JPH11322993A - Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheet - Google Patents
Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheetInfo
- Publication number
- JPH11322993A JPH11322993A JP10153631A JP15363198A JPH11322993A JP H11322993 A JPH11322993 A JP H11322993A JP 10153631 A JP10153631 A JP 10153631A JP 15363198 A JP15363198 A JP 15363198A JP H11322993 A JPH11322993 A JP H11322993A
- Authority
- JP
- Japan
- Prior art keywords
- foamed
- sheet
- foamed sheet
- dyn
- polypropylene resin
- 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
- 229920005989 resin Polymers 0.000 title claims abstract description 62
- 239000011347 resin Substances 0.000 title claims abstract description 62
- -1 Polypropylene Polymers 0.000 title claims abstract description 52
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 47
- 239000004743 Polypropylene Substances 0.000 title claims abstract description 44
- 239000002245 particle Substances 0.000 title claims abstract description 41
- 238000000465 moulding Methods 0.000 title abstract description 34
- 238000004132 cross linking Methods 0.000 title abstract description 18
- 238000002360 preparation method Methods 0.000 title abstract 2
- 238000003860 storage Methods 0.000 claims abstract description 29
- 238000004519 manufacturing process Methods 0.000 claims abstract description 11
- 239000006260 foam Substances 0.000 claims description 42
- 229920005673 polypropylene based resin Polymers 0.000 claims description 8
- 238000005259 measurement Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 17
- 239000000853 adhesive Substances 0.000 abstract description 4
- 230000001070 adhesive effect Effects 0.000 abstract description 4
- 239000002131 composite material Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 description 25
- 238000010438 heat treatment Methods 0.000 description 23
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 11
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 11
- 230000008961 swelling Effects 0.000 description 11
- 239000004088 foaming agent Substances 0.000 description 9
- 229920005604 random copolymer Polymers 0.000 description 8
- 229920001971 elastomer Polymers 0.000 description 7
- 229920001400 block copolymer Polymers 0.000 description 5
- 230000006378 damage Effects 0.000 description 5
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 239000004711 α-olefin Substances 0.000 description 5
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 4
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 4
- 235000019399 azodicarbonamide Nutrition 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000008096 xylene Substances 0.000 description 4
- 239000004156 Azodicarbonamide Substances 0.000 description 3
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 229920001038 ethylene copolymer Polymers 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 238000005187 foaming Methods 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 229920000915 polyvinyl chloride Polymers 0.000 description 3
- 239000004800 polyvinyl chloride Substances 0.000 description 3
- 229910000077 silane Inorganic materials 0.000 description 3
- 238000005979 thermal decomposition reaction Methods 0.000 description 3
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 2
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 2
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 2
- 238000010382 chemical cross-linking Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 229920001903 high density polyethylene Polymers 0.000 description 2
- 239000004700 high-density polyethylene Substances 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 229920005679 linear ultra low density polyethylene Polymers 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920006124 polyolefin elastomer Polymers 0.000 description 2
- 229920001384 propylene homopolymer Polymers 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- 238000007666 vacuum forming Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002759 woven fabric Substances 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- YFYZPVXABJAXSL-UHFFFAOYSA-N 2,3-dinitrosobenzene-1,4-dicarboxamide Chemical compound NC(=O)C1=CC=C(C(N)=O)C(N=O)=C1N=O YFYZPVXABJAXSL-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- 229920000181 Ethylene propylene rubber Polymers 0.000 description 1
- 206010016322 Feeling abnormal Diseases 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- VJRITMATACIYAF-UHFFFAOYSA-N benzenesulfonohydrazide Chemical compound NNS(=O)(=O)C1=CC=CC=C1 VJRITMATACIYAF-UHFFFAOYSA-N 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- WXCZUWHSJWOTRV-UHFFFAOYSA-N but-1-ene;ethene Chemical compound C=C.CCC=C WXCZUWHSJWOTRV-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 229910001872 inorganic gas Inorganic materials 0.000 description 1
- 230000005865 ionizing radiation Effects 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 229920004889 linear high-density polyethylene Polymers 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- ALIFPGGMJDWMJH-UHFFFAOYSA-N n-phenyldiazenylaniline Chemical compound C=1C=CC=CC=1NN=NC1=CC=CC=C1 ALIFPGGMJDWMJH-UHFFFAOYSA-N 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001083 polybutene Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 229920005675 propylene-butene random copolymer Polymers 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- SCPYDCQAZCOKTP-UHFFFAOYSA-N silanol Chemical compound [SiH3]O SCPYDCQAZCOKTP-UHFFFAOYSA-N 0.000 description 1
- 125000003808 silyl group Chemical group [H][Si]([H])([H])[*] 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Molding Of Porous Articles (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、スキンモールド成
形法等により得られる自動車内装材の表皮材(クッショ
ン材)等として好適なポリプロピレン系樹脂架橋発泡シ
ート及び該発泡シートを積層した発泡粒子成形体の製造
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a crosslinked foamed polypropylene resin sheet suitable as a skin material (cushion material) for an automobile interior material obtained by a skin molding method or the like, and a foamed particle molded article obtained by laminating the foamed sheet. And a method for producing the same.
【0002】[0002]
【従来の技術】ポリプロピレン系樹脂架橋発泡シート
は、耐熱性、剛性、成形性、耐薬品性等の点で優れてい
るため、自動車内装材、家庭用品、建材等各種の分野で
用途開発がなされつつある素材である。例えば、スタン
ピングモールド成形法においては、ポリプロピレン系樹
脂架橋発泡シート上に溶融樹脂を積層し高圧条件下でプ
レス成形するという厳しい条件下での複合成形が行われ
ている。しかし、近年ポリプロピレン系樹脂架橋発泡シ
ートのスタンピングモールド成形品は、自動車天井材の
ような比較的形状が単純なものよりも更に形状が複雑な
ものが望まれるようになり、該発泡シートの良好な深絞
り成形性が要求されている。また、スタンピングモール
ド成形法における発泡シート用以外の用途として、樹脂
シートを装着した金型内に発泡粒子を充填し加熱媒体に
て加熱することにより両者を複合一体化するいわゆるス
キンモールド成形法における該樹脂シートとして使用で
きる接着性、成形性、耐熱性、緩衝性に優れたポリプロ
ピレン系樹脂架橋発泡シートが求められている。2. Description of the Related Art Crosslinked polypropylene resin foam sheets are excellent in heat resistance, rigidity, moldability, chemical resistance, etc., and have been developed for use in various fields such as automotive interior materials, household goods, and building materials. It is a growing material. For example, in the stamping molding method, composite molding is performed under severe conditions in which a molten resin is laminated on a crosslinked foamed polypropylene resin sheet and pressed under high pressure conditions. However, in recent years, a stamping molded product of a crosslinked foamed polypropylene resin sheet is desired to have a more complicated shape than a relatively simple shape such as an automobile ceiling material. Deep drawing formability is required. Further, as an application other than the foam sheet in the stamping molding method, the so-called skin molding method in which the two are compositely integrated by filling the foam particles in a mold equipped with a resin sheet and heating with a heating medium is used. There is a need for a crosslinked polypropylene resin foam sheet having excellent adhesiveness, moldability, heat resistance, and cushioning properties that can be used as a resin sheet.
【0003】[0003]
【発明が解決しようとする課題】本発明は、過酷な成形
加工を行っても、発泡体がつぶれたり破れたりすること
なく充分な緩衝性を維持し、かつ他の複合材料との接着
加工性が良好なポリプロピレン系樹脂架橋発泡シートを
提供することをその課題とする。また、前記発泡シート
を用いたスキンモールド成形法による積層発泡粒子成形
体の製造方法を提供することをその課題とする。DISCLOSURE OF THE INVENTION The present invention is intended to maintain a sufficient cushioning property without crushing or tearing of a foam even under severe molding processing, and to provide an adhesive workability with other composite materials. It is an object of the present invention to provide a cross-linked foamed polypropylene resin sheet having a good thermal conductivity. Another object of the present invention is to provide a method for producing a laminated foamed particle molded article by a skin molding method using the foamed sheet.
【0004】[0004]
【課題を解決するための手段】本発明者らは、前記課題
を解決すべく鋭意研究を重ねた結果、本発明を完成する
に至った。即ち、本発明によれば、ポリプロピレン系樹
脂を基材樹脂とする発泡シートであって、該発泡シート
の引張り測定における貯蔵弾性率が50℃で3×107
〜3×108dyn/cm2、100℃で1×107dy
n/cm2以上、130℃で1×106dyn/cm2以
上、140℃で4×105〜6×106dyn/cm2で
あり、かつ50℃、100℃、130℃、140℃での
tanδ(損失弾性率/貯蔵弾性率)の値が0.05以
上であることを特徴とするポリプロピレン系樹脂架橋発
泡シートが提供される。また、本発明によれば、前記ポ
リプロピレン系樹脂架橋発泡シートを金型内に装着した
後、金型内にポリプロピレン系樹脂発泡粒子を充填し、
スチームで加熱して発泡粒子相互を融着せしめるととも
に前記発泡粒子と発泡シートとを融着一体化することを
特徴とする発泡シート積層発泡粒子成形体の製造方法が
提供される。Means for Solving the Problems The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, have completed the present invention. That is, according to the present invention, a foamed sheet using a polypropylene-based resin as a base resin has a storage elastic modulus of 3 × 10 7 at 50 ° C. in a tensile measurement.
~ 3 × 10 8 dynes / cm 2 , 1 × 10 7 dy at 100 ° C.
n / cm 2 or more, 1 × 10 6 dyn / cm 2 or more at 130 ° C., 4 × 10 5 to 6 × 10 6 dyn / cm 2 at 140 ° C., and 50 ° C., 100 ° C., 130 ° C., 140 ° C. Tan δ (loss modulus / storage modulus) of 0.05 or more is provided. Further, according to the present invention, after mounting the polypropylene-based resin crosslinked foamed sheet in a mold, filling the mold with foamed polypropylene-based resin particles,
There is provided a method for producing a foamed sheet-laminated foamed particle molded article, characterized in that the foamed particles are fused together by heating with steam, and the foamed particles and the foamed sheet are fused and integrated.
【0005】[0005]
【発明の実施の形態】本発明のポリプロピレン系樹脂架
橋発泡シートは、その貯蔵弾性率が50℃で3×107
〜3×108dyn/cm2、好ましくは5×107〜2
×108dyn/cm2、100℃で1×107dyn/
cm2以上、好ましくは2×107〜6×108dyn/
cm2、130℃で1×106dyn/cm2以上、好ま
しくは3×106〜2×107dyn/cm2、140℃
で4×105〜6×106dyn/cm2、好ましくは6
×105〜5×106dyn/cm2であり、かつ50
℃、100℃、130℃、140℃でのtanδ(損失
弾性率/貯蔵弾性率)の値が0.05以上、好ましくは
0.06以上であることを特徴とするものである。な
お、本明細書において、発泡シートの貯蔵弾性率(dy
n/cm2)及びtanδ(損失弾性率/貯蔵弾性率)
値は、下記のようにして求めたものである。まず、発泡
シート表面から表層をスライスして幅5.0mm、厚み
1.3mmの試験片を作成する。なお、試験片は発泡シ
ート幅を5分割し各分割された範囲の発泡シート両面か
ら試験片の幅方向を発泡シートの幅方向と一致させスラ
イスを行い、一つの発泡シートから10個の試験片を得
る。次に測定装置として、レオメトリックサイエンティ
フィック社製の粘弾性測定装置SOLIDS ANAL
YZER RSAII、及びその付属品としてフィルムテ
ンションフィクスチュアーを使用し、初期チャック間を
スペーサーを用いて22.6mm±0.5mmに調節し
た後、前記試験片を取り付け、初期荷重を10gに調節
した後、オーブンを閉め昇温速度3℃/分で加熱し、1
Hz(6.28rad/sec)の周波数、設定歪0.
1%、オートテンション機能を使用して、前記試験片の
50℃、100℃、130℃、140℃での貯蔵弾性率
(dyn/cm2)及びtanδ値を求める。そして、
それらの各温度での貯蔵弾性率(dyn/cm2)及び
tanδ値の算術平均値をもって発泡シートの貯蔵弾性
率(dyn/cm2)及びtanδの値とする。DESCRIPTION OF THE PREFERRED EMBODIMENTS The crosslinked foamed polypropylene resin sheet of the present invention has a storage elastic modulus of 3 × 10 7 at 50 ° C.
33 × 10 8 dyn / cm 2 , preferably 5 × 10 7 to 2
× 10 8 dyn / cm 2 , 1 × 10 7 dyn /
cm 2 or more, preferably 2 × 10 7 to 6 × 10 8 dyn /
cm 2, 130 ° C. at 1 × 10 6 dyn / cm 2 or more, preferably 3 × 10 6 ~2 × 10 7 dyn / cm 2, 140 ℃
4 × 10 5 to 6 × 10 6 dyn / cm 2 , preferably 6
× 10 5 to 5 × 10 6 dyn / cm 2 , and 50
The value of tan δ (loss modulus / storage modulus) at ° C, 100 ° C, 130 ° C, and 140 ° C is 0.05 or more, preferably 0.06 or more. In this specification, the storage elastic modulus (dy) of the foamed sheet is used.
n / cm 2 ) and tan δ (loss modulus / storage modulus)
The values were determined as follows. First, the surface layer is sliced from the foam sheet surface to prepare a test piece having a width of 5.0 mm and a thickness of 1.3 mm. The width of the foam sheet was divided into five, the width direction of the test piece was matched with the width direction of the foam sheet from both sides of the foam sheet in each divided area, and the slice was performed. Get. Next, as a measuring device, a viscoelasticity measuring device SOLIDS ANAL manufactured by Rheometric Scientific Inc. was used.
Using YZER RSAII and a film tension fixture as its accessories, adjusting the initial gap between the chucks to 22.6 mm ± 0.5 mm using a spacer, attaching the test piece, and adjusting the initial load to 10 g. Then, close the oven and heat at a heating rate of 3 ° C / min.
Hz (6.28 rad / sec), set distortion 0.
The storage elastic modulus (dyn / cm 2 ) and tan δ value of the test piece at 50 ° C., 100 ° C., 130 ° C., and 140 ° C. are determined by using the auto tension function at 1%. And
They storage modulus at each temperature (dyn / cm 2) and tan [delta value arithmetic mean with a storage elastic modulus of the foam sheet (dyn / cm 2) and the value of tan [delta.
【0006】本発明において、貯蔵弾性率(dyn/c
m2)及びtanδの値を規定したのは次の理由によ
る。一般にポリプロピレン系樹脂架橋発泡体では、その
発泡体の成形性、耐熱性の指標としてゲル分率を用いて
いるが、それのみでは架橋状態を正確にとらえることが
できないため、成形性や他の樹脂との積層接着性等を正
確に関連づけることはできない。例えば、同様なゲル分
率でも架橋助剤の種類や添加量の違い、架橋条件の違い
等により発泡体の加熱時の挙動は大きく変化する。その
ため発泡体の加熱時の挙動を把握するには、前記のとお
り発泡シートの貯蔵弾性率(dyn/cm2)及びta
nδの値を指標とする必要がある。In the present invention, the storage modulus (dyn / c)
The values of m 2 ) and tan δ are specified for the following reasons. Generally, in the case of a crosslinked foam of a polypropylene resin, the gel fraction is used as an index of the moldability and heat resistance of the foam. However, it is not possible to accurately detect the crosslinked state by itself. It is not possible to accurately correlate the laminating adhesiveness with the like. For example, even when the gel fraction is the same, the behavior of the foam at the time of heating greatly changes due to a difference in the type and amount of the crosslinking aid and a difference in crosslinking conditions. Therefore, in order to grasp the behavior of the foam during heating, the storage elastic modulus (dyn / cm 2 ) and ta
It is necessary to use the value of nδ as an index.
【0007】本発明で特定する発泡シートの貯蔵弾性率
の指標について詳述すると、発泡シートにおいて熱変形
温度未満の貯蔵弾性率は発泡シートの通常使用時の圧縮
回復性、圧縮強度などをよく反映し、一方、熱変形温度
以上、結晶融解終了温度以下の貯蔵弾性率は発泡シート
加熱軟化時の気泡の維持、破壊、基材樹脂の溶融特性を
よく反映していると言える。具体的には、140℃にお
ける貯蔵弾性率が6×106dyn/cm2超の場合は、
スキンモールド成形時等で、他のポリプロピレン系樹脂
との融着やアンカー効果が低く、粘着性が低下する。ま
た、加熱真空成形では、加熱時の伸びが悪く深絞り成形
に適さない。一方140℃、130℃における貯蔵弾性
率がそれぞれ4×105dyn/cm2未満、1×106
dyn/cm2未満の場合は、加熱真空成型等では発泡
シートの表面の気泡に破れが生じやすく、また加熱成形
時間調整範囲が狭く生産性が悪い。また、スキンモール
ド成形や他のプロピレン系樹脂シート等を発泡シートに
接着させる等のシートへの加圧が1〜5kg/cm2あ
り、その圧力に耐えられずにつぶれてしまい、発泡シー
トの厚みが大幅に減少し出来上がった成形体は充分な緩
衝性を持たないものとなる。特に140℃における貯蔵
弾性率は、好ましくは6×105〜5×106dyn/c
m2であり、より好ましくは1×106〜5×106dy
n/cm2である。更に、130℃における貯蔵弾性率
は、好ましくは3×106〜2×107dyn/cm2で
ある。50℃における貯蔵弾性率が3×108dyn/
cm2超の場合は、発泡体としての充分な緩衝性が得ら
れない。また、スタンピングモールド成形に用いた場合
に均一な伸びが得られず、厚みむらや部分破壊が発生し
やすくなる。50℃及び100℃における貯蔵弾性率が
それぞれ、3×107dyn/cm2未満、1×107d
yn/cm2未満の場合は、少ない荷重でも変形が大き
く、つぶれやすいため、発泡体厚みを大きくする必要が
あり、コストアップにもなる。しかし、用途によって
は、厚みが限定されるため、必要な厚みが選択できない
場合があり、結果的に充分な緩衝性が得られない。The storage elasticity index of the foamed sheet specified in the present invention will be described in detail. In the foamed sheet, the storage elasticity below the heat distortion temperature well reflects the compression recovery property and the compressive strength of the foamed sheet during normal use. On the other hand, it can be said that the storage elastic modulus not lower than the heat distortion temperature and not higher than the crystal melting end temperature well reflects the maintenance and destruction of bubbles during the heating and softening of the foamed sheet and the melting characteristics of the base resin. Specifically, when the storage elastic modulus at 140 ° C. is more than 6 × 10 6 dyn / cm 2 ,
At the time of skin molding, etc., the adhesion to other polypropylene resin and the anchor effect are low, and the adhesiveness is reduced. Further, in the heating vacuum forming, the elongation at the time of heating is poor and is not suitable for deep drawing. On the other hand, the storage elastic modulus at 140 ° C. and 130 ° C. is less than 4 × 10 5 dyn / cm 2 , respectively, and 1 × 10 6
If it is less than dyn / cm 2, the bubbles on the surface of the foamed sheet are apt to be broken by heating vacuum molding or the like, and the heating molding time adjustment range is narrow, resulting in poor productivity. In addition, there is a pressure of 1 to 5 kg / cm 2 on the sheet, such as skin mold molding or bonding other propylene-based resin sheets to the foam sheet, and the sheet is crushed without withstanding the pressure, and the thickness of the foam sheet is reduced. Is significantly reduced, and the resulting molded article does not have sufficient cushioning properties. Particularly, the storage elastic modulus at 140 ° C. is preferably from 6 × 10 5 to 5 × 10 6 dyn / c.
m 2 , more preferably 1 × 10 6 to 5 × 10 6 dy
n / cm 2 . Further, the storage elastic modulus at 130 ° C. is preferably 3 × 10 6 to 2 × 10 7 dyn / cm 2 . The storage elastic modulus at 50 ° C. is 3 × 10 8 dyn /
If it exceeds cm 2 , sufficient cushioning properties as a foam cannot be obtained. Further, when used in stamping molding, uniform elongation cannot be obtained, and uneven thickness and partial destruction are likely to occur. Storage elastic modulus at 50 ° C. and 100 ° C. is less than 3 × 10 7 dyn / cm 2 and 1 × 10 7 d, respectively.
In the case of less than yn / cm 2 , deformation is large even with a small load, and it is easy to be crushed. However, depending on the application, the thickness is limited, so that the required thickness may not be selected, and as a result, a sufficient cushioning property cannot be obtained.
【0008】次に、本発明で特定する発泡シートのta
nδの指標について詳述すると、tanδ値は損失弾性
率と貯蔵弾性率との比であるためtanδ値が小さけれ
ば発泡シートの機械的変形に対して元に戻ろうとする性
質が強く、tanδ値が大きければ発泡シートの機械的
変形に対して変形した状態に止まっている性質が強いこ
とを意味する。従って、tanδ値が小さければ発泡シ
ートの成形において元に戻ろうとする力が発泡シートの
表面、薄肉部分等に集中する結果、発泡シートは破れ、
変形等が生じることになる。そこで、本発明において
は、50℃、100℃、130℃、140℃の各温度で
のtanδ(損失弾性率/貯蔵弾性率)の値が0.05
未満であると、成形を行っても形状保持しにくく、寸法
安定性が悪くなり、発泡シートに破れを生じることもあ
る。[0008] Next, ta of the foam sheet specified in the present invention.
When the index of nδ is described in detail, the tan δ value is a ratio of the loss elastic modulus and the storage elastic modulus, so that if the tan δ value is small, the property of trying to return to the mechanical deformation of the foamed sheet is strong, and the tan δ value is A larger size means that the foamed sheet is more likely to remain deformed with respect to mechanical deformation. Therefore, if the tan δ value is small, the force of returning to the original state in the molding of the foamed sheet is concentrated on the surface of the foamed sheet, a thin portion, and the like, and the foamed sheet is torn,
Deformation will occur. Therefore, in the present invention, the value of tan δ (loss modulus / storage modulus) at each of 50 ° C., 100 ° C., 130 ° C., and 140 ° C. is 0.05.
If it is less than 3, the shape is difficult to maintain even after molding, the dimensional stability is deteriorated, and the foamed sheet may be broken.
【0009】本発明のポリプロピレン系樹脂架橋発泡シ
ートの基材樹脂であるポリプロピレン系樹脂は、ポリプ
ロピレン、50重量%以上のポリプロピレンとポリエチ
レン等の他の熱可塑性樹脂との混合物等が挙げられる。
前記ポリプロピレンとしては、プロピレンホモポリマ
ー、プロピレン/エチレン共重合体やプロピレン/α−
オレフィン共重合体を挙げることができる。ここで、α
−オレフィンには、ブテン−1、ペンテン−1、ヘキセ
ン−1、4−メチルペンテン等炭素数が4〜10のα−
オレフィンが包含される。前記プロピレン/エチレン共
重合体、プロピレン/α−オレフィン共重合体としては
エチレン/プロピレンランダム共重合体、同ブロック共
重合体、ブテン/プロピレンランダム共重合体、同ブロ
ック共重合体、エチレン/プロピレン/ブテンランダム
共重合体、同ブロック共重合体等が挙げられる。なかで
も、エチレン/プロピレンランダム共重合体、同ブロッ
ク共重合体が好ましく、更にはエチレン/プロピレンラ
ンダム共重合体が好ましい。プロピレン/エチレン共重
合体又はプロピレン/α−オレフィン共重合体中のエチ
レン又はα−オレフィンの含有量は、1〜30重量%、
好ましくは1〜8重量%である。なお、前記他の熱可塑
性樹脂としてはポリエチレン、ポリスチレン、ポリ塩化
ビニル、アクリル樹脂、エチレン/酢酸ビニル共重合体
等が挙げられ、特にポリエチレンとしては、低密度ポリ
エチレン、高密度ポリエチレン、直鎖状低密度ポリエチ
レン、直鎖状超低密度ポリエチレン等が挙げられる。ま
た、本発明においては、基材樹脂に対して柔軟性を向上
させたり、また他の特性を付与させることを目的として
エチレン/プロピレンラバー等のゴム成分を配合しても
よい。ゴム成分の添加量は30重量%未満、通常2〜2
5重量%の範囲にするのが好ましい。The polypropylene resin as the base resin of the crosslinked foamed polypropylene resin sheet of the present invention includes polypropylene, a mixture of 50% by weight or more of polypropylene and another thermoplastic resin such as polyethylene, and the like.
Examples of the polypropylene include propylene homopolymer, propylene / ethylene copolymer and propylene / α-
Olefin copolymers can be mentioned. Where α
-Olefins such as butene-1, pentene-1, hexene-1, and 4-methylpentene having 4 to 10 carbon atoms;
Olefins are included. Examples of the propylene / ethylene copolymer and propylene / α-olefin copolymer include ethylene / propylene random copolymer, same block copolymer, butene / propylene random copolymer, same block copolymer, and ethylene / propylene / Butene random copolymers and the same block copolymers. Among them, ethylene / propylene random copolymers and block copolymers are preferred, and ethylene / propylene random copolymers are more preferred. The content of ethylene or α-olefin in the propylene / ethylene copolymer or propylene / α-olefin copolymer is 1 to 30% by weight,
Preferably it is 1 to 8% by weight. Examples of the other thermoplastic resin include polyethylene, polystyrene, polyvinyl chloride, acrylic resin, and ethylene / vinyl acetate copolymer. Particularly, polyethylene includes low-density polyethylene, high-density polyethylene, linear High-density polyethylene, linear ultra-low-density polyethylene, and the like. Further, in the present invention, a rubber component such as ethylene / propylene rubber may be blended for the purpose of improving flexibility and imparting other properties to the base resin. The amount of the rubber component added is less than 30% by weight, usually 2 to 2%.
Preferably it is in the range of 5% by weight.
【0010】ポリプロピレン系樹脂架橋発泡シートの製
造は次のようにして行う。押出機に前記基材樹脂と熱分
解型発泡剤、必要に応じてジビニルベンゼン等の架橋促
進剤を供給し、熱分解型発泡剤の分解開始温度未満の温
度で混練し発泡性溶融ゲルを得、該発泡性溶融ゲルを押
出機先端に取り付けたTダイより発泡させることなく押
出し、直ちにカレンダーロールにかけ発泡性ポリプロピ
レン系樹脂シートを得る。続いて発泡性ポリプロピレン
系樹脂シートに架橋処理を行った後、該シートを加熱炉
に導入して発泡剤を分解させることによりポリプロピレ
ン系樹脂架橋発泡シートを得ることができる。The production of the crosslinked foamed polypropylene resin sheet is carried out as follows. The extruder is supplied with the base resin and the thermal decomposition type foaming agent, and a crosslinking accelerator such as divinylbenzene as necessary, and kneaded at a temperature lower than the decomposition start temperature of the thermal decomposition type foaming agent to obtain a foamable molten gel. The foamable molten gel is extruded from a T-die attached to the tip of the extruder without foaming, and is immediately applied to a calender roll to obtain a foamable polypropylene resin sheet. Subsequently, after performing a cross-linking treatment on the expandable polypropylene-based resin sheet, the sheet is introduced into a heating furnace to decompose the foaming agent, whereby a cross-linked foamed polypropylene-based resin sheet can be obtained.
【0011】熱分解型発泡剤としては、アゾジカルボン
アミド、アゾビスホルムアミド、N,N−ジニトロソペ
ンタメチレンテトラミン、ジアゾアミノベンゼン、ベン
ゼンスルホニルヒドラジド、P,P−オキシビスベンゼ
ンスルホニルヒドラジド、N,N−ジニトロソテレフタ
ルアミド等が挙げられ、これらのうち、熱安定性及び分
解開始温度の高さからアゾジカルボンアミドが最も好ま
しい。これらの発泡剤は、一種のもののみを単独で用い
る他、複数種のものを混合して用いることもできる。本
発明における前記熱分解型発泡剤の使用量は、基材樹脂
100重量部当り、0.2〜30重量部、好ましくは1
〜20重量部の割合である。Examples of the thermal decomposition type blowing agent include azodicarbonamide, azobisformamide, N, N-dinitrosopentamethylenetetramine, diazoaminobenzene, benzenesulfonylhydrazide, P, P-oxybisbenzenesulfonylhydrazide, N, N And dinitrosoterephthalamide. Among them, azodicarbonamide is most preferred in view of thermal stability and high decomposition initiation temperature. These foaming agents may be used alone or in combination of two or more. The amount of the pyrolytic foaming agent used in the present invention is 0.2 to 30 parts by weight, preferably 1 to 100 parts by weight of the base resin.
-20 parts by weight.
【0012】なお、本発明における発泡シートの架橋方
法としては、電離性放射架橋、化学架橋剤を用いたいわ
ゆる化学架橋、樹脂にシリル基を導入して架橋させるい
わゆるシラン架橋等の方法を採用することができる。特
に、シラン架橋による方法は、発泡シートを構成する基
材樹脂に架橋構造を導入することによりシート表面から
内部まで均一な架橋構造が得られるため好ましく、また
得られる発泡シートの物性が均一なものとなる。更に、
理由は定かではないが発泡シート表面の平滑性も格段に
良化する。As the method of crosslinking the foamed sheet in the present invention, a method such as ionizing radiation crosslinking, so-called chemical crosslinking using a chemical crosslinking agent, or so-called silane crosslinking in which a silyl group is introduced into a resin to perform crosslinking is employed. be able to. In particular, the silane cross-linking method is preferable because a uniform cross-linking structure is obtained from the sheet surface to the inside by introducing a cross-linking structure into the base resin constituting the foamed sheet, and the obtained foamed sheet has uniform physical properties. Becomes Furthermore,
Although the reason is not clear, the smoothness of the foam sheet surface is also significantly improved.
【0013】一般にポリプロピレン系樹脂架橋発泡体で
は、発泡体の密度の他に加熱成形性に関連する架橋状態
の指標としてゲル分率を用いているが、それのみでは架
橋状態と加熱成形性や、他の樹脂との接着性等を関連づ
けることはできない。例えば、同様なゲル分率でも架橋
助剤の種類や添加量の違い、架橋条件の違い等により発
泡体の加熱時の挙動は大きく変化する。そのため発泡体
の加熱時の挙動を把握するには、ゲル分率に加えて膨潤
度を調整するのがよい。よって、本発明のポリプロピレ
ン系樹脂架橋発泡シートはゲル分率、膨潤度を調整する
ことによって得られる。しかし、本発明の該発泡シート
を得るために目標とする発泡シートのゲル分率と膨潤度
の調整範囲は、前記したように架橋方法によって異なる
ためシラン架橋発泡シート、化学架橋発泡シート、放射
線架橋発泡シート毎に違いがあることに注意しなければ
ならない。これは、架橋発泡シートの架橋構造の均一性
や架橋構造の違いによるものと考えられる。調整の指標
として、膨潤度が大きすぎる場合やゲル分率が小さすぎ
る場合は発泡シートの130℃及び140℃における貯
蔵弾性率がそれぞれ、1×106dyn/cm2未満及び
4×105dyn/cm2未満となる傾向にある。一方、
膨潤度が小さすぎる場合やゲル分率が大きすぎる場合は
発泡シートの貯蔵弾性率が140℃で6×106dyn
/cm2超となる傾向にある。In general, in a crosslinked polypropylene resin foam, the gel fraction is used as an index of the crosslinked state related to the heat moldability, in addition to the density of the foam. Adhesiveness with other resins cannot be related. For example, even when the gel fraction is the same, the behavior of the foam at the time of heating greatly changes due to a difference in the type and amount of the crosslinking aid and a difference in crosslinking conditions. Therefore, in order to grasp the behavior of the foam during heating, it is preferable to adjust the degree of swelling in addition to the gel fraction. Therefore, the crosslinked polypropylene resin foam sheet of the present invention can be obtained by adjusting the gel fraction and the degree of swelling. However, the adjustment range of the gel fraction and the degree of swelling of the foamed sheet targeted for obtaining the foamed sheet of the present invention is different depending on the crosslinking method as described above, so that the silane crosslinked foamed sheet, the chemically crosslinked foamed sheet, the radiation crosslinked It should be noted that there are differences between foam sheets. This is considered to be due to the uniformity of the crosslinked structure and the difference in the crosslinked structure of the crosslinked foamed sheet. When the degree of swelling is too large or the gel fraction is too small, the storage modulus of the foamed sheet at 130 ° C. and 140 ° C. is less than 1 × 10 6 dyn / cm 2 and 4 × 10 5 dyn, respectively. / Cm 2 . on the other hand,
When the degree of swelling is too small or the gel fraction is too large, the storage elastic modulus of the foamed sheet is 6 × 10 6 dyn at 140 ° C.
/ Cm 2 .
【0014】本発明において前記粘弾性特性を有するポ
リプロピレン系樹脂架橋発泡シートは、前記基材樹脂を
使用し前述のとおり発泡シートを得る際に、例えばポリ
プロピレン系樹脂シラン架橋発泡シートの場合、見掛け
密度が0.03〜0.2g/cm3、好ましくは0.0
36〜0.100g/cm3の発泡シートとなるように
発泡剤の種類、添加量を調整し、シラングラフトプロピ
レン系樹脂の添加量を20〜90重量%、好ましくは3
0〜70重量%とし、ゲル分率が25〜70%、好まし
くは30〜60%、膨潤度が1000〜9000%、好
ましくは2000〜8000%となるように原料配合、
製造条件等を選択し架橋発泡性シートを得、該架橋発泡
性シートの加熱発泡条件を調節することにより得られ
る。In the present invention, the polypropylene resin crosslinked foamed sheet having the viscoelastic properties is obtained by using the base resin as described above to obtain a foamed sheet. Is 0.03 to 0.2 g / cm 3 , preferably 0.03 to 0.2 g / cm 3 .
The type and amount of the foaming agent are adjusted so as to obtain a foamed sheet of 36 to 0.100 g / cm 3 , and the amount of the silane-grafted propylene-based resin is adjusted to 20 to 90% by weight, preferably 3 to 30% by weight.
0 to 70% by weight, the raw materials are blended so that the gel fraction is 25 to 70%, preferably 30 to 60%, and the degree of swelling is 1000 to 9000%, preferably 2000 to 8000%.
The crosslinked foamable sheet is obtained by selecting the production conditions and the like, and the crosslinked foamable sheet is obtained by adjusting the heating and foaming conditions.
【0015】なお、本明細書において、ゲル分率とは、
ポリプロピレン系樹脂架橋発泡シートの架橋割合を示す
ものであって、その値は、該発泡シートから約1gの試
料を切り出してその重量を測定し、この試料をキシレン
200ml中に投入し、24時間加熱還流後、JIS
Z 8801(1966年)に定められている74μm
の金網で不溶分を速やかにろ過し、ついでその不溶分を
24時間減圧乾燥した後に、その不溶分を試料としても
う一度同じ操作(還流から減圧乾燥まで)を繰り返して
最終的に残った不溶分の重量(g)を測定し、次式によ
り算出される。 ゲル分率(%)=(不溶分重量/測定に使用された試料
重量)×100 また、膨潤度とは、ゲル分率の測定と同様に試料をキシ
レン中に投入し加熱還流後、200メッシュの金網でろ
過し、キシレン溶出分を除去した残渣を直ちに密閉容器
に入れてキシレン膨潤時の残渣重量を測定し、次いでそ
の残渣を24時間減圧乾燥させ乾燥残渣重量を測定し、
次式により算出される。 膨潤度(%)=(キシレン膨潤時残渣重量/乾燥残渣重
量)×100In the present specification, the gel fraction is defined as
It shows the cross-linking ratio of the cross-linked foamed polypropylene resin sheet. The value is measured by cutting out a sample of about 1 g from the foamed sheet, weighing the sample, placing the sample in 200 ml of xylene, and heating for 24 hours. After reflux, JIS
74 μm specified in Z8801 (1966)
The insolubles were quickly filtered through a wire mesh, and the insolubles were dried under reduced pressure for 24 hours. The same operation (from reflux to drying under reduced pressure) was repeated once again using the insolubles as a sample, and finally the remaining insolubles were removed. The weight (g) is measured and calculated by the following equation. Gel fraction (%) = (weight of insoluble matter / weight of sample used for measurement) × 100 The degree of swelling is the same as in the measurement of the gel fraction. The residue from which xylene eluted was removed was immediately placed in a sealed container, and the weight of the residue upon swelling of xylene was measured.Then, the residue was dried under reduced pressure for 24 hours to measure the dry residue weight.
It is calculated by the following equation. Degree of swelling (%) = (weight of residue upon swelling xylene / weight of dry residue) × 100
【0016】前記のようにして得られた本発明のポリプ
ロピレン系樹脂架橋発泡シートは、その密度は0.03
〜0.2g/cm3が好ましく、0.036〜0.1g
/cm3がより好ましい。また、その厚みは、1〜20
mmが好ましく、2〜5mmがより好ましい。The crosslinked foamed polypropylene resin sheet of the present invention obtained as described above has a density of 0.03.
-0.2 g / cm 3 , preferably 0.036-0.1 g
/ Cm 3 is more preferred. The thickness is 1 to 20
mm is preferable, and 2-5 mm is more preferable.
【0017】次いで、前記ポリプロピレン系樹脂架橋発
泡シートを使用した本願発明のいわゆるスキンモールド
成形法による発泡シート積層発泡粒子成形体の製造方法
について説明する。本発明で使用されるポリプロピレン
系樹脂発泡粒子に用いられるポリプロピレン系樹脂は、
(1)プロピレンホモポリマー、及び(2)プロピレン
−エチレンブロックコポリマー、プロピレン−エチレン
ランダムコポリマー、プロピレン−ブテンランダムコポ
リマー、プロピレン−エチレン−ブテンランダムコポリ
マー等のプロピレン含有量が70重量%以上のプロピレ
ン系コポリマーの群から選択される1又は2以上を主成
分(但し、ここでは70重量%以上を意味する)とする
ものである。そのような主成分ポリプロピレン系樹脂
は、発泡粒子の型内成形体、ひいては表皮材付発泡成形
体に耐熱性及び剛性を付与するために、その融点が13
0℃以上のもの、好ましくは135℃以上のものの使用
が望まれる。ただし、その融点の上限を166℃にする
と、設備費を安く抑えることが可能となるので望まし
い。また、各種目的に応じて副成分ポリマーを主成分ポ
リプロピレン系樹脂にブレンドしてもよい。そのような
副成分としては、直鎖状超低密度ポリエチレン、分岐低
密度ポリエチレン樹脂、直鎖状低密度ポリエチレン樹
脂、中密度ポリエチレン樹脂、高密度ポリエチレン樹脂
等のポリエチレン系樹脂;エチレン−プロピレンラバ
ー、エチレン−ブテンラバー、エチレン−オクテンラバ
ー、プロピレン−ブテンラバー等のポリオレフィン系エ
ラストマー;及びポリブテン樹脂から選択される1又は
2以上のポリオレフィン系(コ)ポリマーが例示され
る。Next, a method of producing a foamed sheet-laminated foamed particle molded article by the so-called skin mold molding method of the present invention using the polypropylene resin crosslinked foamed sheet will be described. The polypropylene resin used for the expanded polypropylene resin particles used in the present invention,
(1) a propylene homopolymer, and (2) a propylene-based copolymer having a propylene content of 70% by weight or more, such as a propylene-ethylene block copolymer, a propylene-ethylene random copolymer, a propylene-butene random copolymer, and a propylene-ethylene-butene random copolymer. The main component is 1 or 2 or more selected from the group of (herein, it means 70% by weight or more). Such a main component polypropylene-based resin has a melting point of 13 in order to impart heat resistance and rigidity to an in-mold molded article of foamed particles, and further to a foamed molded article with a skin material.
It is desired to use those having a temperature of 0 ° C or higher, preferably 135 ° C or higher. However, it is desirable to set the upper limit of the melting point to 166 ° C., because the equipment cost can be reduced. Further, the auxiliary component polymer may be blended with the main component polypropylene resin according to various purposes. Such sub-components include polyethylene resins such as linear ultra low density polyethylene, branched low density polyethylene resin, linear low density polyethylene resin, medium density polyethylene resin, and high density polyethylene resin; ethylene-propylene rubber; Examples thereof include polyolefin-based elastomers such as ethylene-butene rubber, ethylene-octene rubber, and propylene-butene rubber; and one or more polyolefin-based (co) polymers selected from polybutene resins.
【0018】前記ポリプロピレン系樹脂発泡粒子の製造
方法としては、例えば、密閉された耐圧容器中で、ポリ
プロピレン系樹脂粒子を水中で撹拌しながら、無機ガス
系発泡剤又は/及び揮発性有機発泡剤を含侵させ、加圧
下で所定の発泡温度まで加熱した後、低圧域に放出する
等の従来公知の方法が挙げられるが、本発明は、かかる
方法によって限定されるものではない。ポリプロピレン
系樹脂発泡粒子の嵩発泡倍率は、3〜60倍が好まし
い。更に好ましくは、3〜20倍である。また、発泡粒
子を構成するポリプロピレン系樹中には特開昭61−4
738号公報で説明されているような二次結晶が存在し
ていることが望ましい。As a method for producing the polypropylene resin foam particles, for example, an inorganic gas foaming agent and / or a volatile organic foaming agent are mixed in a sealed pressure vessel while stirring the polypropylene resin particles in water. Conventionally known methods such as impregnation, heating to a predetermined foaming temperature under pressure, and then discharging to a low pressure region may be mentioned, but the present invention is not limited by such a method. The bulk expansion ratio of the expanded polypropylene resin particles is preferably 3 to 60 times. More preferably, it is 3 to 20 times. Further, among the polypropylene-based trees constituting the foamed particles, Japanese Patent Application Laid-Open No.
It is desirable that a secondary crystal as described in Japanese Patent No. 738 is present.
【0019】発泡シート積層発泡粒子成形体は、前記発
泡粒子の型内成形と同時に型内に配した架橋発泡シート
(表皮材)を一体成形することによって製造される。そ
の方法を図面に従いながら説明する。図1は、一体成形
用金型の一例の概略で、これによって架橋発泡シート積
層発泡粒子成形体が製造される。まず、ポリプロピレン
系樹脂架橋発泡シート1を、金型A(2a)側に配置し
て真空吸引管3aより吸引して金型Aに添わせる。この
際、発泡シート1として、金型Aの内面形状に添わせる
ことが出来るような形状に予め熱成形されたものを使用
することも可能であり、また発泡シート1を金型Aの周
囲で固定して、加熱することなく金型Aの内面に向けて
吸引密着させたり、あるいは必要に応じて加熱軟化させ
てから金型Aの内面に向けて真空成形や圧縮成形等して
使用することも可能である。続いて、金型Aと金型B
(2b)とを型合わせした時に発泡シート1と金型Bと
の間に形成されるキャビティ4内にポリプロピレン系樹
脂発泡粒子Pをフィダー11を通じて充填した後、発泡
粒子の型内成形に必要な加圧スチームをスチーム導入管
8bよりチャンバー7bを通して発泡粒子間に供給し加
熱して型内成形を行って発泡シート積層発泡成形体を得
る。なお、加圧スチームはスチーム導入管8aよりチャ
ンバー7aにも供給されるが、キャビティ4へは供給さ
れず金型A(2a)面を加熱するのみである。金型Aに
は、発泡シート1を金型A(2a)に向けて成形または
密着させるために、0.2−1.0mm径の真空吸引孔
5が複数個設けられており、一方、金型Bには、キャビ
ティ4内の発泡粒子に向けて加圧スチームを供給するた
めのスリット孔6等が設けられている。また、冷却のた
めに冷却水導入管9a、9bが設けられ、冷却水の排水
のためにドレン排出管10a、10bが設けられてい
る。The foamed sheet laminated foamed particle molded article is manufactured by integrally molding a crosslinked foamed sheet (skin material) disposed in a mold at the same time as molding the foamed particles in the mold. The method will be described with reference to the drawings. FIG. 1 is a schematic view of an example of a mold for integral molding, whereby a crosslinked foamed sheet laminated foamed particle molded article is manufactured. First, the cross-linked foamed polypropylene resin sheet 1 is placed on the mold A (2a) side, suctioned from the vacuum suction pipe 3a, and attached to the mold A. At this time, it is also possible to use, as the foamed sheet 1, one that has been thermoformed in advance into a shape that can conform to the inner surface shape of the mold A. Use by fixing and suction-adhering to the inner surface of the mold A without heating, or by heating and softening as necessary, and then vacuum forming or compressing the inner surface of the mold A. Is also possible. Then, mold A and mold B
After filling the polypropylene resin expanded particles P into the cavity 4 formed between the expanded sheet 1 and the mold B when the (2b) is matched with the mold through the feeder 11, it is necessary for in-mold molding of the expanded particles. Pressurized steam is supplied between the foamed particles through the chamber 7b from the steam introduction pipe 8b and heated to perform in-mold molding to obtain a foamed sheet laminated foamed body. The pressurized steam is also supplied to the chamber 7a from the steam introduction pipe 8a, but is not supplied to the cavity 4, but only heats the surface of the mold A (2a). The mold A is provided with a plurality of vacuum suction holes 5 having a diameter of 0.2 to 1.0 mm in order to form or adhere the foam sheet 1 toward the mold A (2a). The mold B is provided with slit holes 6 and the like for supplying pressurized steam toward the foamed particles in the cavity 4. Further, cooling water introduction pipes 9a and 9b are provided for cooling, and drain discharge pipes 10a and 10b are provided for draining the cooling water.
【0020】発泡シート積層発泡粒子成形体がクッショ
ン材として使用される場合には、ポリプロピレン系樹脂
架橋発泡シートはその表面が表面材によってラミネート
されていることが好ましい。ラミネートは、通常、発泡
シートの製造後に行われる。表面材としては、ポリ塩化
ビニルやポリオレフィン系エラストマー等からなるシー
トの他、ポリエステル系の織布・不織布、ポリプロピレ
ン系の織布・不織布といった、車両等の内装表面材に使
用される装飾性の高い素材が例示される。従って、該素
材がポリ塩化ビニルやポリオレフィン系エラストマー等
からなるシートの場合、シボ模様等が転写されているこ
とが外観上望ましい。これら表面材は、前記架橋発泡シ
ートと熱接着性がある場合には接着剤を使用することな
く熱接着されることが望ましい。なお、表面材が架橋発
泡シートと熱接着性がない場合には接着剤の使用が必要
となる。When the foamed sheet laminated foamed particle molded article is used as a cushion material, it is preferable that the surface of the crosslinked polypropylene resin foamed sheet is laminated with a surface material. Lamination is usually performed after the production of the foamed sheet. As the surface material, in addition to sheets made of polyvinyl chloride or polyolefin elastomer, highly decorative materials used for interior surface materials of vehicles and the like, such as polyester woven fabric / nonwoven fabric and polypropylene woven fabric / nonwoven fabric. The material is exemplified. Therefore, when the material is a sheet made of polyvinyl chloride, polyolefin elastomer, or the like, it is desirable in appearance that a grain pattern or the like is transferred. When these surface materials have thermal adhesiveness to the crosslinked foamed sheet, it is desirable that they are thermally bonded without using an adhesive. When the surface material does not have thermal adhesiveness to the crosslinked foam sheet, it is necessary to use an adhesive.
【0021】また、発泡シート積層発泡粒子成形体(表
皮材付発泡粒子成形体)が車両内装材に使用される場合
には、ポリプロピレン系樹脂架橋発泡シートにソフト感
を持たせ、ポリプロピレン系樹脂発泡粒子の型内成形体
には軽量で剛性(保形性)を持たせることが望まれ、そ
のためには、架橋発泡シートの見掛け密度を0.02〜
0.09g/cm3、より好ましくは0.03〜0.0
6g/cm3、厚みを1〜10mm、より好ましくは2
〜5mmにし、かつ型内発泡粒子成形体の見掛け密度を
0.036〜0.3g/cm3、より好ましくは0.0
45〜0.18g/cm3とするとよい。When a foamed sheet laminated foamed particle molded article (foamed particle molded article with a skin material) is used for a vehicle interior material, the polypropylene resin crosslinked foamed sheet has a soft feeling, and the polypropylene resin foam It is desired that the in-mold molded product of the particles be lightweight and have rigidity (shape retention), and for that purpose, the apparent density of the crosslinked foamed sheet is set to 0.02 to 0.02.
0.09 g / cm 3 , more preferably 0.03 to 0.0
6 g / cm 3 , thickness 1-10 mm, more preferably 2
To 5 mm, and the apparent density of the in-mold foamed particle molded product is 0.036 to 0.3 g / cm 3 , more preferably 0.03 to 0.3 g / cm 3 .
It is good to be 45-0.18 g / cm 3 .
【0022】[0022]
【実施例】次に、本発明を実施例によって更に詳細に説
明する。 実施例1〜4及び比較例1、2 表1に示す量のシラノール縮合触媒、アゾジカルボンア
ミド(熱分解型発泡剤)と表1に示す基材樹脂とを二軸
押出機に供給し、発泡剤の分解温度未満の温度条件下で
溶融混練し、押出機先端に取り付けた410mm幅のコ
ートハンガータイプのTダイより押出し、直ちにカレン
ダーロールにかけてシート状成形体を得た。得られた成
形体を水分の存在下で架橋させ、架橋発泡性シートを得
た。得られた架橋発泡性シートの膨潤度を表1に併せて
示す。次に、架橋発泡性シートを加熱炉内で雰囲気温度
220〜240℃の加熱条件にて加熱することにより架
橋発泡シートを得た。得られた架橋発泡シートのみかけ
の密度、貯蔵弾性率及びtanδ値を表2に示す。次
に、架橋発泡シートを200mm角に切り出し、これを
縦200mm×横500mm×厚み20mmのキャビテ
ィ空間を持つ成形機に架橋発泡シートが図1に示す金型
Aの内表面に密着するように金型Aに形成された吸引孔
を通して真空ポンプを用いて吸引固定し、次いで金型A
と金型Bとを型締めして、キャビティ4に、発泡粒子内
の空気圧が2.5気圧となるように予め調整されたプロ
ピレン−エチレンランダム共重合体(エチレン成分2.
4重量%、融点146.0℃)の発泡粒子(嵩発泡倍率
15倍)を金型B側から充填した。更に、金型B側チャ
ンバーに、ドレン弁を開いたまま5秒間スチームを導入
して発泡粒子間に存在する空気を排気した後、ドレン弁
を締めて、金型Bからのみ発泡粒子に向けて3.8kg
/cm2Gのスチームを導入すると共に、金型Aのスチ
ームチャンバー内に2kg/cm2Gのスチームを導入
して成形を行った後、水冷し、片面に架橋発泡シート
(表皮材)が一体に積層された発泡粒子成形体を得た。Next, the present invention will be described in more detail by way of examples. Examples 1 to 4 and Comparative Examples 1 and 2 The amounts of the silanol condensation catalyst, azodicarbonamide (pyrolytic foaming agent) shown in Table 1 and the base resin shown in Table 1 were supplied to a twin-screw extruder and foamed. The mixture was melt-kneaded under a temperature condition lower than the decomposition temperature of the agent, extruded from a 410 mm wide coat hanger type T die attached to the tip of the extruder, and immediately applied to a calender roll to obtain a sheet-like molded product. The obtained molded article was crosslinked in the presence of moisture to obtain a crosslinked foamable sheet. The swelling degree of the obtained crosslinked foamable sheet is also shown in Table 1. Next, the cross-linked foamable sheet was obtained by heating the cross-linked foamable sheet in a heating furnace under a heating condition of an ambient temperature of 220 to 240 ° C. Table 2 shows the apparent density, storage modulus and tan δ value of the obtained crosslinked foamed sheet. Next, the crosslinked foamed sheet was cut into a 200 mm square, and this was cut into a molding machine having a cavity space of 200 mm (length) × 500 mm (width) × 20 mm (thickness) so that the crosslinked foamed sheet adhered to the inner surface of the mold A shown in FIG. Using a vacuum pump to suction-fix through the suction holes formed in the mold A, then mold A
And the mold B, and the cavity 4 is filled in the cavity 4 with a propylene-ethylene random copolymer (ethylene component 2.) which has been adjusted in advance so that the air pressure in the foamed particles becomes 2.5 atm.
Foamed particles (4% by weight, melting point: 146.0 ° C.) (bulk expansion ratio: 15 times) were filled from the mold B side. Further, steam was introduced into the chamber on the mold B side for 5 seconds while the drain valve was opened to exhaust air existing between the foamed particles, and then the drain valve was closed. 3.8 kg
/ Cm 2 G steam and 2 kg / cm 2 G steam were introduced into the mold A steam chamber, followed by molding, followed by water cooling, and a cross-linked foam sheet (skin material) integrated on one side. Was obtained.
【0023】得られた架橋発泡シート積層発泡粒子成形
体について、架橋発泡シートの接着性、架橋発泡シート
の厚み、架橋発泡シートの成形性を次の評価基準に基づ
いて評価し、その結果を表2に示した。 (架橋発泡シートの接着性) ○:発泡シート剥離面において発泡シートの全面に材料
破壊が見られる。 △:発泡シート剥離面において発泡シートに部分的に材
料破壊が見られる。 ×:発泡シート剥離面において発泡シートに全く材料破
壊が見られない。 (架橋発泡シートの厚み維持性) ○:成形前の発泡シートの厚みがほぼ維持されている。 △:成形前の発泡シートの厚みが半分以下につぶれてい
るが発泡シートとしての緩衝性が残されている。 ×:成形前の発泡シートの厚みがほとんど残っておら
ず、発泡シートとしての緩衝性が感触で確認できない。 (架橋発泡シートの成形性) ○:成形体において発泡シートが全体に均一な厚みをも
っており、型通りのシャープな成形体が得られる。 △:成形体コーナー部等、部分的に発泡シートが薄くな
るが、型通りのシャープな成形体が得られる。 ×:加熱時にドローダウンや、発泡体シートが切断する
などの問題があり、良好な成形体が得られない。With respect to the obtained crosslinked foamed sheet laminated foamed particle molded article, the adhesiveness of the crosslinked foamed sheet, the thickness of the crosslinked foamed sheet, and the moldability of the crosslinked foamed sheet were evaluated based on the following evaluation criteria. 2 is shown. (Adhesiveness of crosslinked foamed sheet) :: Material destruction is observed on the entire surface of the foamed sheet on the peeled surface of the foamed sheet. Δ: Material destruction is partially observed in the foam sheet on the foam sheet release surface. X: No material destruction is observed in the foamed sheet on the foamed sheet peeling surface. (Thickness maintenance of crosslinked foamed sheet) ○: The thickness of the foamed sheet before molding is almost maintained. Δ: The thickness of the foam sheet before molding was crushed by half or less, but the cushioning property of the foam sheet was left. X: The thickness of the foam sheet before molding hardly remains, and the cushioning property of the foam sheet cannot be confirmed by touch. (Formability of crosslinked foamed sheet) :: The foamed sheet in the molded article has a uniform thickness as a whole, and a sharp molded article according to the mold can be obtained. Δ: The foamed sheet is partially thin, such as at the corner of the molded body, but a sharp molded body according to the mold is obtained. ×: There are problems such as drawdown during heating and cutting of the foam sheet, and a good molded body cannot be obtained.
【0024】[0024]
【表1】 [Table 1]
【0025】[0025]
【表2】 [Table 2]
【0026】[0026]
【発明の効果】本発明のポリプロピレン系樹脂架橋発泡
シートは、真空、圧空等による金型成形において耐熱性
に優れるため、該シート加熱時にシートの表面の気泡が
熱により破れてしまうようなことがなく、また深絞り成
形性に優れ、加熱成形可能な温度範囲が広い。そして、
柔軟性、緩衝性にも優れたものである。殊に、本発明の
前記発泡シートを用いて、いわゆるスキンモールド成形
法によって好適に発泡シート積層発泡粒子成形体を製造
することができる。この製造方法によれば、前記発泡シ
ートと発泡シートと発泡粒子成形体との接着性がよく、
成形時の破れや成形体の収縮がなく、耐熱性に優れ、表
層における緩衝性に優れた発泡シート積層発泡粒子成形
体が得られる。また、本発明の前記発泡シートはスタン
ピング成形法において形状が複雑なものにも適用できる
ものである。The cross-linked foamed polypropylene resin sheet of the present invention has excellent heat resistance in mold molding by vacuum, air pressure, etc., so that bubbles on the sheet surface may be broken by heat when the sheet is heated. And has excellent deep drawability and a wide temperature range in which heat molding is possible. And
It is also excellent in flexibility and cushioning. In particular, using the foamed sheet of the present invention, a foamed sheet laminated foamed particle molded article can be suitably produced by a so-called skin mold molding method. According to this manufacturing method, the adhesion between the foam sheet, the foam sheet, and the foamed particle molded body is good,
A foamed sheet-laminated foamed particle molded article having no breakage during molding or shrinkage of the molded article, excellent heat resistance, and excellent cushioning properties in the surface layer can be obtained. Further, the foamed sheet of the present invention can be applied to a sheet having a complicated shape in a stamping molding method.
【図1】一体成型用金型を用いた、本発明の発泡シート
積層発泡粒子成形体(表皮材付発泡成形体)を製造する
方法を説明する図である。FIG. 1 is a diagram illustrating a method for producing a foamed sheet laminated foamed particle molded article (foam molded article with a skin material) of the present invention using a mold for integral molding.
1 ポリプロピレン系樹脂架橋発泡シート(表皮材) 2a 金型A 2b 金型B 3a、3b 真空吸引管 4 キャビティ 5 真空吸引孔 6 スリット孔 7a、7b チャンバー 8a、8b スチーム導入管 9a、9b 冷却水導入管 10a、10b ドレン排出管 11 フィーダー P ポリプロピレン系樹脂発泡粒子 1 Crosslinked foamed sheet of polypropylene resin (skin material) 2a Mold A 2b Mold B 3a, 3b Vacuum suction tube 4 Cavity 5 Vacuum suction hole 6 Slit hole 7a, 7b Chamber 8a, 8b Steam introduction tube 9a, 9b Cooling water introduction Pipe 10a, 10b Drain discharge pipe 11 Feeder P Polypropylene resin foam particles
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29L 9:00 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI B29L 9:00
Claims (2)
発泡シートであって、該発泡シートの引張り測定におけ
る貯蔵弾性率が50℃で3×107〜3×108dyn/
cm2、100℃で1×107dyn/cm2以上、13
0℃で1×106dyn/cm2以上、140℃で4×1
05〜6×106dyn/cm2であり、かつ50℃、1
00℃、130℃、140℃でのtanδ(損失弾性率
/貯蔵弾性率)の値が0.05以上であることを特徴と
するポリプロピレン系樹脂架橋発泡シート。1. A foamed sheet comprising a polypropylene-based resin as a base resin, wherein the foamed sheet has a storage elastic modulus in a tensile measurement of 3 × 10 7 to 3 × 10 8 dyn / 50 ° C.
cm 2 , 1 × 10 7 dyn / cm 2 or more at 100 ° C., 13
1 × 10 6 dyn / cm 2 or more at 0 ° C., 4 × 1 at 140 ° C.
0 5 to 6 × 10 6 dyn / cm 2 and at 50 ° C., 1
A crosslinked polypropylene-based resin foam sheet having a tan δ (loss modulus / storage modulus) at 00 ° C, 130 ° C, and 140 ° C of 0.05 or more.
橋発泡シートを金型内に装着した後、金型内にポリプロ
ピレン系樹脂発泡粒子を充填し、スチームで加熱して発
泡粒子相互を融着せしめるとともに前記発泡粒子と発泡
シートとを融着一体化することを特徴とする発泡シート
積層発泡粒子成形体の製造方法。2. After mounting the crosslinked foamed polypropylene resin sheet according to claim 1 in a mold, the foamed polypropylene resin particles are filled in the mold and heated with steam to fuse the foamed particles to each other. And a method for producing a foamed sheet-laminated foamed particle molded article, wherein the foamed particle and the foamed sheet are fused and integrated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10153631A JPH11322993A (en) | 1998-05-18 | 1998-05-18 | Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10153631A JPH11322993A (en) | 1998-05-18 | 1998-05-18 | Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheet |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11322993A true JPH11322993A (en) | 1999-11-26 |
Family
ID=15566734
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10153631A Pending JPH11322993A (en) | 1998-05-18 | 1998-05-18 | Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheet |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11322993A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014051051A1 (en) * | 2012-09-28 | 2014-04-03 | 積水化学工業株式会社 | Foamable composition |
JP2015142282A (en) * | 2014-01-29 | 2015-08-03 | 日東電工株式会社 | Waterproof sound-transmitting member |
-
1998
- 1998-05-18 JP JP10153631A patent/JPH11322993A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014051051A1 (en) * | 2012-09-28 | 2014-04-03 | 積水化学工業株式会社 | Foamable composition |
JP5568197B1 (en) * | 2012-09-28 | 2014-08-06 | 積水化学工業株式会社 | Effervescent composition |
CN104379648A (en) * | 2012-09-28 | 2015-02-25 | 积水化学工业株式会社 | Foamable composition |
US9416242B2 (en) | 2012-09-28 | 2016-08-16 | Sekisui Chemical Co., Ltd. | Foamable composition |
JP2015142282A (en) * | 2014-01-29 | 2015-08-03 | 日東電工株式会社 | Waterproof sound-transmitting member |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3710014B2 (en) | Method for producing foamed article with skin material and vehicle interior material obtained thereby | |
CA2330922C (en) | Thermoformable polypropylene foam sheet | |
KR101166390B1 (en) | Soft Polyolefin Foams With High Heat Resistance | |
CN109476139B (en) | Laminate | |
US20060163765A1 (en) | Method for producing a thermoplastic resin article | |
JP3297253B2 (en) | Crosslinked polyolefin-based resin foam, laminate and molded article | |
JPH11322993A (en) | Polypropylene resin crosslinking foamed sheet and preparation of laminated foamed particle molding of foamed sheet | |
EP0916465B1 (en) | Composite polypropylene material having molded and foamed layer and method of producing same | |
JPH04278340A (en) | Laminated foamed sheet suitable for vacuum molding | |
US20060049551A1 (en) | Method for producing a thermoplastic resin foamed article | |
JP3525095B2 (en) | Polypropylene resin composite molding for automobile | |
US20060061003A1 (en) | Method for producing a thermoplastic resin foamed article | |
US6815051B2 (en) | Polyolefin resin molding composite | |
JP4172685B2 (en) | Method for producing foam molded article with skin material | |
JP3396400B2 (en) | Laminated sheet | |
WO2004078832A1 (en) | Crosslinked polyolefin resin foam sheet and moldings | |
JP3070960B2 (en) | Laminates and molded articles from them | |
WO2022220258A1 (en) | Injection foam molded body | |
JP4190314B2 (en) | Molding | |
JP3279456B2 (en) | Crosslinked polyolefin resin foam | |
JPH0623919A (en) | Forming method of interior trim material | |
JPH05222233A (en) | Polypropylene-based resin composition for foam, laminated sheet and laminate | |
JP2914842B2 (en) | Laminated composite | |
JPH08198993A (en) | Foamed sheet of cross-linked polypropylene resin | |
JP2007007869A (en) | Manufacturing method of thermoplastic resin molded product |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20040511 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20050223 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20070222 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20070226 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20070726 |