JPH01282234A - Powdery polyolefin composition - Google Patents
Powdery polyolefin compositionInfo
- Publication number
- JPH01282234A JPH01282234A JP11152788A JP11152788A JPH01282234A JP H01282234 A JPH01282234 A JP H01282234A JP 11152788 A JP11152788 A JP 11152788A JP 11152788 A JP11152788 A JP 11152788A JP H01282234 A JPH01282234 A JP H01282234A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- polyethylene
- fluidity
- coating
- fatty acid
- 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.)
- Pending
Links
- 239000000203 mixture Substances 0.000 title claims abstract description 12
- 229920000098 polyolefin Polymers 0.000 title 1
- 239000000843 powder Substances 0.000 claims abstract description 40
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 20
- 239000000194 fatty acid Substances 0.000 claims abstract description 20
- 229930195729 fatty acid Natural products 0.000 claims abstract description 20
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 20
- 150000003839 salts Chemical class 0.000 claims abstract description 14
- 239000004698 Polyethylene Substances 0.000 claims description 37
- -1 polyethylene Polymers 0.000 claims description 37
- 229920000573 polyethylene Polymers 0.000 claims description 37
- 229910052751 metal Inorganic materials 0.000 claims description 15
- 239000002184 metal Substances 0.000 claims description 15
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- 238000000576 coating method Methods 0.000 abstract description 16
- 239000011248 coating agent Substances 0.000 abstract description 14
- 239000000049 pigment Substances 0.000 abstract description 7
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 abstract description 4
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 abstract description 4
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 abstract description 3
- 239000008116 calcium stearate Substances 0.000 abstract description 3
- 235000013539 calcium stearate Nutrition 0.000 abstract description 3
- 238000007610 electrostatic coating method Methods 0.000 abstract description 3
- 235000019359 magnesium stearate Nutrition 0.000 abstract description 2
- 150000001875 compounds Chemical class 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000010298 pulverizing process Methods 0.000 description 15
- 238000000034 method Methods 0.000 description 12
- 239000002904 solvent Substances 0.000 description 5
- 238000007598 dipping method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 229920001684 low density polyethylene Polymers 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- GHVNFZFCNZKVNT-UHFFFAOYSA-N decanoic acid Chemical compound CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 2
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 description 2
- ZQPPMHVWECSIRJ-MDZDMXLPSA-N elaidic acid Chemical compound CCCCCCCC\C=C\CCCCCCCC(O)=O ZQPPMHVWECSIRJ-MDZDMXLPSA-N 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- SECPZKHBENQXJG-FPLPWBNLSA-N palmitoleic acid Chemical compound CCCCCC\C=C/CCCCCCCC(O)=O SECPZKHBENQXJG-FPLPWBNLSA-N 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- BITHHVVYSMSWAG-KTKRTIGZSA-N (11Z)-icos-11-enoic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCC(O)=O BITHHVVYSMSWAG-KTKRTIGZSA-N 0.000 description 1
- OYHQOLUKZRVURQ-NTGFUMLPSA-N (9Z,12Z)-9,10,12,13-tetratritiooctadeca-9,12-dienoic acid Chemical compound C(CCCCCCC\C(=C(/C\C(=C(/CCCCC)\[3H])\[3H])\[3H])\[3H])(=O)O OYHQOLUKZRVURQ-NTGFUMLPSA-N 0.000 description 1
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 235000021357 Behenic acid Nutrition 0.000 description 1
- DPUOLQHDNGRHBS-UHFFFAOYSA-N Brassidinsaeure Natural products CCCCCCCCC=CCCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000005632 Capric acid (CAS 334-48-5) Substances 0.000 description 1
- URXZXNYJPAJJOQ-UHFFFAOYSA-N Erucic acid Natural products CCCCCCC=CCCCCCCCCCCCC(O)=O URXZXNYJPAJJOQ-UHFFFAOYSA-N 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
- 239000005639 Lauric acid Substances 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- 235000021319 Palmitoleic acid Nutrition 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 229940116226 behenic acid Drugs 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- SECPZKHBENQXJG-UHFFFAOYSA-N cis-palmitoleic acid Natural products CCCCCCC=CCCCCCCCC(O)=O SECPZKHBENQXJG-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 229940108623 eicosenoic acid Drugs 0.000 description 1
- BITHHVVYSMSWAG-UHFFFAOYSA-N eicosenoic acid Natural products CCCCCCCCC=CCCCCCCCCCC(O)=O BITHHVVYSMSWAG-UHFFFAOYSA-N 0.000 description 1
- 238000009503 electrostatic coating Methods 0.000 description 1
- 238000007590 electrostatic spraying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006353 environmental stress Effects 0.000 description 1
- DPUOLQHDNGRHBS-KTKRTIGZSA-N erucic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-KTKRTIGZSA-N 0.000 description 1
- 229920006226 ethylene-acrylic acid Polymers 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000005339 levitation Methods 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- WBHHMMIMDMUBKC-XLNAKTSKSA-N ricinelaidic acid Chemical compound CCCCCC[C@@H](O)C\C=C\CCCCCCCC(O)=O WBHHMMIMDMUBKC-XLNAKTSKSA-N 0.000 description 1
- 229960003656 ricinoleic acid Drugs 0.000 description 1
- FEUQNCSVHBHROZ-UHFFFAOYSA-N ricinoleic acid Natural products CCCCCCC(O[Si](C)(C)C)CC=CCCCCCCCC(=O)OC FEUQNCSVHBHROZ-UHFFFAOYSA-N 0.000 description 1
- 235000003441 saturated fatty acids Nutrition 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 238000000790 scattering method Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- TUNFSRHWOTWDNC-HKGQFRNVSA-N tetradecanoic acid Chemical compound CCCCCCCCCCCCC[14C](O)=O TUNFSRHWOTWDNC-HKGQFRNVSA-N 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Paints Or Removers (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、流動浸漬法、静電塗装法、散布法などの粉体
塗装用として、特に、優れた流動性及び顔料の分散性を
有する粉末ポリエチレン組成物に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention has particularly excellent fluidity and pigment dispersibility, and is suitable for powder coating such as fluidized dipping, electrostatic coating, and spraying. The present invention relates to powdered polyethylene compositions.
粉末ポリエチレンは、流動浸漬法、静電塗装法、散布法
などの粉体塗装用材料として広く用いられている。上記
した各種の粉体塗装法は、危険な溶剤を使用しないこと
、塗装効率が裔いこと、−度の塗装で厚膜の塗装が可能
であることなど数々の利点を有している。又、種々の粉
末樹脂の中でも、粉末ポリエチレンは、特に、耐熱性、
耐候性、耐薬品性、耐環境応力亀裂性などの優れた特性
を有し、粉体塗装用材料として好適である。Powdered polyethylene is widely used as a material for powder coating methods such as fluidized dipping, electrostatic coating, and scattering methods. The various powder coating methods described above have a number of advantages, such as not using dangerous solvents, high coating efficiency, and the ability to coat a thick film with just a few coats. Also, among various powder resins, powder polyethylene has particularly good heat resistance,
It has excellent properties such as weather resistance, chemical resistance, and resistance to environmental stress cracking, making it suitable as a powder coating material.
粉体塗装用材料にとって、優れた流動性は必須である。Excellent fluidity is essential for powder coating materials.
流動性が劣る粉体では、例えば、流動浸漬法で、粉体を
多孔質シートを底部に備えた流動槽に入れ、多孔質シー
トの下部から送られてくる空気によって流動層を形成さ
せようとしても良好な流動層が形成されず、得られる塗
膜の膜厚が不均一になったり、塗膜にピンホールが発生
したりする。又、静電塗装法に於いても、粉体の流動性
が劣ると、粉体貯槽より塗装用ガン迄空気により粉体を
移送することが困難となるばかりでなく、帯電した粉末
粒子が均一に被塗物に付着せず、優れた塗膜を得ること
ができない。For powders with poor fluidity, for example, the fluidized dipping method is used to place the powder in a fluidized tank with a porous sheet at the bottom and try to form a fluidized bed using air sent from the bottom of the porous sheet. However, a good fluidized bed is not formed, and the thickness of the resulting coating film becomes uneven, and pinholes occur in the coating film. Also, in electrostatic coating methods, if the fluidity of the powder is poor, not only will it be difficult to transport the powder from the powder storage tank to the coating gun using air, but the charged powder particles will not be uniform. It does not adhere to the object to be coated, making it impossible to obtain a good coating film.
このため従来より粉末ポリエチレンの流動性向上のため
、粉砕方法の改良及び添加剤の配合の二面から研究が進
められてきた。Therefore, in order to improve the fluidity of powdered polyethylene, research has been carried out from two aspects: improvement of the pulverization method and addition of additives.
ポリエチレンは軟化温度が比較的低く、容易に塑性変形
するため、常温付近での粉砕によって効率良く均一な形
状及び粒径の粉末を製造することは極めて困難である。Since polyethylene has a relatively low softening temperature and is easily plastically deformed, it is extremely difficult to efficiently produce powder with a uniform shape and particle size by pulverization at around room temperature.
又、得られる粉末ポリエチレンには、繊維状の技(所謂
ヒゲと称されているもの)が多くみられ、このヒゲが流
動性を低下させる要因となっている。In addition, the obtained powder polyethylene has many fibrous grains (so-called whiskers), and these whiskers are a factor in reducing fluidity.
このため、従来より、溶剤に溶解後処理する方法或いは
液体窒素などで冷却しながら粉砕する所謂冷凍粉砕など
の方法によって、流動性の良好な粉末ポリエチレンの製
造が試みられ、実際に実施もされている。For this reason, production of polyethylene powder with good fluidity has been attempted and actually carried out by methods such as dissolving it in a solvent and then treating it, or using methods such as so-called cryo-pulverization, in which the polyethylene is crushed while cooling with liquid nitrogen. There is.
又、粉末ポリエチレン組成物の組成によって流動性を改
良する方法として、従来より樹脂の滑剤として広く使用
されている脂肪酸アミドを添加する方法が、例えば、特
開昭49−92171号公報及び特開昭58−1762
51号公報などに提案され実施されている。Furthermore, as a method for improving fluidity by changing the composition of a powder polyethylene composition, a method of adding a fatty acid amide, which has conventionally been widely used as a lubricant for resins, is disclosed, for example, in JP-A-49-92171 and JP-A-Sho. 58-1762
It has been proposed and implemented in Publication No. 51, etc.
〔解決されるべき課題]
しかしながら、溶剤に溶解後処理する方法によって得ら
れる粉末ポリエチレンは、比較的丸味を帯びた形状であ
って、流動性が良好ではあるものの、歿存溶剤による生
成粉末ポリエチレンの物性の低下、顔料の変色或いはキ
シレンなどの危険な溶剤を使用することに伴う作業環境
の悪化及びコストアップなど種々の問題点を有している
。又、冷凍粉砕方法は機械粉砕でありながら、良好な流
動性を有する粉末ポリエチレンが得られるが、コストが
非常に高く、現在では一般的に採用されていない。[Problems to be Solved] However, although the polyethylene powder obtained by dissolving it in a solvent and then treating it has a relatively rounded shape and good fluidity, It has various problems such as deterioration of physical properties, discoloration of pigments, deterioration of the working environment due to the use of dangerous solvents such as xylene, and increase in costs. Further, although the cryo-pulverization method is mechanical pulverization, it is possible to obtain powdered polyethylene having good fluidity, but the cost is extremely high and it is not generally employed at present.
一方、脂肪酸アミドを含有する粉末ポリエチレンは、常
温付近に於いて粉砕した粉末であっても、確かに流動性
は比較的良好である。しかし、特に、流動浸漬法では、
裔温に加熱された被塗物が次々と流動槽の中に入れられ
るため、槽内雰囲気温度が35〜55°Cと問くなり、
この様な高雰囲気温度では流動性改良の効果が大幅に低
下してしまうという欠点を有している。On the other hand, powdered polyethylene containing fatty acid amide certainly has relatively good fluidity even if it is a powder that is ground at around room temperature. However, especially in the fluidized immersion method,
Since the objects to be coated heated to a temperature of 100°C are placed one after another into the fluidized tank, the atmospheric temperature inside the tank ranges from 35 to 55°C.
Such a high ambient temperature has the disadvantage that the effect of improving fluidity is significantly reduced.
又、脂肪酸アミドは、顔料の分散については全く効果を
をさず、被塗物に色むらを生ずる。Furthermore, fatty acid amide has no effect on pigment dispersion and causes color unevenness on the coated object.
本発明は、上記した従来の粉末ポリエチレンが有してい
た欠点を排除した粉末ポリエチレン組成物を提供するも
のである。The present invention provides a powder polyethylene composition that eliminates the drawbacks of the conventional powder polyethylene described above.
即ち、本発明は、粉末ポリエチレン100重量部及び炭
素数10〜22の脂肪酸金属塩0.0 O5〜2重量部
からなる粉末ポリエチレン組成物に関する。That is, the present invention relates to a powder polyethylene composition comprising 100 parts by weight of powder polyethylene and 0.05 to 2 parts by weight of a fatty acid metal salt having 10 to 22 carbon atoms.
本発明の粉末ポリエチレン組成物は、流動性が極めて良
好であって、顔料の分散も良好である。The powder polyethylene composition of the present invention has extremely good fluidity and also has good pigment dispersion.
ポリエチレンとしては、低密度ポリエチレン、裔密度ポ
リエチレンなどのエチレンホモポリマーの池、エチレン
−プロピレン共重合体、エチレン−酢酸ビニル共重合体
、エチレン−アクリル酸エステル共重合体、線状低密度
ポリエチレンなどの共重合体を使用できる。又、脂肪酸
或いはそれらの無水物で変成したポリエチレンも使用す
ることができる。Examples of polyethylene include ethylene homopolymers such as low-density polyethylene and low-density polyethylene, ethylene-propylene copolymers, ethylene-vinyl acetate copolymers, ethylene-acrylic acid ester copolymers, and linear low-density polyethylene. Copolymers can be used. Furthermore, polyethylene modified with fatty acids or their anhydrides can also be used.
脂肪酸金属塩を形成する脂肪酸としては、パルミトレイ
ン酸、オレイン酸、エイコセン酸、エルシン酸、エライ
ジン酸、リノール酸、リルン酸、リシノール酸などの不
飽和脂肪酸及びカプリン酸、ラウリン酸、ミリスチン酸
、パルミチン酸、ステアリン酸、アラキシン酸、ベヘン
酸などの飽和脂肪酸が挙げられる。Fatty acids that form fatty acid metal salts include unsaturated fatty acids such as palmitoleic acid, oleic acid, eicosenoic acid, erucic acid, elaidic acid, linoleic acid, lylinic acid, and ricinoleic acid, and capric acid, lauric acid, myristic acid, and palmitic acid. , stearic acid, alaxic acid, behenic acid, and other saturated fatty acids.
金属としては、亜鉛、カルシウム、マグネシウムなどが
挙げられる。Examples of metals include zinc, calcium, and magnesium.
脂肪酸金属塩としては、上記の脂肪酸と金属とが組み合
わされた種々のものが挙げられる。特に、ステアリン酸
亜鉛、ステアリン酸カルシウム、ステアリン酸マグネシ
ウムなどのステアリン酸金属塩が好適である。Examples of fatty acid metal salts include various combinations of the above fatty acids and metals. Particularly suitable are metal stearates such as zinc stearate, calcium stearate, and magnesium stearate.
脂肪酸金属塩の添加量は、粉末ポリエチレン100重量
部に対して0.01〜2重量部、特に、0゜05〜1.
5重量部であることが好ましい。The amount of fatty acid metal salt added is 0.01 to 2 parts by weight, particularly 0.05 to 1.0 parts by weight, per 100 parts by weight of powdered polyethylene.
Preferably it is 5 parts by weight.
脂肪酸金属塩の添加量が0.01重量部未満では、得ら
れる粉末ポリエチレンの流動性は殆ど改良されないばか
りではなく、被膜に色むらが発生する。If the amount of the fatty acid metal salt added is less than 0.01 part by weight, not only will the fluidity of the obtained powder polyethylene be hardly improved, but also color unevenness will occur in the coating.
脂肪酸金属塩の添加量が2重量部を越える場合は、流動
性の改良は認められるものの、被塗物への接着強度が低
下するため好ましくない。If the amount of the fatty acid metal salt added exceeds 2 parts by weight, although an improvement in fluidity is observed, it is not preferable because the adhesive strength to the coated object decreases.
粉砕は公知の粉砕機を用いて、常温で行われる。The pulverization is performed at room temperature using a known pulverizer.
特定のメツシュの篩を使用し、篩上の大った粒径の大き
いものは、再度粉砕機に供給される。A specific mesh sieve is used, and the larger particles on the sieve are fed again to the crusher.
本発明に於いて、これら脂肪酸金属塩は、ポリエチレン
を粉砕する前に、例えば、押出機などで練り込んでおい
てもよく、粉砕時に添加してもよく、又、粉末ポリエチ
レンにミルなどの混合機によって添加してもよい。何れ
の添加方法であっても、無添加に比べて流動性の向上が
認められる。In the present invention, these fatty acid metal salts may be kneaded in, for example, with an extruder before pulverizing polyethylene, or may be added during pulverization, or they may be mixed into powdered polyethylene using a mill or the like. It may be added depending on the machine. Regardless of the method of addition, an improvement in fluidity is observed compared to when no additive is used.
粉砕前或いは粉砕時に脂肪酸金属塩を添加した場合、得
られた粉末ポリエチレンの流動性が改良されるばかりで
はなく、粉砕効率(単位時間当たりの粉末ポリエチレン
の収量)の向上という効果もある。又、何れの粉砕方法
であっても、被塗物は色むらなどの全(ない美しい仕上
がりとなる。When a fatty acid metal salt is added before or during pulverization, not only the fluidity of the obtained powdered polyethylene is improved, but also the pulverization efficiency (yield of powdered polyethylene per unit time) is improved. In addition, no matter which grinding method is used, the coated object will have a beautiful finish with no color unevenness.
以下に、実施例によって本発明の詳細な説明する。Hereinafter, the present invention will be explained in detail by way of examples.
尚、実施例に於いる粉末ポリエチレンの流動性は下記の
方法により評価したものである。In addition, the fluidity of the powdered polyethylene in the examples was evaluated by the following method.
直径80mn+、iさ200IIIalのアクリル樹脂
製の透明な円筒を直立させ、その底部に濾布を敷く。A transparent cylinder made of acrylic resin with a diameter of 80 mm+ and a height of 200 mm is stood upright, and a filter cloth is placed on the bottom of the cylinder.
次いで、円筒内に下から10011IIT+の憂さまで
粉末ポリエチレンを入れ、濾布を通して空気を吹き込む
。この時均−に浮上流動する高さL(単位mm)を測定
し、(L/1σ0)を流動性の尺度とする。Next, powdered polyethylene is placed in the cylinder from the bottom to a depth of 10011IIT+, and air is blown through the filter cloth. The height L (unit: mm) of this time-average floating and flowing is measured, and (L/1σ0) is used as a measure of fluidity.
流動性の良好な粉末ポリエチレンでは、少ない空気量で
バブリング或いはチャネリングを生ずることなく、粉末
全体が均一に浮上し流動する。この場合、供給される空
気量は少量であるため、浮上する高さは小さいものの、
流動層の粉末密度は大であって、−度の浸漬で厚膜の塗
膜が得られ、しかも空気量が少ないため被塗物の温度低
下が小さく、密着性が良好であってピンホールなどを生
ずることもない。流動性の劣る粉末ポリエチレンでは、
大量の空気を供給しなければ、均一な流動を得ることは
できない。このため浮上高さは大となり、流動層の粉末
密度は小となるため、厚膜の塗膜を得るためには、何度
も浸漬を繰り返す必要があり、又、空気量が大であるた
め被塗物の温度低下が大きく、密着不良或いはピンホー
ルなどを生じ易い。上記の如く、本評価法では数値が小
である方が流動性が良好である。又、本評価法では0.
5の数値の差は、実際の粉末ポリエチレンの流動性及び
被塗物の仕上がりのうえで明確な差となって表れる。In powdered polyethylene having good fluidity, the entire powder floats and flows uniformly even with a small amount of air without causing bubbling or channeling. In this case, the amount of air supplied is small, so although the height of levitation is small,
The powder density of the fluidized bed is high, and a thick coating film can be obtained by immersion at -degrees.Furthermore, since the amount of air is small, the temperature drop of the coated object is small, and the adhesion is good, so there are no pinholes. It does not cause Powdered polyethylene has poor fluidity,
Uniform flow cannot be achieved unless a large amount of air is supplied. For this reason, the floating height becomes large and the powder density of the fluidized bed becomes small, so it is necessary to repeat dipping many times in order to obtain a thick coating film, and the amount of air is large. The temperature of the object to be coated decreases significantly, and poor adhesion or pinholes are likely to occur. As mentioned above, in this evaluation method, the smaller the value, the better the fluidity. Also, in this evaluation method, 0.
The difference in the numerical values of 5 appears as a clear difference in the fluidity of the actual powder polyethylene and the finish of the coated object.
実施例
低密度ポリエチレン(Ml:Log/分、密度: 0.
919 g/d、宇部興産■製)をターボミルT−40
0(ターボ興業■製)にて、50メツシユの篩を用いて
、平均粒径80メツシユの粉末とした。次いで、ヘンシ
ェルミキサー(三井三池化工機M製)により上記粉末に
下記の脂肪酸金属塩をそれぞれ500ppm 、 80
0ppm、1200ppm添加した。得られた粉末ポリ
エチレンの流動性を第1表に示す。Example Low density polyethylene (Ml: Log/min, density: 0.
919 g/d, manufactured by Ube Industries) using Turbo Mill T-40
0 (manufactured by Turbo Kogyo ■) using a 50 mesh sieve to obtain a powder with an average particle size of 80 mesh. Next, the following fatty acid metal salts were added to the above powder using a Henschel mixer (manufactured by Mitsui Miike Kakoki M) at 500 ppm and 80 ppm, respectively.
0 ppm and 1200 ppm were added. Table 1 shows the fluidity of the obtained powder polyethylene.
第1表
1j口jユ 坦1 」L
ステアリン酸亜鉛 500 1.35800
1.28
1200 1.22
ステアリン酸カル 500 i、38シウ
ム 800 1.351200
1.32
ステアリン酸マグ 500 1.40ネシウ
ム 800 1.371200
1、.34
無添加 1.47〔発明
の効果〕
本発明の粉末ポリエチレン組成物は、常温に於いて粉砕
する或いは粉砕した粉末ポリエチレンに、脂肪酸金属塩
を少量添加した、極めて低コストで単純な組成でありな
がら、溶剤に溶解後処理する方法或いは冷凍粉砕などの
、特殊な粉砕方法によって得られる粉末ポリエチレンと
同等の優れた流動性を有する。又、粉砕前のポリエチレ
ンに脂肪酸金属塩を添加しておくか或いは粉砕時に添加
しておれば、粉砕効率の向上という効果も得られる。Table 1 1 1 1 1 L Zinc stearate 500 1.35800
1.28 1200 1.22 Calcium stearate 500 i, 38sium 800 1.351200
1.32 Stearic acid mag 500 1.40 Nesium 800 1.371200
1. 34 No additives 1.47 [Effect of the invention] The powder polyethylene composition of the present invention has an extremely low cost and simple composition in which a small amount of fatty acid metal salt is added to powder polyethylene that is ground or ground at room temperature. However, it has excellent fluidity comparable to that of powdered polyethylene obtained by a special pulverization method such as a method of dissolving it in a solvent and then processing it or freezing and pulverization. Furthermore, if a fatty acid metal salt is added to the polyethylene before pulverization or during pulverization, the pulverization efficiency can be improved.
更に、顔料を含有する粉末では、顔料の分散が極めて良
好であって、仕上がりの美しい被塗物が得られるという
効果もある。Furthermore, the pigment-containing powder has the effect that the pigment is dispersed very well, and the object to be coated has a beautiful finish.
Claims (1)
脂肪酸金属塩0.005〜2重量部からなる粉末ポリエ
チレン組成物。A powder polyethylene composition comprising 100 parts by weight of powder polyethylene and 0.005 to 2 parts by weight of a fatty acid metal salt having 10 to 22 carbon atoms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11152788A JPH01282234A (en) | 1988-05-10 | 1988-05-10 | Powdery polyolefin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11152788A JPH01282234A (en) | 1988-05-10 | 1988-05-10 | Powdery polyolefin composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01282234A true JPH01282234A (en) | 1989-11-14 |
Family
ID=14563594
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11152788A Pending JPH01282234A (en) | 1988-05-10 | 1988-05-10 | Powdery polyolefin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01282234A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011219657A (en) * | 2010-04-12 | 2011-11-04 | Mitsui Chemicals Inc | Powder resin composition, polymer alloy using the same, and methods for manufacturing those |
JP2020094153A (en) * | 2018-12-14 | 2020-06-18 | 旭化成株式会社 | Resin composition mainly comprising ethylenic polymer powder, and molded article comprising the same |
-
1988
- 1988-05-10 JP JP11152788A patent/JPH01282234A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011219657A (en) * | 2010-04-12 | 2011-11-04 | Mitsui Chemicals Inc | Powder resin composition, polymer alloy using the same, and methods for manufacturing those |
JP2020094153A (en) * | 2018-12-14 | 2020-06-18 | 旭化成株式会社 | Resin composition mainly comprising ethylenic polymer powder, and molded article comprising the same |
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