JPH0443929B2 - - Google Patents
Info
- Publication number
- JPH0443929B2 JPH0443929B2 JP58143656A JP14365683A JPH0443929B2 JP H0443929 B2 JPH0443929 B2 JP H0443929B2 JP 58143656 A JP58143656 A JP 58143656A JP 14365683 A JP14365683 A JP 14365683A JP H0443929 B2 JPH0443929 B2 JP H0443929B2
- Authority
- JP
- Japan
- Prior art keywords
- fragrance
- powder
- weight
- polyolefin
- parts
- 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 - Lifetime
Links
- 239000000843 powder Substances 0.000 claims description 41
- 239000003205 fragrance Substances 0.000 claims description 39
- 229920000098 polyolefin Polymers 0.000 claims description 28
- 239000004594 Masterbatch (MB) Substances 0.000 claims description 21
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 12
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 12
- 238000003756 stirring Methods 0.000 claims description 4
- 238000004898 kneading Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 description 9
- 239000004743 Polypropylene Substances 0.000 description 8
- -1 polypropylene Polymers 0.000 description 8
- 229920001155 polypropylene Polymers 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 238000001746 injection moulding Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 3
- 238000009775 high-speed stirring Methods 0.000 description 3
- 239000011256 inorganic filler Substances 0.000 description 3
- 229910003475 inorganic filler Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- GRWFGVWFFZKLTI-IUCAKERBSA-N (-)-α-pinene Chemical compound CC1=CC[C@@H]2C(C)(C)[C@H]1C2 GRWFGVWFFZKLTI-IUCAKERBSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- CRPUJAZIXJMDBK-UHFFFAOYSA-N camphene Chemical compound C1CC2C(=C)C(C)(C)C1C2 CRPUJAZIXJMDBK-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000001023 inorganic pigment Substances 0.000 description 2
- XMGQYMWWDOXHJM-UHFFFAOYSA-N limonene Chemical compound CC(=C)C1CCC(C)=CC1 XMGQYMWWDOXHJM-UHFFFAOYSA-N 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- OSWPMRLSEDHDFF-UHFFFAOYSA-N methyl salicylate Chemical compound COC(=O)C1=CC=CC=C1O OSWPMRLSEDHDFF-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 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
- 230000000704 physical effect Effects 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920005653 propylene-ethylene copolymer Polymers 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- NOOLISFMXDJSKH-UTLUCORTSA-N (+)-Neomenthol Chemical compound CC(C)[C@@H]1CC[C@@H](C)C[C@@H]1O NOOLISFMXDJSKH-UTLUCORTSA-N 0.000 description 1
- NOOLISFMXDJSKH-UHFFFAOYSA-N DL-menthol Natural products CC(C)C1CCC(C)CC1O NOOLISFMXDJSKH-UHFFFAOYSA-N 0.000 description 1
- 235000019501 Lemon oil Nutrition 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- PXRCIOIWVGAZEP-UHFFFAOYSA-N Primaeres Camphenhydrat Natural products C1CC2C(O)(C)C(C)(C)C1C2 PXRCIOIWVGAZEP-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- XCPQUQHBVVXMRQ-UHFFFAOYSA-N alpha-Fenchene Natural products C1CC2C(=C)CC1C2(C)C XCPQUQHBVVXMRQ-UHFFFAOYSA-N 0.000 description 1
- MVNCAPSFBDBCGF-UHFFFAOYSA-N alpha-pinene Natural products CC1=CCC23C1CC2C3(C)C MVNCAPSFBDBCGF-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 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
- 229930006739 camphene Natural products 0.000 description 1
- ZYPYEBYNXWUCEA-UHFFFAOYSA-N camphenilone Natural products C1CC2C(=O)C(C)(C)C1C2 ZYPYEBYNXWUCEA-UHFFFAOYSA-N 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000000171 lavandula angustifolia l. flower oil Substances 0.000 description 1
- 239000010501 lemon oil Substances 0.000 description 1
- 229940087305 limonene Drugs 0.000 description 1
- 235000001510 limonene Nutrition 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 229940041616 menthol Drugs 0.000 description 1
- 229960001047 methyl salicylate Drugs 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- GRWFGVWFFZKLTI-UHFFFAOYSA-N rac-alpha-Pinene Natural products CC1=CCC2C(C)(C)C1C2 GRWFGVWFFZKLTI-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003856 thermoforming Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
【発明の詳細な説明】
本発明は、香料を例えば5重量%以上含有した
顆粒状マスターバツチに関する。従来、無機顔料
を高濃度に含有したポリオレフインの着色マスタ
ーバツチの製造は、無機顔料が粉体であることか
らポリオレフインパウダーへの分散が容易で且つ
熱による分解および逸散がなく、従つて押出機等
で比較的容易にペレツト化することができた。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a granular masterbatch containing, for example, 5% by weight or more of a fragrance. Conventionally, colored master batches of polyolefin containing a high concentration of inorganic pigments have been manufactured using extruders, etc. because the inorganic pigments are powders, so they can be easily dispersed into polyolefin powders, and they do not decompose or dissipate due to heat. could be pelletized relatively easily.
しかしながら液状組成物、たとえば香料をポリ
オレフインパウダーに高濃度に含有したペレツト
状マスターバツチを製造する場合は、香料が液状
のためにポリオレフインパウダーへの分散が悪
く、そのうえ押出機等でペレツト化する際には、
香料の有する沸点がポリオレフインの軟化温度よ
りも低く、従つて熱による逸散率が高くこの方法
は採用し得なかつた。 However, when manufacturing a liquid composition, for example, a pellet masterbatch containing a fragrance in polyolefin powder at a high concentration, the fragrance has difficulty dispersing into the polyolefin powder due to its liquid state, and furthermore, when pelletizing with an extruder, etc. ,
This method could not be adopted because the boiling point of the fragrance is lower than the softening temperature of the polyolefin, and therefore the heat dissipation rate is high.
上記の問題を解決する方法として、シリカ微粉
末等の無機フイラーに香料を吸着させた後、ポリ
オレフインパウダーにブレンドし押出機等でペレ
ツト化して目的物質を得る方法が知られている。
しかしながら、シリカ等の無機フイラーは、一般
にポリオレフインに添加した場合は得られる成形
品の透明性、光沢等を低下させ、また無機フイラ
ーはそれ自体水を数%含有しているために押出あ
るいは射出成形時に発泡現象を生じ、満足な成形
品を得られないのが実情であつた。 As a method for solving the above problem, a method is known in which a fragrance is adsorbed onto an inorganic filler such as fine silica powder, blended with polyolefin powder, and pelletized using an extruder or the like to obtain the desired substance.
However, when inorganic fillers such as silica are added to polyolefins, they generally reduce the transparency, gloss, etc. of the molded products obtained, and since inorganic fillers themselves contain several percent water, they cannot be used in extrusion or injection molding. The reality is that foaming sometimes occurs, making it impossible to obtain a satisfactory molded product.
一方、高い空〓率を有する多孔性ポリオレフイ
ンペレツトに香料を多量に含有させる方法があ
る。この方法により得られるマスターバツチはポ
リオレフインペレツトに数%ブレンドし押出ある
いは射出成形することができるが、香料の逸散も
少なく芳香性のあるプラスチツク成形品を得るこ
とができる。 On the other hand, there is a method in which a large amount of fragrance is contained in a porous polyolefin pellet having a high porosity. The masterbatch obtained by this method can be blended in a few percent with polyolefin impellets and then extruded or injection molded, and it is possible to obtain fragrant plastic molded articles with less fragrance loss.
しかしながら、多孔性ポリオレフインの製造工
程および香料を含有させる工程に特殊技術を要す
るためコスト高となることが避けられない。 However, since special techniques are required for the manufacturing process of the porous polyolefin and the process of incorporating the fragrance, high costs are unavoidable.
本発明者らは上記した実情に鑑み香料含有率が
高く且つ成形時に香料の逸散が少なく、安価な顆
粒状マスターバツチの製造について深く検討した
結果、特定のエチレン系共重合体パウダーを使用
することによりこの目的が達成されることを見出
して本発明に到達した。 In view of the above-mentioned circumstances, the inventors of the present invention have deeply studied the production of inexpensive granular masterbatches that have a high fragrance content, less fragrance escape during molding, and have decided to use a specific ethylene copolymer powder. The inventors have discovered that this object can be achieved by the following methods and have arrived at the present invention.
即ち本発明はエチレン−酢酸ビニル共重合体パ
ウダー100重量部に香料を50重量部以上添加し高
速撹拌して混練し、次いでポリオレフインパウダ
ーを添加して高速撹拌して得られる顆粒状香料含
有マスターバツチ、である。 That is, the present invention provides a granular fragrance-containing masterbatch obtained by adding 50 parts by weight or more of a fragrance to 100 parts by weight of ethylene-vinyl acetate copolymer powder, kneading with high speed stirring, and then adding polyolefin powder and stirring at high speed. It is.
本発明によれば高濃度に香料を含有した顆粒状
マスターバツチを低コストで提供することが可能
であり、このマスターバツチは顆粒状を有するこ
とから一般のポリオレフインペレツトと容易にブ
レンドすることができる。 According to the present invention, it is possible to provide a granular masterbatch containing a fragrance at a high concentration at a low cost, and since this masterbatch has a granular shape, it can be easily blended with general polyolefin pellets.
また押出または射出成形等の熱成形時に香料が
逸散することも少なく、外観および物性の低下も
なく芳香性のあるプラスチツク製品を容易に提供
することができる。 Furthermore, fragrance is less likely to escape during thermoforming such as extrusion or injection molding, and fragrant plastic products can be easily provided without deterioration of appearance and physical properties.
本発明に用いられるエチレン−酢酸ビニル共重
合体パウダー(以下EVAパウダーと略す)とは、
通常、酢酸ビニル5〜45重量%を含むものであ
り、またはその変性樹脂もこれに含まれる。 The ethylene-vinyl acetate copolymer powder (hereinafter abbreviated as EVA powder) used in the present invention is:
It usually contains 5 to 45% by weight of vinyl acetate, and also includes modified resins thereof.
また、ポリオレフインパウダーとしてはポリプ
ロピレン、ポリプロピレン−エチレン共重合体、
低密度ポリエチレン、中密度ポリエチレン、高密
度ポリエチレン等、さらに前記ポリオレフインの
多孔質パウダーが挙げられるが、EVAと相溶性
のあるものならばポリオレフインパウダー以外の
ものも利用できる。また香料については、一般に
市販されているものが使用可能であり、特に限定
されるものではない。而して、例えばレモン油、
ラベンダー油、メントール等の天然香料、α−ピ
ネン、カンフエン、リモネン、サリチル酸メチル
等の合成香料、及びこれら香料の調合香料等が利
用できる。 In addition, polyolefin powders include polypropylene, polypropylene-ethylene copolymer,
Examples include porous powders of low density polyethylene, medium density polyethylene, high density polyethylene, and the aforementioned polyolefins, but materials other than polyolefin powders can also be used as long as they are compatible with EVA. Further, as for fragrances, generally commercially available ones can be used, and there are no particular limitations. For example, lemon oil,
Natural fragrances such as lavender oil and menthol, synthetic fragrances such as α-pinene, camphene, limonene, and methyl salicylate, and blended fragrances of these fragrances can be used.
良好な顆粒状マスターバツチの生成条件として
は、EVAパウダーと香料の配合比およびポリオ
レフインパウダーの添加量に左右される。すなわ
ちEVAパウダー100重量部に対して香料を50重量
部以上好ましくは100重量部以上含浸しゲル状に
することが重要である。50重量部未満ではゲル状
とはならず、後にポリオレフインパウダーを添加
しても顆粒状を形成し難い。 Conditions for producing a good granular masterbatch depend on the blending ratio of EVA powder and fragrance and the amount of polyolefin powder added. That is, it is important to impregnate 100 parts by weight of EVA powder with 50 parts by weight or more, preferably 100 parts by weight or more, of fragrance to form a gel. If it is less than 50 parts by weight, it will not become gel-like, and even if polyolefin powder is added later, it will be difficult to form granules.
ポリオレフインパウダーの添加量は、顆粒状と
なる条件下でマスターバツチが高濃度の香料含有
率になるようにできるだけ少量が良い。すなわち
EVAパウダーと香料からなるゲル状組成物100重
量部に対して、通常100重量部以上添加すること
が好ましい。このポリオレフインパウダー添加量
が100重量部未満ではべたつきのある顆粒状マス
ターバツチが生成し好ましくない。この際ステア
リン酸、ステアリン酸カルシウム等の滑剤を少量
加えることにより、この傾向は若干改良される
が、少なくとも100重量部以上好ましくは150重量
部以上の添加が好ましい。しかしながら多孔質ポ
リオレフインパウダーを使用する場合は、一般の
ポリオレフインパウダーに比べてかさ比重が小さ
いので、100重量部未満でもべたつきのない顆粒
状マスターバツチとすることができる。この場合
の多孔質ポリオレフインパウダーとしては、
Armak社製、商品名Accurelパウダー等が挙げら
れる。上記方法で得られる香料入り顆粒状マスタ
ーバツチの香料含率は、通常、一般のポリオレフ
インパウダーの添加では5〜30重量%、多孔質ポ
リオレフインパウダーの場合では5〜60重量%の
範囲である。 The amount of polyolefin powder to be added is preferably as small as possible so that the masterbatch has a high concentration of fragrance content under granular conditions. i.e.
It is usually preferable to add 100 parts by weight or more to 100 parts by weight of a gel composition consisting of EVA powder and fragrance. If the amount of polyolefin powder added is less than 100 parts by weight, a sticky granular masterbatch will be produced, which is not preferable. At this time, this tendency can be slightly improved by adding a small amount of a lubricant such as stearic acid or calcium stearate, but it is preferable to add at least 100 parts by weight or more, preferably 150 parts by weight or more. However, when porous polyolefin powder is used, the bulk specific gravity is smaller than that of general polyolefin powder, so a granular masterbatch without stickiness can be obtained even with less than 100 parts by weight. In this case, the porous polyolefin powder is
Examples include Accurel powder manufactured by Armak. The fragrance content of the fragrance-containing granular masterbatch obtained by the above method is usually in the range of 5 to 30% by weight when a general polyolefin powder is added, and 5 to 60% by weight in the case of a porous polyolefin powder.
ここで定義される香料含率とは香料の重量を香
料とポリオレフインパウダー、EVAパウダーの
総重量和で除した値を100倍したものである。ま
たマスターバツチは、通常、直径1〜5mmの顆粒
を主体としており、一般に樹脂ペレツトと同程度
の大きさである為ブレンドが容易である。 The fragrance content defined here is the weight of the fragrance divided by the total weight of the fragrance, polyolefin powder, and EVA powder, multiplied by 100. Furthermore, masterbatches usually consist mainly of granules with a diameter of 1 to 5 mm, and are generally about the same size as resin pellets, so blending is easy.
本発明に用いられる高速撹拌の条件としては通
常用いられるヘンシエルミキサー等の利用により
容易に得られる程度の高速撹拌能力で充分であ
り、特別な条件を必要とするものでもなく、従つ
てかならずしもヘンシエルミキサーの利用に限定
されるものでもない。 As the conditions for high-speed stirring used in the present invention, a high-speed stirring capacity easily obtained by using a commonly used Henschel mixer is sufficient, and no special conditions are required. Nor is it limited to the use of shell mixers.
本発明により得られる顆粒状香料含有マスター
バツチは、押出成形、射出成形等の方法によつて
成形されるポリオレフイン系成形品に香料を含有
せしめて香料を有する成形品を得る際に有用であ
る。 The granular fragrance-containing masterbatch obtained according to the present invention is useful when a fragrance-containing molded article is obtained by incorporating a fragrance into a polyolefin-based molded article molded by extrusion molding, injection molding, or the like.
以下、実施例により、より詳細に説明する。 Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例 1
10ヘンシエル(三菱電機 スーパーライン
E)にEVAパウダー(東京インキ社製、商品名
サーモタツク8050c)60gを入れ、低速撹拌しな
がらヘンシエル上部の開口部より香料(長谷川香
料社製、商品名Mis−1333)90gを添加し、毎分
1000回転で30秒間撹拌し、ゲル状組成物が得られ
た。さらにポリプロピレンパウダー(三井東圧化
学社製)250gを添加し毎分1000回転で30秒間撹
拌すると顆粒状マスターバツチが得られた。前記
香料含率22%のマスターバツチをプロピレン−エ
チレン共重合体(三井東圧化学社製、商品名 三
井ノーブレンMJS−G)100重量部に対して6重
量部ブレンドし押出機で0.5mm厚シートを製造し
た。Example 1 10 Put 60 g of EVA powder (manufactured by Tokyo Ink Co., Ltd., trade name Thermotatsu 8050c) into Henschel (manufactured by Tokyo Ink Co., Ltd., product name: Thermotatsu 8050c), and add fragrance (manufactured by Hasegawa Fragrance Co., Ltd., product name: Mis −1333) 90g per minute
A gel composition was obtained by stirring at 1000 rpm for 30 seconds. Furthermore, 250 g of polypropylene powder (manufactured by Mitsui Toatsu Chemical Co., Ltd.) was added and stirred at 1000 revolutions per minute for 30 seconds to obtain a granular masterbatch. 6 parts by weight of the masterbatch with a fragrance content of 22% was blended with 100 parts by weight of propylene-ethylene copolymer (manufactured by Mitsui Toatsu Chemical Co., Ltd., trade name: Mitsui Noblen MJS-G), and a 0.5 mm thick sheet was produced using an extruder. Manufactured.
芳香性の持続するシートが得られた。発泡もな
くシートの外観も良好であり透明製の、物性等の
低下もなかつた。 A sheet with a lasting aroma was obtained. There was no foaming, the appearance of the sheet was good, and there was no deterioration in the physical properties of the transparent sheet.
実施例 2
実施例1においてポリオレフインパウダーのか
わりにArmak社製多孔質パウダー(商品名
Accurel、空〓率80%)30gを添加し香料含率50
%の顆粒状マスターバツチを得た。上記マスター
バツチをポリプロピレン(三井東圧化学社製、三
井ノーブレンJH−G)100重量部に2重量部ブレ
ンドし,射出成形機によりペン皿を成形した。こ
の成形物は6ケ月後も殆ど変化が認められない程
度に芳香性が持続された。Example 2 In Example 1, porous powder manufactured by Armak (trade name) was used instead of polyolefin powder.
Add 30g of Accurel (empty rate 80%) and fragrance content 50
% granular masterbatch was obtained. 2 parts by weight of the above masterbatch was blended with 100 parts by weight of polypropylene (Mitsui Noblen JH-G, manufactured by Mitsui Toatsu Chemical Co., Ltd.), and a pen plate was molded using an injection molding machine. This molded product maintained its aromatic properties to the extent that almost no change was observed even after 6 months.
実施例 3
実施例1と同様の操作でEVA(東京インキ社
製、商品名サーモタツクD219)60g、香料(長
谷川香料社製、Perfume ST−613)90gよりな
るゲル状組成物に、ステアリン酸20g、ポリプロ
ピレンパウダー(三井東圧化学社製)150gを添
加し、香料含率28%のマスターバツチを得た。上
記マスターバツチをポリプロピレン(三井東圧化
学社製、三井ノーブレンFL−100)100重量部に
4重量部ブレンドし、厚み30μのインフレーシヨ
ンフイルムを製造した。芳香性のあるフイルムで
外観も良好であつた。Example 3 In the same manner as in Example 1, 20 g of stearic acid, 150 g of polypropylene powder (manufactured by Mitsui Toatsu Chemical Co., Ltd.) was added to obtain a masterbatch with a fragrance content of 28%. 4 parts by weight of the above master batch was blended with 100 parts by weight of polypropylene (manufactured by Mitsui Toatsu Chemical Co., Ltd., Mitsui Noblen FL-100) to produce an inflation film with a thickness of 30 μm. The film was aromatic and had a good appearance.
比較例 1
実施例1においてEVAパウダーを用いずポリ
プロピレンパウダー60gに香料90gを添加したが
ゲル状組成物は得られず懸濁液となり、さらにポ
リプロピレンパウダーを添加しても顆粒状とはな
らなかつた。Comparative Example 1 In Example 1, 90 g of fragrance was added to 60 g of polypropylene powder without using EVA powder, but a gel-like composition was not obtained but a suspension, and even when polypropylene powder was further added, it did not become granular. .
比較例 2
実施例1においてEVAパウダー60g、香料90
g、ポリプロピレンパウダー250gを一度に添加
して毎分1000回転で撹拌したが顆粒状とはならず
パウダー状のマスターバツチが得られた。Comparative Example 2 In Example 1, 60g of EVA powder and 90g of fragrance
250 g of polypropylene powder was added at once and stirred at 1000 revolutions per minute, but the masterbatch did not become granular and a powder-like masterbatch was obtained.
Claims (1)
重量部に香料を50重量部以上添加し高速撹拌して
混練し、次いでポリオレフインパウダーを添加し
て高速撹拌して得られる顆粒状香料含有マスター
バツチ。1 Ethylene-vinyl acetate copolymer powder 100
A granular fragrance-containing masterbatch obtained by adding 50 parts by weight or more of a fragrance to the parts by weight, stirring and kneading at high speed, and then adding polyolefin powder and stirring at high speed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14365683A JPS6035029A (en) | 1983-08-08 | 1983-08-08 | Perfume-containing granular master batch and its production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14365683A JPS6035029A (en) | 1983-08-08 | 1983-08-08 | Perfume-containing granular master batch and its production |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6035029A JPS6035029A (en) | 1985-02-22 |
JPH0443929B2 true JPH0443929B2 (en) | 1992-07-20 |
Family
ID=15343863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14365683A Granted JPS6035029A (en) | 1983-08-08 | 1983-08-08 | Perfume-containing granular master batch and its production |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6035029A (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63139121A (en) * | 1986-12-02 | 1988-06-10 | Kenkoo:Kk | Blending of compound perfume |
US5112919A (en) * | 1989-10-30 | 1992-05-12 | Union Carbide Chemicals & Plastics Technology Corporation | Solid feeding of silane crosslinking agents into extruder |
ITPC970001A1 (en) * | 1997-01-10 | 1998-07-10 | Antonio Campagnoli | NET SPONGE WITH PERFUME RELEASE AND RELATED PRODUCTION METHOD. |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5849151A (en) * | 1981-09-18 | 1983-03-23 | 日東電工株式会社 | Granular aroma release material |
JPS6122585A (en) * | 1984-07-06 | 1986-01-31 | 小島プレス工業株式会社 | Terminal structure and method of producing same |
-
1983
- 1983-08-08 JP JP14365683A patent/JPS6035029A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5849151A (en) * | 1981-09-18 | 1983-03-23 | 日東電工株式会社 | Granular aroma release material |
JPS6122585A (en) * | 1984-07-06 | 1986-01-31 | 小島プレス工業株式会社 | Terminal structure and method of producing same |
Also Published As
Publication number | Publication date |
---|---|
JPS6035029A (en) | 1985-02-22 |
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