JPH0522730B2 - - Google Patents
Info
- Publication number
- JPH0522730B2 JPH0522730B2 JP21829284A JP21829284A JPH0522730B2 JP H0522730 B2 JPH0522730 B2 JP H0522730B2 JP 21829284 A JP21829284 A JP 21829284A JP 21829284 A JP21829284 A JP 21829284A JP H0522730 B2 JPH0522730 B2 JP H0522730B2
- Authority
- JP
- Japan
- Prior art keywords
- rubber
- styrene
- weight
- styrene content
- mixed
- 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
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 82
- 229920001971 elastomer Polymers 0.000 claims description 56
- 239000005060 rubber Substances 0.000 claims description 56
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 30
- 239000000203 mixture Substances 0.000 claims description 28
- 238000002156 mixing Methods 0.000 claims description 19
- 239000004816 latex Substances 0.000 claims description 18
- 229920000126 latex Polymers 0.000 claims description 18
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 229920001821 foam rubber Polymers 0.000 claims description 9
- 229920001577 copolymer Polymers 0.000 claims description 8
- 238000004073 vulcanization Methods 0.000 claims description 8
- 238000005187 foaming Methods 0.000 claims description 6
- 238000006116 polymerization reaction Methods 0.000 claims description 6
- 239000006260 foam Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000004604 Blowing Agent Substances 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 239000004014 plasticizer Substances 0.000 claims description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N vinyl-ethylene Natural products C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims 2
- 229920000642 polymer Polymers 0.000 description 13
- 239000000463 material Substances 0.000 description 8
- 230000000704 physical effect Effects 0.000 description 7
- 238000010521 absorption reaction Methods 0.000 description 6
- 230000035939 shock Effects 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000004927 clay Substances 0.000 description 4
- 239000004088 foaming agent Substances 0.000 description 4
- 238000004898 kneading Methods 0.000 description 4
- 239000004636 vulcanized rubber Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- -1 sericite Substances 0.000 description 3
- ICGLPKIVTVWCFT-UHFFFAOYSA-N 4-methylbenzenesulfonohydrazide Chemical compound CC1=CC=C(S(=O)(=O)NN)C=C1 ICGLPKIVTVWCFT-UHFFFAOYSA-N 0.000 description 2
- 239000004156 Azodicarbonamide Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000002174 Styrene-butadiene Substances 0.000 description 2
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 2
- 235000019399 azodicarbonamide Nutrition 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000013016 damping Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000004815 dispersion polymer Substances 0.000 description 2
- 229920002857 polybutadiene Polymers 0.000 description 2
- 239000011115 styrene butadiene Substances 0.000 description 2
- 239000000454 talc Substances 0.000 description 2
- 229910052623 talc Inorganic materials 0.000 description 2
- 239000013585 weight reducing agent Substances 0.000 description 2
- NBOCQTNZUPTTEI-UHFFFAOYSA-N 4-[4-(hydrazinesulfonyl)phenoxy]benzenesulfonohydrazide Chemical compound C1=CC(S(=O)(=O)NN)=CC=C1OC1=CC=C(S(=O)(=O)NN)C=C1 NBOCQTNZUPTTEI-UHFFFAOYSA-N 0.000 description 1
- 239000005995 Aluminium silicate Substances 0.000 description 1
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 1
- 229920000181 Ethylene propylene rubber Polymers 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 229920006311 Urethane elastomer Polymers 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 239000010692 aromatic oil Substances 0.000 description 1
- 230000000386 athletic effect Effects 0.000 description 1
- AYJRCSIUFZENHW-DEQYMQKBSA-L barium(2+);oxomethanediolate Chemical compound [Ba+2].[O-][14C]([O-])=O AYJRCSIUFZENHW-DEQYMQKBSA-L 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 229910052626 biotite Inorganic materials 0.000 description 1
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical class CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 1
- 230000037396 body weight Effects 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- YGANSGVIUGARFR-UHFFFAOYSA-N dipotassium dioxosilane oxo(oxoalumanyloxy)alumane oxygen(2-) Chemical compound [O--].[K+].[K+].O=[Si]=O.O=[Al]O[Al]=O YGANSGVIUGARFR-UHFFFAOYSA-N 0.000 description 1
- 239000012990 dithiocarbamate Substances 0.000 description 1
- 150000004659 dithiocarbamates Chemical class 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 150000002357 guanidines Chemical class 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- BDAGIHXWWSANSR-NJFSPNSNSA-N hydroxyformaldehyde Chemical compound O[14CH]=O BDAGIHXWWSANSR-NJFSPNSNSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 229910052627 muscovite Inorganic materials 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 210000000653 nervous system Anatomy 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- 229910052628 phlogopite Inorganic materials 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 229920001084 poly(chloroprene) Polymers 0.000 description 1
- 229920000636 poly(norbornene) polymer Polymers 0.000 description 1
- 229920001083 polybutene Polymers 0.000 description 1
- 230000001012 protector Effects 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000012763 reinforcing filler Substances 0.000 description 1
- 239000011359 shock absorbing material Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 229910000018 strontium carbonate Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 150000003557 thiazoles Chemical class 0.000 description 1
- 150000003585 thioureas Chemical class 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 239000010456 wollastonite Substances 0.000 description 1
- 229910052882 wollastonite Inorganic materials 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
発明の目的
産業上の利用分野
本発明は広い温度領域で反発弾性が0〜30%
で、且つ製造過程において作業性が著しく改良さ
れた低反発弾性ゴム及び低反発弾性ゴム発泡体に
関する。
最近、特に運動用具において衝撃吸収性能の優
れた材料が要求されている。これら材料は人体に
悪影響を与える運動時に発生する過大な衝撃力を
吸収または緩和する事を目的に用いられる。その
1例としてスポーツシユーズの中敷があげられる
が、これは走行時に体重の2〜7倍という衝撃が
足にかかるために起る踵、膝等の関節系や神経系
の損傷を使用者から守つている。
従来の技術
従来、衝撃吸収材料としては、ポリノルボルネ
ンを用いたもの(特開昭56−74801)、エチレン−
酢ビ共重合体を用いたもの(特開昭53−32441)、
ウレタンエラストマーを用いたもの(特開昭52−
54000)、ブタジエン樹脂を用いたもの及びブチル
ゴムを用いたもの等が提案されているが、いずれ
も反発弾性が適当でなく、また引張強度が十分で
なかつた。
上記事情に鑑み、本発明者等は先に−10℃〜50
℃という広い温度領域において30%以下の低反発
弾性を示すゴム組成物を見出し提案した。(特開
昭58−179246、特願昭58−189379、特願昭58−
189380)
また、本発明者等は「軽量化」という観点から
も鋭意検討をつづけ、分解型の発泡剤を用い発泡
することにより低反発弾性、即ち衝撃吸収の性能
を損なうことなく軽量化できる条件を見出しすで
に提案してきた。(特願昭57−205551、特願昭58
−71231)
ところで上記の本発明者等が提案してきた衝撃
吸収性能の極めて優れた低反発弾性の加硫ゴム組
成物及び加硫ゴム発泡体はすべて高スチレン含量
のスチレン−ブタジエン共重合体をその主ポリマ
ーとして使用しているが、この高スチレン含量ス
チレン−ブタジエン共重合体は80℃を越えた温度
条件では急激に粘度が下がるという性質をもつて
おり、この性質がこのポリマーを使用する上で特
に作業性において重大な障害となつている。
たとえばバンバリー等のゴムミキサーにおいて
は、投入するポリマー塊の表面と内部で温度差が
生じることにより表面と内部の粘度が大きく変る
ために、混合過程においてポリマー塊の表面です
べる形となり、ポリマー分散不良の原因となる。
この分散不良をひき起すと、物性が著しく損な
われて衝撃吸収性能が劣り、破壊強度が低下する
こととなる。このゴムミキサーによる混練におけ
るポリマーの分散不良はポリマーのみで予備練す
ることにより避けることができる。この理由とし
てポリマー分散不良の原因である温度による粘度
変化が特に激しい高スチレン側のスチレン−ブタ
ジエン共重合体の温度による粘度変化を他のポリ
マーで緩和できることが挙げられる。しかしこの
ゴムミキサーの混合過程におけるポリマーのみの
予備練は、口数的にも電力的にもコストアツプに
つながり、工業的見地から著しく不利な条件とな
る。
発明が解決しようとする問題点
本発明は、上記従来技術に比し製造が容易で且
つ製品の物性が優れた低反発弾性ゴム及び低反発
弾性ゴム発泡体を提供することを目的とする。
発明の構成
問題点を解決するための手段
以下本発明について詳細に説明する。第1の発
明は、
ア結合スチレン含量が重合過程で45〜75重量%
に調整された高スチレン含量スチレン−ブタ
ジエン共重合体の結合スチレン含量が相互に
少なくとも8%以上離れた2者もしくはそれ
以上を選択し、それらをラテツクスの状態で
混合したのち乾燥して得られる、トータルの
スチレン含量が48重量%から68重量%の間に
調整された高スチレン含量スチレン−ブタジ
エン共重合体の混合物、
全混合ゴム量に対して10重量%から40重量
%以下の汎用ゴム、
の及びからなる高スチレン含量スチレン−
ブタジエン共重合体と汎用ゴムとの混合ゴム、
イ 混合ゴム100重量部に対して10〜250重量部の
充填剤、
ウ 混合ゴム100重量部に対して0〜60重量部の
可塑剤、
からなる混合物に加硫剤、加硫促進剤を加え、加
熱硬化して得られる反発弾性が0〜30%である低
反発弾性ゴムである。
また第2の発明は、上記ア、イ及びウの3成分
からなる混合物に加硫剤、加硫促進剤、分解型発
泡剤を加えた後加熱発泡して得られる反発弾性が
0〜30%である低反発弾性ゴム発泡体である。
上記ア成分(混合ゴム)のうち、の高スチレ
ン含量スチレン−ブタジエン共重合体の混合物に
使用される高スチレン含量スチレン−ブタジエン
共重合体は上述したように重合過程で45〜75重量
%、好ましくは45−65重量%、さらに好ましくは
45〜60重量%に調整される必要があり、この高ス
チレン含量スチレン−ブタジエン共重合体の結合
スチレン含量が相互に少なくとも8%以上、好ま
しくは10%以上離れた2者もしくはそれ以上を選
択し、それらをラテツクスの状態で混合したのち
乾燥した状態で使用される。
このラテツクス状態で混合して得られる高スチ
レン含量スチレン−ブタジエン共重合体の混合物
の総スチレン含量は48〜68重量%、好ましくは50
〜63重量%、さらに好ましくは51〜57重量%にブ
レンド過程において調整される必要がある。
また衝撃吸収性能を向上させるという観点よ
り、ラテツクス状態で混合されるべき高スチレン
含量スチレン−ブタジエン共重合体は、その1種
類のムーニー粘度が5〜25、好ましくは7〜20で
ある事が望ましい。
また作業性という観点より、高スチレン含量ス
チレン−ブタジエン共重合体のトータルのムーニ
ー粘度を40〜80に調整する意味で、前述した低ム
ーニー粘度高スチレン含量スチレン−ブタジエン
共重合体以外の少なくとも1種類の高スチレン含
量スチレン−ブタジエン共重合体のムーニー粘度
は60以上、好ましくは75以上、さらに好ましくは
90以上であることが望ましい。
上記アの成分(混合ゴム)のうちの汎用ゴム
としては、天然ゴム、イソプレンゴム、ブタジエ
ンゴム、スチレン−ブタジエンゴム、クロロプレ
ンゴム、アクリロニトリル−ブタジエンゴム、エ
チレン−プロピレンゴム等の、ガラス転移点が−
20℃以下のゴムから選ばれたものが好ましく用い
られる。この汎用ゴムは、全混合ゴムに対して40
重量%以下、好ましくは10〜20重量%の量で混合
されるものである。
上記イ成分(充填剤)は、上述したように上記
混合ゴム100重量部に対して10〜250重量部の配合
量であることが必要であるが、特に20〜100重量
部である事が好ましい。
このイ成分としては、炭酸カルシウム、炭酸マ
グネシウム、炭酸バリウム、炭酸ストロンチウ
ム、硫酸バリウム、硫酸カルシウム、ドロマイ
ト、カオリンクレー、焼成クレー、ハードクレ
ー、セリサイト、滑石、タルク、ワラストナイ
ト、ベントナイト、白雲母、金雲母、黒雲母、水
酸化アルミニウム、亜鉛華、活性白土、ハロサイ
ト、酸化チタン、石膏、軽灰、重灰、ケイソウ
土、シラス、シラスバルーン等の非補強性もしく
は弱補強性の充填剤から選ばれたものが好ましく
用いられる。
上記ウ成分(可塑剤)は、上述したように上記
ゴム100重量部に対して0〜60重量部の配合量で
ある事が必要であるが、特に10〜35重量部である
ことが好ましい。
このウ成分としては、アロマ系オイル、ナフテ
ン系オイル、ポリブテン、ジオクチルフタレート
などの有機酸誘導体、燐酸トリクレジル等の燐酸
誘導体や硫酸誘導体などの無機酸誘導体等、通常
ゴムに使用できるものであればすべて使用でき
る。
本発明の低反発弾性ゴムは上記ア〜ウの3成分
からなる混合物に加硫剤及び加硫促進剤を加えて
これを加熱硬化し、また低反発弾性ゴム発泡体は
上記ア〜ウの3成分からなる混合物に加硫剤、加
硫促進剤及び分解型発泡剤を加えて加熱発泡する
ことにより得る事ができる。
この場合加硫剤としては、有機過酸化物、イオ
ウ、有機イオウ化合物などの公知のものが使用で
きる。加硫剤は混合ゴム100重量部に対して通常
0.5〜10重量部が使用される。また加硫促進剤と
してはアルデヒド−アミン類、アルデヒド−アン
モニア類、ジチオカルバメート類、グアニジン
類、チウラム類、スルフエンアミド類、チアゾー
ル類、チオウレア類などの公知のものが使用し得
る。加硫促進剤は混合ゴム100重量部に対して通
常0.5〜10重量部が使用される。
分解型発泡剤としてはジニトロソペンタメチレ
ンテトラミン(DPT)、アゾジカ−ボンアミド
(AZC)、p−トルエンスルホニルヒドラジド
(TSH)、4,4′−オキシビスベンゼンスルホニ
ルヒドラジド(OBSH)等の有機系発泡剤及び
炭酸水素ナトリウム等の無機系の発泡剤等、ゴム
の発泡に使用できるものなら、すべて使用可能で
ある。また発泡剤の量は混合ゴム100重量部に対
して0.5〜60重量部であり、好ましくは2〜30重
量部である。
更に本発明の低反発弾性ゴム又は発泡体には、
上記各成分に加えてカーボンブラツク、シリカ等
の補強剤や劣化防止のためのワツクス類、老化防
止剤などの任意成分を添加することができる。
本発明の低反発弾性ゴム又は該発泡体は、通常
の方法で混合し加熱硬化又は加熱発泡する事がで
きる。この場合硬化温度は110〜180℃とする事が
好ましい。硬化温度が110℃以下では硬化に長時
間を要し、180℃以上では物性が低下してしまう。
作 用
本発明の低反発弾性ゴム及び該発泡体は、ゴム
ミキサーの混練工程における予備練の段階をあら
かじめポリマー重合後のラテツクス状態で混合す
ることにより行う事ができる。またこのポリマー
重合後のラテツクス状態での混合は通常工業的な
ポリマー製造において行われるムーニー粘度調整
時のブレンド工程で行う事ができるので工数を増
す事なく遂行する事ができ、トータルの製造コス
トという観点から著しく有利となる。
このラテツクス状態で混合した高スチレン含量
スチレン−ブタジエン共重合体の混合物は、ゴム
ミキサーに混練の作業と同様の原因によるロール
作業におけるロール密着などの作業性の悪さを著
しく改善する事ができる。
またラテツクス状態での混合はゴムミキサー、
ロール等での物理的混合に比べ遥にミクロな状態
での相溶を可能とする。
この事はゴムミキサー、ロールでの混合物に比
べラテツクス状態で混合した混合物の物性が優れ
ている事を意味している。
さらにミクロな状態での相溶が可能になる事に
より、より離れたスチレン含量の高スチレン含量
スチレン−ブタジエン共重合体同志の良好な相溶
性を現出する事ができる。
また本発明におけるラテツクス状態での高スチ
レン含量スチレン−ブタジエン共重合体の混合は
混合するスチレン−ブタジエンの一種のムーニー
粘度を極端に下げる事ができる。混合するスチレ
ン−ブタジエンの一種のムーニー粘度を下げる事
により衝撃吸収性能をさらに上げる事ができる。
本発明の低反発弾性加硫ゴム組成物及び加硫ゴ
ム発泡体は前述したように優れた衝撃吸収性を有
するために中底、中敷、ミツドソール等の靴の部
材、ターンテーブル ゴムシート等の音響部品、
振動減衰材、衝撃吸収材、制振材、免振材、遮音
材、各種グリツプ、卓球ラケツトのフエース材、
野球のミツト、グラブ、プロテクター、ヘルメツ
ト等に好適に使用し得る。
次に本発明を実施例により詳細に説明する。
実施例 1〜3
第1表A、B、Cに示した、ラテツクスの状態
で混合して得られるポリマーを、第2表に示した
組成で配合した原料を容器内温度80℃のゴムミキ
サーで混合したのち、表面温度60℃のロールでシ
ート状にし、これを10×10×0.1cmの金型に充填
し、50Kg/cm2、145℃で25分加熱、加圧した後脱
型した。物性等を第3表に示す。
いずれも−10℃〜45℃の広い温度範囲で反発弾
性が30%以下で、作業性も良好である。
Purpose of the invention Industrial application field The present invention has a rebound resilience of 0 to 30% over a wide temperature range.
The present invention also relates to a low-rebound elastic rubber and a low-rebound elastic rubber foam that has significantly improved workability during the manufacturing process. Recently, there has been a demand for materials with excellent shock absorption performance, especially in athletic equipment. These materials are used for the purpose of absorbing or mitigating excessive impact forces generated during exercise that have a negative impact on the human body. One example of this is the insoles of Sports Shoes, which protect the user from damage to the joints and nervous system of the heel and knee caused by shocks of 2 to 7 times the body weight being applied to the feet while running. I'm protecting you from Conventional technology Conventionally, impact-absorbing materials using polynorbornene (Japanese Patent Application Laid-Open No. 1974-74801), ethylene-
Those using vinyl acetate copolymer (Japanese Patent Application Laid-open No. 53-32441),
Those using urethane elastomer (Japanese Unexamined Patent Publication No. 1983-
54000), one using butadiene resin, and one using butyl rubber, etc., but all of them had inadequate impact resilience and insufficient tensile strength. In view of the above circumstances, the inventors first decided to
We have discovered and proposed a rubber composition that exhibits low impact resilience of 30% or less in a wide temperature range of °C. (Japanese Unexamined Patent Publication No. 179246, Patent Application No. 189379, Patent Application No. 1987-
189380) In addition, the present inventors have continued to study intensively from the viewpoint of "weight reduction", and have found conditions under which weight reduction can be achieved by foaming using a decomposable foaming agent without impairing low rebound resilience, that is, impact absorption performance. have already been proposed. (Special application 1982-205551, Patent application 1983
-71231) By the way, all of the low-resilience vulcanized rubber compositions and vulcanized rubber foams with extremely excellent shock absorption performance that the inventors of the present invention have proposed include styrene-butadiene copolymers with a high styrene content. This styrene-butadiene copolymer with a high styrene content has the property of rapidly decreasing its viscosity at temperatures exceeding 80°C, and this property is important when using this polymer. This is a serious problem, especially in terms of workability. For example, in rubber mixers such as Banbury, the viscosity between the surface and the inside of the polymer mass changes greatly due to the difference in temperature between the surface and the inside of the polymer mass, which causes the polymer mass to slip on the surface during the mixing process, resulting in poor polymer dispersion. It causes. If this poor dispersion occurs, the physical properties will be significantly impaired, the impact absorption performance will be poor, and the breaking strength will be reduced. This poor dispersion of the polymer during kneading with a rubber mixer can be avoided by pre-mixing only with the polymer. The reason for this is that the viscosity change due to temperature of the styrene-butadiene copolymer on the high styrene side, which has a particularly severe viscosity change due to temperature, which is the cause of poor polymer dispersion, can be alleviated by using other polymers. However, premixing only the polymer during the mixing process using the rubber mixer leads to an increase in cost in terms of number of units and power, and is extremely disadvantageous from an industrial standpoint. Problems to be Solved by the Invention An object of the present invention is to provide a low-resilience rubber and a low-resilience rubber foam that are easier to manufacture and have superior physical properties as compared to the above-mentioned conventional techniques. Means for Solving the Constituent Problems of the Invention The present invention will be described in detail below. The first invention is that the content of a-bonded styrene is 45 to 75% by weight during the polymerization process.
Select two or more high styrene content styrene-butadiene copolymers whose combined styrene contents are separated by at least 8% from each other, mix them in a latex state, and then dry them. A mixture of high styrene-content styrene-butadiene copolymers with a total styrene content adjusted between 48% and 68% by weight, a general-purpose rubber with a content of 10% to 40% by weight based on the total amount of mixed rubber, High styrene content styrene consisting of and
A mixed rubber of a butadiene copolymer and a general-purpose rubber, consisting of (a) a filler of 10 to 250 parts by weight per 100 parts of the mixed rubber, and (c) a plasticizer of 0 to 60 parts by weight per 100 parts of the mixed rubber. A vulcanizing agent and a vulcanization accelerator are added to the mixture, and the resulting mixture is heated and cured to produce a low-resilience rubber having an impact resilience of 0 to 30%. In addition, the second invention is such that the rebound resilience obtained by adding a vulcanizing agent, a vulcanization accelerator, and a decomposable foaming agent to the mixture consisting of the three components A, B, and C above and then heating and foaming the mixture is 0 to 30%. It is a low-resilience rubber foam. Of the above component A (mixed rubber), the high styrene content styrene-butadiene copolymer used in the high styrene content styrene-butadiene copolymer mixture is preferably 45 to 75% by weight during the polymerization process, as described above. is 45-65% by weight, more preferably
It is necessary to adjust the content to 45 to 60% by weight, and the bound styrene content of the high styrene content styrene-butadiene copolymer should be selected from two or more materials whose bound styrene content is separated from each other by at least 8% or more, preferably by 10% or more. , they are mixed in the latex state and then used in the dry state. The total styrene content of the mixture of high styrene content styrene-butadiene copolymers obtained by mixing in the latex state is 48 to 68% by weight, preferably 50% by weight.
It needs to be adjusted to ~63% by weight, more preferably 51-57% by weight during the blending process. In addition, from the viewpoint of improving shock absorption performance, it is desirable that the high styrene content styrene-butadiene copolymer to be mixed in the latex state has a Mooney viscosity of 5 to 25, preferably 7 to 20. . In addition, from the viewpoint of workability, in order to adjust the total Mooney viscosity of the high styrene content styrene-butadiene copolymer to 40 to 80, at least one type of styrene-butadiene copolymer other than the low Mooney viscosity and high styrene content styrene-butadiene copolymer mentioned above was selected. The high styrene content styrene-butadiene copolymer has a Mooney viscosity of at least 60, preferably at least 75, more preferably at least 75.
Desirably 90 or higher. Examples of general-purpose rubbers in component (a) above (mixed rubber) include natural rubber, isoprene rubber, butadiene rubber, styrene-butadiene rubber, chloroprene rubber, acrylonitrile-butadiene rubber, and ethylene-propylene rubber, which have a glass transition point of -
A rubber selected from rubbers having a temperature of 20°C or less is preferably used. This general purpose rubber is rated at 40% for all mixed rubbers.
It is mixed in an amount of not more than 10% by weight, preferably 10 to 20% by weight. As mentioned above, the component A (filler) needs to be blended in an amount of 10 to 250 parts by weight based on 100 parts by weight of the mixed rubber, but it is particularly preferably 20 to 100 parts by weight. . These components include calcium carbonate, magnesium carbonate, barium carbonate, strontium carbonate, barium sulfate, calcium sulfate, dolomite, kaolin clay, calcined clay, hard clay, sericite, talc, talc, wollastonite, bentonite, and muscovite. , phlogopite, biotite, aluminum hydroxide, zinc white, activated clay, hallosite, titanium oxide, gypsum, light ash, heavy ash, diatomaceous earth, shirasu, shirasu balloon, and other non-reinforcing or weakly reinforcing fillers. Those selected from the following are preferably used. As mentioned above, the component C (plasticizer) needs to be blended in an amount of 0 to 60 parts by weight based on 100 parts by weight of the rubber, and particularly preferably 10 to 35 parts by weight. This component includes aromatic oils, naphthenic oils, polybutene, organic acid derivatives such as dioctyl phthalate, phosphoric acid derivatives such as tricresyl phosphate, and inorganic acid derivatives such as sulfuric acid derivatives, as long as they can be used normally in rubber. Can be used. The low-resilience rubber of the present invention is produced by adding a vulcanizing agent and a vulcanization accelerator to a mixture consisting of the three components A to C above, and curing the mixture by heating. It can be obtained by adding a vulcanizing agent, a vulcanization accelerator, and a decomposable foaming agent to a mixture of the components and heating and foaming the mixture. In this case, known vulcanizing agents such as organic peroxides, sulfur, and organic sulfur compounds can be used. Vulcanizing agent is usually added to 100 parts by weight of mixed rubber.
0.5-10 parts by weight are used. Further, as the vulcanization accelerator, known ones such as aldehyde-amines, aldehyde-ammonias, dithiocarbamates, guanidines, thiurams, sulfenamides, thiazoles, and thioureas can be used. The vulcanization accelerator is usually used in an amount of 0.5 to 10 parts by weight per 100 parts by weight of the mixed rubber. Decomposable blowing agents include organic blowing agents such as dinitrosopentamethylenetetramine (DPT), azodicarbonamide (AZC), p-toluenesulfonyl hydrazide (TSH), and 4,4'-oxybisbenzenesulfonyl hydrazide (OBSH). Any agent that can be used for foaming rubber, such as inorganic foaming agents such as sodium hydrogen carbonate and the like, can be used. The amount of the blowing agent is 0.5 to 60 parts by weight, preferably 2 to 30 parts by weight, based on 100 parts by weight of the mixed rubber. Furthermore, the low resilience rubber or foam of the present invention includes:
In addition to the above-mentioned components, optional components such as reinforcing agents such as carbon black and silica, waxes for preventing deterioration, and anti-aging agents can be added. The low-resilience rubber or foam of the present invention can be mixed and heat-cured or heat-foamed by a conventional method. In this case, the curing temperature is preferably 110 to 180°C. If the curing temperature is below 110°C, it will take a long time to cure, and if it is above 180°C, the physical properties will deteriorate. Function The low-repulsion elastic rubber of the present invention and the foam can be prepared by mixing in a latex state after polymerization in advance in the pre-kneading stage in the kneading process of a rubber mixer. In addition, this mixing in the latex state after polymerization can be carried out in the blending process during Mooney viscosity adjustment, which is normally carried out in industrial polymer production, so it can be accomplished without increasing the number of man-hours, and the total production cost can be reduced. This is a significant advantage from this point of view. This mixture of high styrene content styrene-butadiene copolymer mixed in a latex state can significantly improve poor workability such as roll adhesion in roll work due to the same reasons as kneading work in a rubber mixer. Also, for mixing in the latex state, use a rubber mixer.
This enables compatibility in a much more microscopic state than physical mixing using rolls or the like. This means that the physical properties of the mixture mixed in the latex state are superior to those mixed in a rubber mixer or roll. Furthermore, by making compatibility possible in a microscopic state, it is possible to exhibit good compatibility between high styrene-containing styrene-butadiene copolymers that are far apart from each other. Further, the mixing of the styrene-butadiene copolymer with a high styrene content in the latex state of the present invention can extremely lower the Mooney viscosity of the styrene-butadiene to be mixed. Shock absorption performance can be further improved by lowering the Mooney viscosity of the styrene-butadiene mixture. As mentioned above, the low-resilience vulcanized rubber composition and vulcanized rubber foam of the present invention have excellent shock absorbing properties, so they can be used for shoe components such as midsole, insole, midsole, turntable rubber sheet, etc. acoustic parts,
Vibration damping materials, shock absorbing materials, vibration damping materials, vibration isolation materials, sound insulation materials, various grips, face materials for table tennis rackets,
It can be suitably used for baseball gloves, gloves, protectors, helmets, etc. Next, the present invention will be explained in detail with reference to examples. Examples 1 to 3 Raw materials prepared by mixing the polymers shown in Table 1 A, B, and C in the latex state with the composition shown in Table 2 were mixed in a rubber mixer at an internal temperature of 80°C. After mixing, the mixture was formed into a sheet using rolls with a surface temperature of 60°C, filled into a mold of 10 x 10 x 0.1 cm, heated and pressurized at 50 kg/cm 2 at 145°C for 25 minutes, and then demolded. Physical properties etc. are shown in Table 3. All have impact resilience of 30% or less over a wide temperature range of -10°C to 45°C, and have good workability.
【表】【table】
【表】【table】
【表】【table】
【表】
数字はいずれも重量部
【table】
All numbers are parts by weight
【表】
比較例 1〜3
第1表D、E、Fに示した、ポリマーの状態で
混合して得られたポリマーを、第4表に示した組
成で配合した原料を、容器内温度80℃のゴムミキ
サーで混合した後、表面温度60℃のロールでシー
ト状にし、これを10×10×0.1cmの金型に充填し、
50Kg/cm2、145℃で25分加熱、加圧した後脱型し
た。[Table] Comparative Examples 1 to 3 Raw materials prepared by mixing the polymers shown in Table 1 D, E, and F in the polymer state with the composition shown in Table 4 were mixed at a container temperature of 80°C. After mixing with a rubber mixer at ℃, it is made into a sheet with a roll with a surface temperature of 60℃, and this is filled into a 10 x 10 x 0.1 cm mold.
After heating and pressurizing at 50 kg/cm 2 and 145° C. for 25 minutes, the mold was demolded.
【表】【table】
【表】
数字はいずれも重量部
物性等を第5表に示す。[Table] All numbers are parts by weight.
Physical properties etc. are shown in Table 5.
【表】
実施例 4
(発泡体の例)
第1表Aに示した、ラテツクスの状態で混合し
て得られるポリマーを、第2表に示した組成で配
合した原料を容器内温度80℃のゴムミキサーで混
合した後、プロ薬品及び発泡材を表面温度60℃の
ロールで混合後シート状にし、これを10×10×1
cmの金型に充填し90Kg/cm2、140℃で30分加熱し
た後脱型した。物性等を第3表に示す。
これも−10℃〜45℃の広い温度範囲で反発弾性
が30%以下で、作業性も良好である。
発明の効果
広い温度領域で反発弾性が0〜30%で且つ製造
過程において作業性が著しく改良された低反発弾
性ゴム及び低反発弾性ゴム発泡体が得られる。[Table] Example 4 (Example of foam) The raw materials prepared by mixing the polymers shown in Table 1 A in the latex state with the composition shown in Table 2 were mixed at a container temperature of 80°C. After mixing with a rubber mixer, the professional chemicals and foaming material are mixed with a roll with a surface temperature of 60°C and made into a sheet, which is then rolled into a 10×10×1 sheet.
The mixture was filled into a cm mold, heated at 90 kg/cm 2 at 140° C. for 30 minutes, and then demolded. Physical properties etc. are shown in Table 3. This also has a rebound resilience of 30% or less over a wide temperature range of -10°C to 45°C, and has good workability. Effects of the Invention A low-resilience rubber and a low-resilience rubber foam can be obtained that have an impact resilience of 0 to 30% over a wide temperature range and have significantly improved workability during the manufacturing process.
Claims (1)
重量%に調整された高スチレン含量スチレン
−ブタジエン共重合体の結合スチレン含量が
相互に少なくとも8%以上離れた2種もしく
はそれ以上を選択し、それらをラテツクスの
状態で混合したのち乾燥して得られる、トー
タルのスチレン含量が48重量%から68重量%
の間に調整された高スチレン含量スチレン−
ブタジエン共重合体の混合物、 全混合ゴム量に対して40重量%以下の汎用
ゴム、 の及び成分からなる高スチレン含量スチレ
ン−ブタジエン共重合体と汎用ゴムとの混合ゴ
ム、 イ 上記混合ゴム100重量部に対して10〜250重量
部の充填剤、 ウ 上記混合ゴム100重量部に対して0〜60重量
部の可塑剤、 からなる混合物に加硫剤、加硫促進剤を加え、加
熱硬化して得られる反発弾性が0〜30%である低
反発弾性ゴム。 2 ラテツクス状態で混合する高スチレン含量ス
チレン−ブタジエン共重合体のうち1種類のムー
ニー粘度が5〜25である特許請求の範囲第1項記
載の低反発弾性ゴム。 3 ラテツクス状態で混合する高スチレン含量ス
チレン−ブタジエン共重合体のうち特許請求の範
囲第2項記載の共重合体以外の少なくとも1種類
の共重合体のムーニー粘度が60以上である特許請
求の範囲第1項記載の低反発弾性ゴム。 4 ア 結合スチレン含量が重合過程で45〜75
重量%に調整された高スチレン含量スチレン
−ブタジエン共重合体の結合スチレン含量が
相互に少なくとも8%以上離れた2種もしく
はそれ以上を選択し、それらをラテツクスの
状態で混合したのち乾燥して得られる、トー
タルのスチレン含量が48重量%から68重量%
の間に調整された高スチレン含量スチレン−
ブタジエン共重合体の混合物、 全混合ゴム量に対して40重量%以下の汎用
ゴム、 の及び成分からなる高スチレン含量スチレ
ン−ブタジエン共重合体と汎用ゴムとの混合ゴ
ム、 イ 上記混合ゴム100重量部に対して10〜250重量
部の充填剤、 ウ 上記混合ゴム100重量部に対して0〜60重量
部の可塑剤、 からなる混合物に加硫剤、加硫促進剤、分解型発
泡剤を加えた後加熱発泡して得られる反発弾性が
0〜30%である低反発弾性ゴム発泡体。 5 ラテツクス状態で混合する高スチレン含量ス
チレン−ブタジエン共重合体のうち1種類のムー
ニー粘度が5〜25である特許請求の範囲第4項記
載の低反発弾性ゴム発泡体。 6 ラテツクス状態で混合する高スチレン含量ス
チレン−ブタジエン共重合体のうち特許請求の範
囲第5項記載の共重合体以外の少なくとも1種類
の共重合体のムーニー粘度が60以上である特許請
求の範囲第4項記載の低反発弾性ゴム発泡体。[Claims] 1. A. The bound styrene content is 45 to 75 during the polymerization process.
High styrene content styrene-butadiene copolymers adjusted to % by weight are obtained by selecting two or more types of styrene-butadiene copolymers whose combined styrene content is at least 8% apart from each other, mixing them in a latex state, and then drying them. Total styrene content ranges from 48% to 68% by weight
High styrene content styrene prepared between -
A mixture of a butadiene copolymer, a general-purpose rubber of not more than 40% by weight based on the total amount of mixed rubber, and a mixed rubber of a styrene-butadiene copolymer with a high styrene content and a general-purpose rubber, (a) 100% by weight of the above mixed rubber A vulcanizing agent and a vulcanization accelerator are added to a mixture consisting of 10 to 250 parts by weight of a filler per 100 parts of the mixed rubber, c) a plasticizer of 0 to 60 parts by weight per 100 parts by weight of the above mixed rubber, and the mixture is heated and cured. Low-rebound elastic rubber with an impact elasticity of 0 to 30%. 2. The low resilience rubber according to claim 1, wherein one of the high styrene content styrene-butadiene copolymers to be mixed in the latex state has a Mooney viscosity of 5 to 25. 3 Claims in which at least one copolymer other than the copolymer described in claim 2 among the high styrene content styrene-butadiene copolymers to be mixed in a latex state has a Mooney viscosity of 60 or more. The low-repulsion elastic rubber according to item 1. 4 A. The bound styrene content increases from 45 to 75 during the polymerization process.
High styrene content styrene-butadiene copolymers adjusted to % by weight are obtained by selecting two or more types of styrene-butadiene copolymers whose combined styrene content is at least 8% apart from each other, mixing them in a latex state, and then drying them. Total styrene content ranges from 48% to 68% by weight
High styrene content styrene prepared between -
A mixture of a butadiene copolymer, a general-purpose rubber of not more than 40% by weight based on the total amount of mixed rubber, and a mixed rubber of a styrene-butadiene copolymer with a high styrene content and a general-purpose rubber, (a) 100% by weight of the above mixed rubber a vulcanizing agent, a vulcanization accelerator, and a decomposable blowing agent to a mixture consisting of 10 to 250 parts by weight of a filler per 100 parts by weight of the above mixed rubber; A low-resilience rubber foam with an impact resilience of 0 to 30% obtained by heating and foaming after adding the foam. 5. The low resilience rubber foam according to claim 4, wherein one of the high styrene content styrene-butadiene copolymers to be mixed in the latex state has a Mooney viscosity of 5 to 25. 6 Claims in which at least one copolymer other than the copolymer described in Claim 5 among the high styrene content styrene-butadiene copolymers to be mixed in a latex state has a Mooney viscosity of 60 or more. 4. The low-resilience rubber foam according to item 4.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21829284A JPS6197334A (en) | 1984-10-19 | 1984-10-19 | Low-resiliency rubber and its foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21829284A JPS6197334A (en) | 1984-10-19 | 1984-10-19 | Low-resiliency rubber and its foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6197334A JPS6197334A (en) | 1986-05-15 |
| JPH0522730B2 true JPH0522730B2 (en) | 1993-03-30 |
Family
ID=16717546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21829284A Granted JPS6197334A (en) | 1984-10-19 | 1984-10-19 | Low-resiliency rubber and its foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6197334A (en) |
-
1984
- 1984-10-19 JP JP21829284A patent/JPS6197334A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6197334A (en) | 1986-05-15 |
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