JP3119678B2 - Composition for open-cell propylene resin foam - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a composition for an open-cell propylene resin foam. More specifically, the present invention relates to a resin composition from which an open-cell propylene-based resin foam having excellent heat resistance, mechanical properties, chemical resistance, and the like can be produced. It is used as a heat insulating material, automotive interior material, various mat materials, etc., and is particularly suitable as various filter materials.

[0002]

2. Description of the Related Art A propylene-based resin is a highly crystalline resin coordinated in a stereoregular manner, and therefore has a melting point of about 30 to 50 ° C. higher than that of an ethylene-based resin and has excellent heat resistance and mechanical strength. Therefore, foams using this as a material have been conventionally proposed. The propylene-based resin has a higher melting point and a lower melt viscosity than the ethylene-based resin, and causes a sharp change in viscosity near the melting point, so that the temperature range suitable for extrusion foaming is extremely narrow. Therefore, it is difficult to uniformly knead the blowing agent with the propylene-based resin, and even if kneading is possible, only a blowing agent having a high decomposition temperature can be used, and the range of choice of the blowing agent is narrow. Crosslinking with an organic peroxide to obtain an appropriate melt viscosity for foaming is also conceivable as a diversion of polyethylene foaming technology. However, since polypropylene contains tertiary carbon due to its molecular structure, the crosslinking reaction is difficult. The decomposition reaction takes precedence, and an effective effect cannot be obtained unless a crosslinking aid is used.

To solve these problems, propylene and other monomers are copolymerized to lower the melting point of the polymer so that the melt viscosity is relatively high and the change in the melt viscosity is small over a wide temperature range. (Japanese Patent Publication Nos. 60-26418, 61-61)
1460). There is also a proposal in which a styrene-isoprene block copolymer is blended in order not to lower the melt viscosity (Japanese Patent Publication No. 60-39697). Furthermore, a method has been proposed in which a propylene-based resin is denatured with an alkoxy group-containing vinyl silane and crosslinked with water to increase the melt viscosity relatively (JP-B-61-18933). By these methods, foams made from propylene-based resin have been industrially manufactured, but all of the cell structures are closed cells, and open-cell ones have never been proposed.

[0004]

According to the present invention, the conventional propylene-based resin foam has a closed cell structure and is inferior in air permeability, flexibility, flexibility and the like, and in particular, has no air permeability. An object of the present invention is to propose an open-cell propylene-based resin foam in order to solve these problems, since it is not used for a filter material.

[0005]

As described above, the propylene resin has a high melting point and sharply decreases in viscosity above the melting temperature of the crystal. The application of an appropriate melt viscosity to give a foam is an important technical point in producing a foam, and the formation of an open-cell foam requires special means.

The present inventors have filed a number of patents on techniques for obtaining an open-cell foam using an ethylene resin as a material (Japanese Patent Publication No. 60-49657 and Japanese Patent Application Laid-Open No. 60-124632). No. 62-89738, No. 62
Nos. -89739, 62-89741, 62-89
No. 742, No. 63-113034, No. 63-1130
No. 35, No. 63-126733, Japanese Patent Application No. 63-260
No. 620, No. 63-260621, and Japanese Patent Application No. 1-154.
No. 636, No. 1-154637, No. 1-264419
No. 1-276149). The present invention has been developed by applying these techniques to propylene-based resins.

That is, the present invention relates to (1) a) 100 parts by weight of a propylene-based resin, and b) 0.01 to 10 parts of a polypropylene-modified polysiloxane.
Parts by weight, c) 1 to 30 parts by weight of a foaming agent having a foaming temperature (Tf) in the range of 100 to 200 ° C, and d) an organic peroxide having a 10 minute half-life temperature (Tp) of 110 to 220 ° C. 2 to 10 parts by weight (-10 ° C ≦ T
(p-Tf ≦ 50 ° C.); a composition for an open-cell propylene-based resin foam comprising the following: And processed into a predetermined shape at a temperature not higher than the decomposition temperature of the organic peroxide,
(3) A method for producing an open-cell propylene-based resin foam characterized by heating to 300 ° C .; (3) An open-cell propylene-based resin foam produced by the method (2).

In the present invention, the propylene-based resin is a polymer containing propylene as a main component, propylene homopolymer, propylene and another α-olefin (ethylene,
Butene-1,4-methyl-pentene-1, hexene-
1, octene-1 etc.) or a random copolymer having an MFR (meter flow rate) of 0.1 to
It is preferably 0.2 to 10 at 20 (g / min 230 ° C).
If it is less than 0.1, kneading with a foaming agent is difficult, and extrudability is poor. If it is more than 20, the melt viscosity is reduced and foaming becomes difficult. Specific examples include polypropylene, propylene-ethylene block or random copolymer, propylene-butene-1 block or random copolymer propylene-ethylene-butene-1, random or block copolymer, and the like.

In the present invention, the polypropylene-modified polysiloxane is defined as (A) 100 parts by weight of a propylene-based polymer and (A) the following formula I:

Embedded image (Wherein, R ¹ represents an aliphatic unsaturated group, R ² represents an unsubstituted or substituted monovalent hydrocarbon group containing no aliphatic unsaturated group, and a and b represent the following conditions: 0 ≦ a <1, 0.5 <b <3, representing a numerical value satisfying 1 <a + b <3), 1 to 900 parts by weight of an organopolysiloxane, (B) 0.1 to 50 parts by weight of a butadiene rubber, and (C) an organic compound. It is obtained by heating and kneading a composition obtained by adding 0.01 to 10 parts by weight of a peroxide.
No.-171142. In the present invention, the amount of the polypropylene-modified polysiloxane used is
When the amount is 0.01 to 10 parts by weight, and when the amount is 0.01 part by weight or less, the effect of forming a continuous foam does not reach a saturation point even when the amount is 10 parts by weight or more, and the bleeding phenomenon occurs. Is undesirable.

The foaming agent used in the present invention has a foaming temperature of 100 ° C. to 220 ° C., preferably has a decomposition temperature equal to or higher than the crystal melting point of the propylene resin used. This also includes the case where the decomposition temperature is adjusted to this range. As an example,
These include: Azobisisobutyronitrile,
Diazocarbonamide, p-toluenesulfonylhydrazide, 4,4′-oxybis (benzenesulfonylhydrazide), n-heptane, n-octane, n-nonane,
n-decane. The amount of the foaming agent needs to be 1 to 30 parts by weight.
If the amount is less than 1 part by weight, there is almost no foaming effect. If the amount is more than 30 parts by weight, the amount of the decomposed product of the foaming agent that escapes into the air at the time of foaming increases, resulting in poor efficiency.

The organic peroxide used in the present invention preferably has a decomposition temperature of 110 to 220 ° C. with a half-life of 10 minutes, ie, a half-life of 110 to 220 ° C. for 10 minutes. For example, the following can be mentioned. However, the value in parentheses is the decomposition temperature (° C.). Succinic peroxide (110), benzoyl peroxide (110), t-butylperoxy-2-ethylhexanoate (113), p-chlorobenzoyl peroxide (115), t-butylperoxyisobutyrate (115), t- Butylperoxyisopropyl carbonate (135), t-butylperoxylaurate (140), 2,5-dimethyl-2,5-di (benzoylperoxy) hexane (140), t-butylperoxyacetate (140), di-t -Butyldiperoxyphthalate (140), t-butylperoxymaleic acid (140), cyclohexanone peroxide (145), t-butylperoxybenzoate (14)
5), dicumyl peroxide (150), 2,5-dimethyl-2,5-di (t-butylperoxy) hexane (155), t-butylcumyl peroxide (15)
5), t-butyl hydroperoxide (158), di-
t-butyl peroxide (160), 2,5-dimethyl-2,5-di (t-butylperoxy) hexyne-3
(170), di-isopropylbenzene hydroperoxide (170), p-menthane hydroperoxide (1
80), 2,5-dimethylhexane-2,5-dihydroperoxide (213).

In the present invention, the amount of the organic peroxide is 0.2
-10 parts by weight are required. If the amount is less than 0.2 parts by weight, the viscosity of the resin hardly increases when the composition is heated, and the resin layer becomes loose. If the amount is more than 10 parts by weight, the increase in the crosslinking efficiency is small. Next, in the present invention, one of the organic peroxides is used.
Assuming that the 0 minute half-life temperature is Tp and the foaming temperature of the foaming agent is Tf, selecting and combining an organic peroxide and a foaming agent so as to satisfy the following equation: −10 ° C. ≦ Tp−Tf ≦ 50 ° C. is necessary. That is, by using such a combination, if the composition is heated and then cooled, an open-cell foam having open cells or partially closed cells can be obtained.

In the present invention, an ethylene resin such as polyethylene, an oxidation stabilizer, an ultraviolet stabilizer, an inorganic filler, a pigment, a flame retardant, a rubber, and the like can be added to the composition, if necessary. The temperature at the time of heating the composition of the present invention,
It is above the temperature required for foaming and crosslinking to take place, specifically between 130 and 300 ° C. In the present invention, the decomposition temperature of the organic peroxide is determined by the half-life 1 of the pure product.
Since the temperature is shown at 0 minute, crosslinking proceeds even below this temperature. Depending on the purpose, the heating can be performed under normal pressure or under pressure.

In order to produce the open-cell propylene resin foam of the present invention, the respective components are mixed and kneaded at a temperature not higher than the decomposition temperature of the blowing agent or the chemical blowing agent. , Sheets, rods, spheres, etc., with or without a mold, at or above the decomposition temperature of the blowing agent or chemical blowing agent and -10 ° C ≦ Tp-Tf ≦ 50 ° C
(May be pressurized). Hereinafter, examples of the present invention will be described.

[0015]

EXAMPLE 1 Impact-resistant polypropylene J-409 (manufactured by Tonen Chemical) 20
kg, azodicarbonamide-based blowing agent "Celmic C-
2 "(foaming temperature 204 ° C: Sankyo Kasei) 2 kg, 40 g of organic peroxide" Parcadox 14 "(decomposition temperature 158 ° C: Kayaku Nouri), antioxidant" Irganox 1 "
010 "(manufactured by Ciba-Geigy) and 1 kg of polypropylene-modified polysiloxane" Silgraft 610 "(polypropylene content: 50%: manufactured by Nippon Unicar) at 160 DEG C. with a DS20-40 MWA-H type kneader manufactured by Moriyama Seisakusho at 160.degree.
Kneaded for 0 minutes. The number of revolutions of the blade was 45 rpm. This kneaded material was pelletized. 15 pellets
A sheet having a thickness of 1 mm was formed at 0 ° C. by a compression molding method. The pressure and time were 100 kg / cm ² and 5 minutes, respectively. Place this sheet on a polyester sheet and
When placed in an oven at 0 ° C., it foamed uniformly in 9 minutes. When this foam was taken out and allowed to cool to room temperature, a foam having a thickness of 10 mm and an average cell diameter of 0.4 mm was obtained. The density of the foam was 0.07 g / cm ³ .
After immersing the foam in warm water of 90 ° C. for 10 minutes, the thickness was measured to be 10 mm. In addition, foam
When compression and relaxation were repeated in water at 3 ° C. and water was forcibly absorbed, 8.6 g of water was absorbed per 1 cm ³ .

Comparative Example 1 In the same manner as in Example 1, a sheet was obtained using dityl polysiloxane (manufactured by Nippon Unicar) having a viscosity of 300,000 CP at 23 ° C. instead of “Silgraft 610”. Place this sheet on a polyester sheet and
When placed in an oven at 0 ° C., foaming took place in 9 minutes. When this foam was taken out and allowed to cool to room temperature, a foam having a thickness of 10 mm was obtained. However, the foam was a foam having an average long diameter of 5 mm and an average short diameter of 1 mm and having a coarse cell diameter.

Comparative Example 2 In the same manner as in Example 1, a sheet was obtained without using a crosslinking agent. Place this sheet on a polyester sheet and
When placed in an oven at 0 ° C., foaming took place in 9 minutes. When this foam was taken out and allowed to cool to room temperature, a foam having a thickness of 10 mm was obtained. However, the foam was a foam having an average long diameter of 5 mm and an average short diameter of 1 mm and having a coarse cell diameter.

Example 2 Impact-resistant polypropylene J-409 (manufactured by Tonen Chemical) 18
kg, low-density polyethylene NUCG-5381 (manufactured by Nippon Unicar) 700 g, azodicarbonamide-based blowing agent “Celmic C-2” (foaming temperature 204 ° C .: manufactured by Sankyo Chemical) 2 kg, organic peroxide “Parcadox 14” (Decomposition temperature: 158 ° C .: Kayaku Nouri) 40 g, antioxidant “Irganox 1010” (Ciba Geigy) 10
g, 1 kg of polypropylene-modified polysiloxane “Silgraft 610” (polypropylene content: 50%, manufactured by Nippon Unicar) was kneaded at 160 ° C. for 10 minutes using a DS20-40 MWA-H type kneader manufactured by Moriyama Seisakusho. The number of revolutions of the blade was 45 rpm. This kneaded material was pelletized. The pellet is compressed at 150 ° C. by 1 mm
The sheet was thick. Pressure and time are 100kg each
/ Cm ² for 5 minutes. This sheet was placed on a polyester sheet and placed in a 200 ° C. oven, where it was uniformly foamed in 9 minutes. Take out this foam,
Upon cooling to room temperature, a foam having a thickness of 10 mm and an average cell diameter of 0.38 mm was obtained. 90 ° C
After immersion in warm water for 10 minutes, the thickness was measured.
It was 0 mm. When the foam was repeatedly compressed and relaxed in water at 23 ° C. to forcibly absorb water, 1 cm ³
8.9 g of water was absorbed.

Example 3 18 kg of polypropylene BJ-315 (manufactured by Tonen Chemical),
700 g of low-density polyethylene NUCG-5381 (manufactured by Nippon Unicar), 2 k of an azodicarbonamide-based foaming agent “CellMike C-2” (foaming temperature: 204 ° C .: manufactured by Sankyo Chemical)
g, organic peroxide "Parcadox 14" (decomposition temperature 1
58 ° C .: 40 g of Kayaku Nouri), 10 g of antioxidant “Irganox 1010” (manufactured by Ciba Geigy), polypropylene-modified polysiloxane “Silgraft 610”
(Polypropylene content 50%: manufactured by Nippon Unicar) 1 kg
Was kneaded at 170 ° C. for 10 minutes with a DS20-40 MWA-H type kneader manufactured by Moriyama Seisakusho. This kneaded material was pelletized. The pellets were compressed at 160 ° C for 1m by compression molding.
m-thick sheet. Pressure and time are 100k each
g / cm ² for 5 minutes. This sheet was placed on a polyester sheet and placed in a 200 ° C. oven, where it was uniformly foamed in 9 minutes. Take out this foam,
Upon cooling to room temperature, a foam having a thickness of 10 mm and an average cell diameter of 0.4 mm was obtained. The density of the foam is 0.0
It was 8 g / cm ³ . Put this foam in warm water at 90 ° C for 1
After immersion for 0 minutes, the thickness was measured and found to be 20 mm. Further, foam repeated compression and relaxation in water at 23 ° C., was forced to water, 1 cm ³ per 8.0
g of water absorption.

[0020]

The open-cell foam obtained by the present invention is excellent in heat resistance, mechanical properties, chemical resistance and the like, and has a uniform cell diameter. It can be applied to materials, filters, car interior wall cushions, culture floor materials, etc. Especially since the bubbles are open-celled,
It is suitable for filters.

Continuation of the front page (56) References JP-A-4-342743 (JP, A) JP-A-3-269027 (JP, A) JP-A-3-269026 (JP, A) JP-A-2-240145 (JP, A) JP-A-4-170442 (JP, A) JP-A-3-139536 (JP, A) JP-A-3-21640 (JP, A) JP-A-4-170443 (JP, A) 3-287636 (JP, A) JP-A-3-287635 (JP, A) (58) Fields investigated (Int. Cl. ⁷ , DB name) C08J 9/00-9/42 C08L 23/00-23 / 36

Claims (3)

(57) [Claims] 1. A) 100 parts by weight of a propylene-based resin, b) 0.01 to 10 parts of a polypropylene-modified polysiloxane.
Parts by weight, c) 1 to 30 parts by weight of a foaming agent having a foaming temperature (Tf) in the range of 100 to 200 ° C, and d) an organic peroxide having a 10 minute half-life temperature (Tp) of 110 to 220 ° C. 2 to 10 parts by weight (-10 ° C ≦ T
(p-Tf ≦ 50 ° C.). 2. The composition for an open-cell propylene-based resin foam according to claim 1 is processed into a predetermined shape at a decomposition temperature of a foaming agent or lower and at a decomposition temperature of an organic peroxide or lower. A method for producing an open-cell propylene-based resin foam, characterized by heating to 130 to 300 ° C. 3. An open-cell propylene-based resin foam produced by the method according to claim 2.