycerides whose carboxylic acid has 12 to 22 carbon atoms, polyethylene wax, and silicone oil can be mentioned.
本発明の組成物に使用するアルキルベンゼンスルホン酸
中性塩としては、ナトリウム塩、カリウム塩、マグネシ
ウム塩、カルシウム塩を挙げることができる。アルキル
ベンゼンスルホン酸中性塩の使用量は2〜40重量%が
好ましい。The neutral salts of alkylbenzenesulfonic acids used in the compositions of the present invention include sodium salts, potassium salts, magnesium salts, and calcium salts. The amount of the neutral salt of alkylbenzenesulfonic acid used is preferably 2 to 40% by weight.
2重間%未満では、高温度における洗浄能力が小さく、
40重量%を超える使用量では流動性が強すきで、先行
エンジニアリングプラスチックの剥離が困難になり好ま
しくない。If the ratio is less than 2%, the cleaning ability at high temperatures will be small;
If the amount used exceeds 40% by weight, the fluidity will be too strong and it will be difficult to peel off the preceding engineering plastic, which is not preferable.
本発明の組成物には、MS樹脂、MBS樹脂、ABSs
l脂、As樹脂、BS樹脂等のスブレン系コポリマーを
含有することができる。また炭酸カルシウム、タルク、
シリカ、アルミナ、ガラス繊維等の無機充填剤を加える
ことができる。更にステアリン酸マグネシウム、ステア
リン酸カルシウム、ステアリン酸亜鉛等の金属石鹸類、
ビスフIノールA、ジブチル錫マレート等の熱安定剤、
アルキルエーテル1iXBI!エステルナトリウム、ア
ルファオレフィンスルホン酸ナトリウム等のアニオン界
面活性剤なども加えることができる。The composition of the present invention includes MS resin, MBS resin, ABSs
It can contain soubrene-based copolymers such as L resin, As resin, and BS resin. Also calcium carbonate, talc,
Inorganic fillers such as silica, alumina, glass fiber, etc. can be added. Furthermore, metal soaps such as magnesium stearate, calcium stearate, and zinc stearate,
Heat stabilizers such as bisphinol A, dibutyltin malate,
Alkyl ether 1iXBI! Anionic surfactants such as sodium ester and sodium alpha olefin sulfonate can also be added.
本発明の組成物の141!は次の方法で行うことができ
る。141 of the composition of the present invention! This can be done in the following way.
予め混合した組成物を押出機のホッパーに充填し、加熱
した押出機より、溶融した組成物を吐出させ、ストラン
ドをカットしてペレット状組成物を得る。A hopper of an extruder is filled with the premixed composition, the molten composition is discharged from the heated extruder, and the strands are cut to obtain a pelletized composition.
混合はヘンシェルタイプの高速ミキサー、リボンブレン
ダー、タンブラ−等の通常の混合機を樹脂の種類や形状
に応じて使用できる。For mixing, a conventional mixer such as a Henschel type high-speed mixer, a ribbon blender, or a tumbler can be used depending on the type and shape of the resin.
使用する樹脂の形状は粉状、ビーズ状、フレーク状、ベ
レット状等を挙げることができる。押出様は単軸スクリ
ュー押出機、二軸スクリュー押出機、コニーダー等を使
用できる。造粒のためのカット方法は、水中カット、霧
中カット、あるいは空中カットのいずれでも良い。The shape of the resin used may be powder, beads, flakes, pellets, etc. For extrusion, a single screw extruder, twin screw extruder, co-kneader, etc. can be used. The cutting method for granulation may be underwater cutting, mist cutting, or aerial cutting.
(実施例)
以下に実施例及び比較例により、本発明を具体的に説明
するが、本発明はこれらに限定されるものではない。実
施例及び比較例において、組成物の洗浄効果はつぎの方
法による洗浄テストにおいて、消費した置換用樹脂の量
、及び、洗浄に要した時間によって評価する。(Example) The present invention will be specifically described below with reference to Examples and Comparative Examples, but the present invention is not limited thereto. In Examples and Comparative Examples, the cleaning effects of the compositions are evaluated by the amount of displacing resin consumed and the time required for cleaning in a cleaning test using the following method.
洗浄テスト
35トン射出成型機を使用してカーボンブラック1重量
%を含有する先行樹脂3009を供給する。次に洗浄用
として組成物100gを供給し、更に置換用樹脂を供給
し射出成型を繰り返し、吐出した樹脂が消色するまで続
ける。消費した置換用樹脂の量、及び、組成物を供給し
tよじめてから消色するまでの時間を計測する。Cleaning Test A 35 ton injection molding machine is used to feed precursor resin 3009 containing 1% by weight carbon black. Next, 100 g of a composition for cleaning is supplied, and a replacement resin is further supplied, and injection molding is repeated until the discharged resin disappears in color. The amount of the replacement resin consumed and the time from supplying the composition until it disappears is measured.
(実施例1)
ポリスチレン(メルトフローインデックス(JISK6
870 : 200℃、5?(fff)1.Of/lo
ginのホモポリ?−)3.90Kg、ドデシルベンゼ
ンスルホン酸ナトリウム0.5ONy、ステアリン酸モ
ノグリセライドのホウ酸エステル0.40Kg、ポリエ
チレンワックス(数平均分子f!11500)0.10
幻、ステアリン酸マグネシウム0.10に5F、を内容
積20jlの高速ミキサーにて回転数50Orpmで3
分間攪拌して混合した。(Example 1) Polystyrene (melt flow index (JISK6
870: 200℃, 5? (fff)1. Of/lo
Is gin homopoly? -) 3.90Kg, sodium dodecylbenzenesulfonate 0.5ONy, boric acid ester of stearic acid monoglyceride 0.40Kg, polyethylene wax (number average molecule f! 11500) 0.10
Phantom, magnesium stearate 0.10 at 5F in a high speed mixer with an internal volume of 20Jl at a rotation speed of 50Orpm.
Mix by stirring for a minute.
この混合物をシリンダーのL/Dが30でシリンダー径
が30mの二輪スクリュー押出機に供給し、シリンダー
温度220℃、ダイス温度230℃の条件でストランド
を押し出し水槽中で冷却し、ペレタイザーでカットして
乳白色で粒状の組成物を得た。この組成物を用いて、カ
ーボンブラック1重階%を含有するポリフェニレンオキ
サイドで汚染させた射出成型機の洗浄テストを行った。This mixture was supplied to a two-wheel screw extruder with a cylinder L/D of 30 and a cylinder diameter of 30 m, and the strands were extruded at a cylinder temperature of 220°C and a die temperature of 230°C, cooled in a water tank, and cut with a pelletizer. A milky white, granular composition was obtained. This composition was used in a cleaning test on an injection molding machine contaminated with polyphenylene oxide containing 1% carbon black.
射出成型機のシリンダー温度280℃で、また置換用樹
脂としてポリエチレンテレフタレートを使用した。ポリ
エチレンテレフタレートの消費量は140g、洗浄に要
した時間は12分であった。The cylinder temperature of the injection molding machine was 280°C, and polyethylene terephthalate was used as the replacement resin. The amount of polyethylene terephthalate consumed was 140 g, and the time required for washing was 12 minutes.
(実施例2)
ポリスチレン〔メルトフローインデックス(J l5K
6870 : 200℃、5Kyf)1.0g/10a
iinのホモポリ’? −)4.55Ny、ドデシルベ
ンゼンスルホン酸マグネシウム0.25Kg、シリコン
オイル(粘度(25℃)500センチストークス>0.
15kg、ドデシルスルホン酸す1−リウム0.05N
y、を実施例1と同様に混合した。(Example 2) Polystyrene [melt flow index (J l5K
6870: 200℃, 5Kyf) 1.0g/10a
iin homopoly'? -) 4.55 Ny, magnesium dodecylbenzenesulfonate 0.25 Kg, silicone oil (viscosity (25°C) 500 centistokes > 0.
15kg, 1-lium dodecylsulfonate 0.05N
y, were mixed in the same manner as in Example 1.
シリンダー温度230℃、ダイス温度240℃以外は実
施例1と同様にして組成物を得た。この組成物を用いて
、カーボンブラック1重量%を含有するポリカーボネー
トで汚染させた射出成型機の洗浄テストを行った。射出
成型機のシリンダー温度260℃で、また置換用樹脂と
してポリスチレンを使用した。ポリスチレンの消費層は
1809、洗浄に要した時間は14分であった。A composition was obtained in the same manner as in Example 1 except that the cylinder temperature was 230°C and the die temperature was 240°C. This composition was used in a cleaning test on an injection molding machine contaminated with polycarbonate containing 1% by weight of carbon black. The cylinder temperature of the injection molding machine was 260° C., and polystyrene was used as the replacement resin. The consumed layer of polystyrene was 1809, and the time required for washing was 14 minutes.
(実施例3)
ポリスチレン(メルトフローインデックス(JISK6
870 : 200℃、5kgf)i、89/10w1
nのホモポリマー)3.1ONp、ドデシルベンビンス
ルホン酸カリウム1.60Kg、ポリエチレンワックス
(数平均分子11500)0.20Kg、ステアリン酸
マグネシウム0.10Kg、を実施例1と同様に混合し
た。シリンダー温度190℃、ダイス温度200℃以外
は実施例1と同様にして組成物を得た。この組成物を用
いて、力−ボ、ンブラック1瓜泄%を含有するポリフェ
ニレンザルファイドで汚染させた射出成型機の洗浄テス
トを行った。射出成型機のシリンダー温度300℃で、
また置換用樹脂としてポリアセタールを使用した。ポリ
アセタールの消費量は260り、洗浄に要した@i!l
は18分であった。(Example 3) Polystyrene (melt flow index (JISK6)
870: 200℃, 5kgf)i, 89/10w1
In the same manner as in Example 1, 3.1 ONp (homopolymer of n), 1.60 Kg of potassium dodecylbenvinsulfonate, 0.20 Kg of polyethylene wax (number average molecule 11,500), and 0.10 Kg of magnesium stearate were mixed. A composition was obtained in the same manner as in Example 1 except that the cylinder temperature was 190°C and the die temperature was 200°C. This composition was used to perform a cleaning test on an injection molding machine contaminated with polyphenylene sulfide containing 1% carbon black. The cylinder temperature of the injection molding machine is 300℃,
In addition, polyacetal was used as the substitution resin. The amount of polyacetal consumed was 260, and the time required for cleaning was @i! l
was 18 minutes.
(実施例4)
ポリスチレン〔メルトフローインデックス(J l5K
6870 : 200℃、5Kyf)5.2SF/10
m1nのホモポリ?−)4.50に!g、ドデシルベン
ゼンスルーボン酸カルシウム0.15Ny、パルミチン
酸モノグリセライドのホウ酸エステルのカルシウムF0
.15Kg、ポリエチレンワックス(数平均分子ff1
l 500) 0.1 ONy、アルミナ(住友化学■
製AL−32)0.1ONg、を実施例1と同様に混合
した。シリンダー温度190℃、ダイス温度200℃以
外は実施例1と同様にして組成物を得た。この組成物を
用いて、カーボンブラック1臣m%を含有するポリフェ
ニレンオキサイドで汚染させた射出成型機の洗浄テスト
を行った。射出成型機のシリンダー温度280℃で、ま
た置換用樹脂としてABS樹脂を使用した。(Example 4) Polystyrene [melt flow index (J l5K
6870: 200℃, 5Kyf) 5.2SF/10
Homopoly of m1n? -) 4.50! g, calcium dodecylbenzenesulfonate 0.15Ny, calcium borate of palmitic acid monoglyceride F0
.. 15Kg, polyethylene wax (number average molecule ff1
l 500) 0.1 ONy, alumina (Sumitomo Chemical ■
AL-32) 0.1 ONg was mixed in the same manner as in Example 1. A composition was obtained in the same manner as in Example 1 except that the cylinder temperature was 190°C and the die temperature was 200°C. Using this composition, a cleaning test was carried out on an injection molding machine contaminated with polyphenylene oxide containing 1 mm% of carbon black. The cylinder temperature of the injection molding machine was 280° C., and ABS resin was used as the replacement resin.
ABS樹脂の消費量は320g、洗浄に要した時間は2
1分であった。The amount of ABS resin consumed was 320g, and the time required for cleaning was 2
It was 1 minute.
(実施例5)
ポリスチレンCメルトフローインデックス(J l5K
6870 : 200℃、5Kgf)5.2g/10m
1nのホモポリ?−)4.10Kg、ドデシルベンげン
スルホン酸ナトリウム0.7589、ペンタエリスリト
ールテトラステアレート0.10Kg、ステアリン酸マ
グネシウム0.05句、を実施例1と同様に混合した。(Example 5) Polystyrene C melt flow index (J l5K
6870: 200℃, 5Kgf) 5.2g/10m
1n homopoly? -) 4.10 kg, sodium dodecylbenzene sulfonate 0.7589, pentaerythritol tetrastearate 0.10 kg, and magnesium stearate 0.05 kg were mixed in the same manner as in Example 1.
シリンダー温度190℃、ダイス温度200℃以外は実
施例1と同様にして組成物を得た。この組成物を用いて
、カーボンブラック1重量%を含有するポリフェニレン
オキサイドで汚染させた射出成型機の洗浄テストを行っ
た。射出成型機のシリンダー温度280℃で、また置換
用@4脂としてポリエチレンテレフタレートを使用した
。ポリエチレンテレフタレー1への消費量は300g、
洗浄に要した部間は20分であった。A composition was obtained in the same manner as in Example 1 except that the cylinder temperature was 190°C and the die temperature was 200°C. This composition was used in a cleaning test on an injection molding machine contaminated with polyphenylene oxide containing 1% by weight of carbon black. The cylinder temperature of the injection molding machine was 280° C., and polyethylene terephthalate was used as the substitute @4 resin. The consumption amount for polyethylene terephthalate 1 is 300g,
The time required for cleaning was 20 minutes.
(比較例1)
ポリスチレン(メルトフローインデックス(J l5K
687(5: 200℃、5/(gf)5.2g/10
m1nのホモポリマー〕4.80Kg、ドデシルベンゼ
ンスルホン酸ナトリウム0.057(9、ペンタエリス
リトールテトラステアレート0.101’i9、ステア
リン酸マグネシウム0.058y、を実施例1と同様に
混合した。シリンダー温1食190℃、ダイス温度20
0℃以外は実施例1と同様にして組成物を得た。この組
成物を用いて、カーボンブラック1f4ff1%を含有
するポリフェニレンオキサイドで汚染させた射出成型機
の洗浄テストを行った。射出成型機のシリンダー温度2
80℃で、また置換用樹脂としてポリエチレンプレフタ
レートを使用した。ポリエチレンテレフタレートの消費
量は1220g、洗浄に要した時間は66分であった。(Comparative Example 1) Polystyrene (melt flow index (J l5K)
687 (5: 200℃, 5/(gf)5.2g/10
m1n homopolymer] 4.80 Kg, sodium dodecylbenzenesulfonate 0.057 (9, pentaerythritol tetrastearate 0.101'i9, magnesium stearate 0.058 y) were mixed in the same manner as in Example 1. Cylinder temperature 1 meal 190℃, dice temperature 20
A composition was obtained in the same manner as in Example 1 except for the temperature of 0°C. Using this composition, a cleaning test was carried out on an injection molding machine contaminated with polyphenylene oxide containing 1% carbon black 1f4ff. Injection molding machine cylinder temperature 2
The temperature was 80° C. and polyethylene prephthalate was used as the replacement resin. The amount of polyethylene terephthalate consumed was 1220 g, and the time required for washing was 66 minutes.
(比較例2)
ポリスチレン〔メルトフローインデックス(J l5K
6870 : 200℃、5/(yf>23.09/1
0+tnのホ[ポリ?−)4.10に9、ドデシルベン
ゼンスルホン酸ナトリウム0.75Kg、ペンタエリス
リトールテトラステアレート0.IC1、ステアリン酸
マグネシウム0.05Kg、を実施例1と同様に混合し
た。シリンダー温度190℃、ダイス温度200℃以外
(ま実施例1と同様にして組成物を得た。この組成物を
用いて、カーボンブラック1重量%を含りするポリフェ
ニレンオキサイドで汚染させた射出成型機の洗浄テスト
を行った。°射出成型機のシリンダー温度280℃で、
また置換用樹脂としてポリ1チレンテレフタレートを使
用した。ポリエチレンテレフタレートの消費のは920
g、洗浄に要した時間は51分であった。(Comparative Example 2) Polystyrene [melt flow index (J l5K
6870: 200℃, 5/(yf>23.09/1
0+tn ho [poly? -) 4.10 to 9, sodium dodecylbenzenesulfonate 0.75Kg, pentaerythritol tetrastearate 0. IC1 and 0.05 kg of magnesium stearate were mixed in the same manner as in Example 1. A composition was obtained in the same manner as in Example 1 except that the cylinder temperature was 190°C and the die temperature was 200°C.This composition was used in an injection molding machine contaminated with polyphenylene oxide containing 1% by weight of carbon black. A cleaning test was conducted at an injection molding machine cylinder temperature of 280°C.
Moreover, poly(1-ethylene terephthalate) was used as a substitute resin. The consumption of polyethylene terephthalate is 920
g. The time required for washing was 51 minutes.
実施例1〜5、比較例1〜2の条件および結果を表1に
まとめた。The conditions and results of Examples 1 to 5 and Comparative Examples 1 to 2 are summarized in Table 1.
本発明の組成物を洗浄用として使用することにより、高
温度で成形するエンジニアリングプラスブックの品種切
り替えにおいて、極めて効果的な方法を実現できた。By using the composition of the present invention for cleaning, it was possible to realize a very effective method for changing types of engineering plus books that are molded at high temperatures.
即ち、本発明の樹脂組成物を少量用いることにより、従
来の洗浄用組成物の使用に比べて、著しく後続の置換用
樹脂の量を減少させ、また洗浄時間を短縮出来た。表1
のポリフェニレンオキサイドからポリエチレンテレフタ
レートへの品種切り替えを例に取ると、置換用樹脂の吊
を1/3以下に減少させ、洗浄時間も215以下に短縮
出来た。That is, by using a small amount of the resin composition of the present invention, the amount of subsequent replacement resin can be significantly reduced and the cleaning time can be shortened, compared to the use of conventional cleaning compositions. Table 1
For example, when switching from polyphenylene oxide to polyethylene terephthalate, the amount of replacement resin used was reduced to less than one-third, and the cleaning time was also shortened to less than 215%.
Claims (1)
及び離型性化合物を配合してなる組成物を含む洗浄用樹
脂組成物。 2、ポリスチレン50〜95重量%に、アルキルベンゼ
ンスルホン酸中性塩2〜40重量%、及び離型性化合物
1.5〜15重量%を配合してなる組成物を含む洗浄用
樹脂組成物。 3、ポリスチレンがメルトフローインデックス(g/1
0分)(JISK6870)7.0以下のものである請
求項1又は2記載の洗浄用樹脂組成物。 4、離型性化合物が、カルボン酸の炭素数が10〜22
のペンタエリスリトールテトラカルボン酸エステル、カ
ルボン酸の炭素数が12〜22のカルボン酸モノグリセ
ライドのホウ酸エステル、カルボン酸の炭素数が12〜
22のカルボン酸モノグリセライドのホウ酸エステルの
カルシウム塩、ポリエチレンワックス、シリコンオイル
からなる群より選んだ1種又は2種以上である請求項1
又は2記載の洗浄用樹脂組成物。[Claims] 1. A cleaning resin composition containing a composition prepared by blending polystyrene with a neutral salt of alkylbenzenesulfonic acid and a mold release compound. 2. A cleaning resin composition comprising 50 to 95% by weight of polystyrene, 2 to 40% by weight of a neutral salt of alkylbenzenesulfonic acid, and 1.5 to 15% by weight of a releasing compound. 3. Polystyrene has a melt flow index (g/1
3. The cleaning resin composition according to claim 1 or 2, wherein the cleaning resin composition has a water resistance of 7.0 (JIS K6870) or less. 4. The mold release compound has a carboxylic acid having 10 to 22 carbon atoms.
Pentaerythritol tetracarboxylic acid ester, boric acid ester of carboxylic acid monoglyceride with carboxylic acid having 12 to 22 carbon atoms, carboxylic acid having 12 to 22 carbon atoms
Claim 1: One or more selected from the group consisting of calcium salt of boric acid ester of carboxylic acid monoglyceride No. 22, polyethylene wax, and silicone oil.
Or the cleaning resin composition according to 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1024061A JPH0741658B2 (en) | 1989-02-03 | 1989-02-03 | Cleaning resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1024061A JPH0741658B2 (en) | 1989-02-03 | 1989-02-03 | Cleaning resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02206636A true JPH02206636A (en) | 1990-08-16 |
JPH0741658B2 JPH0741658B2 (en) | 1995-05-10 |
Family
ID=12127932
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1024061A Expired - Lifetime JPH0741658B2 (en) | 1989-02-03 | 1989-02-03 | Cleaning resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0741658B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006182887A (en) * | 2004-12-27 | 2006-07-13 | Toho Chem Ind Co Ltd | Polylactic acid based biaxially oriented film excellent in antistatic property |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2820113B1 (en) | 2012-02-28 | 2017-07-12 | SABIC Global Technologies B.V. | Processes and compositions for cleaning mixing devices to improve polycarbonate production |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62195045A (en) * | 1986-02-20 | 1987-08-27 | Chisso Corp | Thermoplastic resin composition |
-
1989
- 1989-02-03 JP JP1024061A patent/JPH0741658B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62195045A (en) * | 1986-02-20 | 1987-08-27 | Chisso Corp | Thermoplastic resin composition |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006182887A (en) * | 2004-12-27 | 2006-07-13 | Toho Chem Ind Co Ltd | Polylactic acid based biaxially oriented film excellent in antistatic property |
JP4652803B2 (en) * | 2004-12-27 | 2011-03-16 | 東邦化学工業株式会社 | Polylactic acid biaxially stretched film with excellent antistatic properties |
Also Published As
Publication number | Publication date |
---|---|
JPH0741658B2 (en) | 1995-05-10 |
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