JPS6225084B2 - - Google Patents
Info
- Publication number
- JPS6225084B2 JPS6225084B2 JP3468780A JP3468780A JPS6225084B2 JP S6225084 B2 JPS6225084 B2 JP S6225084B2 JP 3468780 A JP3468780 A JP 3468780A JP 3468780 A JP3468780 A JP 3468780A JP S6225084 B2 JPS6225084 B2 JP S6225084B2
- Authority
- JP
- Japan
- Prior art keywords
- acetylene
- polymer
- pressure
- organic solvent
- molded product
- 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
Links
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 52
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 52
- 229920000642 polymer Polymers 0.000 claims description 45
- 239000003960 organic solvent Substances 0.000 claims description 20
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 9
- 238000003490 calendering Methods 0.000 claims description 7
- 238000000465 moulding Methods 0.000 claims description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 37
- 238000000034 method Methods 0.000 description 17
- 239000010408 film Substances 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 12
- 238000006116 polymerization reaction Methods 0.000 description 11
- 239000000499 gel Substances 0.000 description 7
- 239000002904 solvent Substances 0.000 description 7
- 238000001291 vacuum drying Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- RDOXTESZEPMUJZ-UHFFFAOYSA-N anisole Chemical compound COC1=CC=CC=C1 RDOXTESZEPMUJZ-UHFFFAOYSA-N 0.000 description 4
- 230000000379 polymerizing effect Effects 0.000 description 4
- 239000004065 semiconductor Substances 0.000 description 4
- 238000009864 tensile test Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 150000003623 transition metal compounds Chemical class 0.000 description 3
- LKUDPHPHKOZXCD-UHFFFAOYSA-N 1,3,5-trimethoxybenzene Chemical compound COC1=CC(OC)=CC(OC)=C1 LKUDPHPHKOZXCD-UHFFFAOYSA-N 0.000 description 2
- OHBQPCCCRFSCAX-UHFFFAOYSA-N 1,4-Dimethoxybenzene Chemical compound COC1=CC=C(OC)C=C1 OHBQPCCCRFSCAX-UHFFFAOYSA-N 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 description 2
- UZKWTJUDCOPSNM-UHFFFAOYSA-N methoxybenzene Substances CCCCOC=C UZKWTJUDCOPSNM-UHFFFAOYSA-N 0.000 description 2
- -1 n-dimethoxybenzene Chemical compound 0.000 description 2
- 150000002902 organometallic compounds Chemical class 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 description 1
- VWGNFIQXBYRDCH-UHFFFAOYSA-N 1,4-diethoxybenzene Chemical compound CCOC1=CC=C(OCC)C=C1 VWGNFIQXBYRDCH-UHFFFAOYSA-N 0.000 description 1
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical group [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000007983 Tris buffer Substances 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 150000001334 alicyclic compounds Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 150000008378 aryl ethers Chemical class 0.000 description 1
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 150000002391 heterocyclic compounds Chemical class 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000013081 microcrystal Substances 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- DLRJIFUOBPOJNS-UHFFFAOYSA-N phenetole Chemical compound CCOC1=CC=CC=C1 DLRJIFUOBPOJNS-UHFFFAOYSA-N 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明はアセチレン高重合体の成形品の製造方
法に係り、更に詳しくはシス含量が50%以上のア
セチレン高重合体5〜95重量%と不活性有機溶媒
95〜5重量%からなるゲル状物を、温度50℃以
下、圧力10〜1000Kg/cm2で加圧成形し、次いで得
られた加圧成形品を50℃以下の温度でカレンダー
加工してシート、フイルムなどの各種成形品を製
造する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a molded article of an acetylene high polymer, and more specifically, the present invention relates to a method for producing a molded article of an acetylene high polymer, and more specifically, a method for manufacturing a molded article of an acetylene high polymer, which comprises a cis content of 5 to 95% by weight of an acetylene high polymer having a cis content of 50% or more and an inert organic solvent.
A gel-like material consisting of 95 to 5% by weight is pressure-molded at a temperature of 50°C or less and a pressure of 10 to 1000 kg/cm 2 , and then the resulting pressure-molded product is calendered at a temperature of 50°C or less to form a sheet. , relates to a method for manufacturing various molded products such as films.
遷移金属化合物と有機金属化合物から成るいわ
ゆるチーグラーナツタ触媒を用いてアセチレンを
重合して得られるアセチレン高重合体は有機半導
体として知られているが、加熱しても溶融せず、
また酸素存在下で加熱すると容易に酸化劣化を受
ける。また、このアセチレン高重合体を溶解する
溶媒も見い出されておらず、アセチレン高重合体
の実用的成形物を製造する場合には従来次の二つ
の方法のみに限られていた。 The acetylene polymer obtained by polymerizing acetylene using a so-called Ziegler-Natsuta catalyst consisting of a transition metal compound and an organometallic compound is known as an organic semiconductor, but it does not melt even when heated.
Moreover, when heated in the presence of oxygen, it easily undergoes oxidative deterioration. Furthermore, no solvent has been found that can dissolve this acetylene high polymer, and the production of practical molded products of acetylene high polymers has heretofore been limited to the following two methods.
(イ) 粉末状アセチレン高重合体を加圧成形する方
法、
(ロ) 触媒溶液と気体アセチレンの自由表面近傍の
界面および固体表面にこの触媒溶液を塗布した
表面で重合を行なつて膜状および繊維状アセチ
レン重合体を製造する方法。(a) A method of pressure molding a powdery acetylene high polymer; (b) A method of polymerizing a catalyst solution at the interface near the free surface of gaseous acetylene and a solid surface coated with the catalyst solution to form a film-like and A method for producing a fibrous acetylene polymer.
しかしながら前者(イ)の方法では機械的強度の低
い成形品しか得られず、又後者の方法(ロ)ではフイ
ルムおよび繊維の原料が限定され、実質的には厚
みの小さい膜および繊維状の成形品しか得られな
いばかりでなく、均一な厚みの成形品を得ること
は困難であつた。 However, with the former method (a), only molded products with low mechanical strength can be obtained, and with the latter method (b), raw materials for films and fibers are limited, and in reality, thin films and fibrous molded products can be obtained. Not only was it difficult to obtain a molded product with a uniform thickness, but it was also difficult to obtain a molded product with a uniform thickness.
本発明者等はかかる点に鑑みて、充分な機械的
強度を持ち、膜厚が厚く、かつ均一な厚みを持つ
アセチレン高重合体の成形品を成形する方法を見
い出し既に提案した。 In view of this, the present inventors have discovered and already proposed a method for molding an acetylene polymer molded product having sufficient mechanical strength, a thick film thickness, and a uniform thickness.
しかしながら、上記提案の方法ではかさ密度の
非常に低いゲル状物から一気に加圧又はロール成
形する為、膜厚の均一な成形品を得る為には高度
な成形技術が必要であり、往々、ゲル状物が破壊
されて小片となり均一な膜厚の成形品が得られな
いこともあつた。また、この様にして得られる成
形品の機械的強度は必ずしも充分満足すべきもの
ではなかつた。 However, in the method proposed above, a gel-like material with a very low bulk density is pressurized or roll-formed all at once, so advanced molding technology is required to obtain a molded product with a uniform film thickness. In some cases, the molded product was broken and became small pieces, making it impossible to obtain a molded product with a uniform film thickness. Furthermore, the mechanical strength of the molded articles obtained in this manner was not necessarily sufficiently satisfactory.
本発明者等は上記の点に鑑みて、容易に膜厚の
均一な成形品の成形方法について種々検討した結
果本発明に到達した。本発明の方法によつて均一
な膜厚の成形品を容易に得ることができるばかり
でなく、得られた成形品の機械的強度も大きい。 In view of the above points, the present inventors have arrived at the present invention as a result of various studies on methods for easily forming molded products with uniform film thickness. By the method of the present invention, it is not only possible to easily obtain a molded article with a uniform film thickness, but also the mechanical strength of the obtained molded article is high.
有機溶媒の存在下、触媒を用いてアセチレン高
重合体と有機溶媒のゲル状物を製造する方法とし
ては、例えば次の方法が挙げられる。 Examples of the method for producing a gel-like material of an acetylene polymer and an organic solvent using a catalyst in the presence of an organic solvent include the following method.
(1) ヘキサンを溶媒としてμ−(η1:η5−
cyclopcntadienyl)−tris(η−cyclo−
pentadienyl)dititan ium(Ti−Ti)〔(C5H4)5
(C5H5)3Ti2〕なる特殊な遷移金属化合物の触媒
を用いてアセチレンを重合してゲル状アセチレ
ン高重合体を製造する方法〔S.L.Hsu et.al.J.
chem.pys.69(1)、106−111(1978)〕。(1) μ−(η 1 :η 5 −
cyclopcntadienyl)−tris(η−cyclo−
pentadienyl) dititanium (Ti−Ti) [(C 5 H 4 ) 5
A method for producing a gel-like acetylene polymer by polymerizing acetylene using a special transition metal compound catalyst (C 5 H 5 ) 3 Ti 2 [SLHsu et.al.J.
chem.pys.69(1), 106-111 (1978)].
(2) 本発明者等の見出した(A)遷移金属化合物と(B)
有機金属化合物とからなる触媒系を用いて、重
合溶媒として芳香族化合物を用い、(A)成分の濃
度が0.1〜0.0001モル/でアセチレンを重合
してゲル状組成物を製造する方法。(2) (A) transition metal compound and (B) discovered by the present inventors
A method for producing a gel composition by polymerizing acetylene using a catalyst system consisting of an organometallic compound, an aromatic compound as a polymerization solvent, and a concentration of component (A) of 0.1 to 0.0001 mol/.
本発明で用いられるアセチレン高重合体と有機
溶媒のゲル状物とは、アセチレン高重合体の繊維
状微結晶(フイブリル)が絡みあつて、有機溶媒
に膨潤している状態のものであり、その製造方法
は上記の方法に限定されるものではない。 The gel of acetylene polymer and organic solvent used in the present invention is a state in which fibrous microcrystals (fibrils) of acetylene polymer are entangled and swollen in the organic solvent. The manufacturing method is not limited to the above method.
本発明で用いられる有機溶媒としては脂肪族又
は芳香族の炭化水素、ハロゲン化炭化水素、エー
テル、カルボン酸エステル、酸無水物、ケトン、
脂環式化合物、含酸素複素環式化合物などを用い
ることができる。 Examples of organic solvents used in the present invention include aliphatic or aromatic hydrocarbons, halogenated hydrocarbons, ethers, carboxylic acid esters, acid anhydrides, ketones,
Alicyclic compounds, oxygen-containing heterocyclic compounds, and the like can be used.
これらの有機溶媒を重合溶媒として用いてもよ
いし、重合終了後、重合溶媒をこれらの有機溶媒
で置換してもよい。 These organic solvents may be used as the polymerization solvent, or the polymerization solvent may be replaced with these organic solvents after the polymerization is completed.
これらのうちでも芳香族炭化水素及び芳香族エ
ーテルが好ましく、それらの代表例としては、ベ
ンゼン、トルエン、キシレン、エチルベンゼン、
メチルフエニルエーテル(アニソール)、エチル
フエニルエーテル、ジフエニルエーテル、n−ジ
メトキシベンゼン、p−ジメトキシベンゼン、n
−ジエトキシベンゼン、p−ジエトキシベンゼ
ン、1・3・5−トリメトキシベンゼンなどを挙
げることができる。 Among these, aromatic hydrocarbons and aromatic ethers are preferred, and representative examples thereof include benzene, toluene, xylene, ethylbenzene,
Methyl phenyl ether (anisole), ethyl phenyl ether, diphenyl ether, n-dimethoxybenzene, p-dimethoxybenzene, n
-diethoxybenzene, p-diethoxybenzene, 1,3,5-trimethoxybenzene, and the like.
有機溶媒は上記の1種又は2種以上の混合溶媒
でもよいし、上記の有機溶媒の一部を脂肪族又は
芳香族のアルコール、カルボン酸で置換してもよ
い。 The organic solvent may be one or a mixed solvent of two or more of the above, or a part of the above organic solvent may be replaced with an aliphatic or aromatic alcohol or carboxylic acid.
アセチレンの重合終了後、重合溶媒の一部を通
常の方法により除去したり、触媒を除去する為に
有機溶媒でアセチレン重合体を洗滌することは一
向に構わないが、加圧するまでアセチレン高重合
体を有機溶媒の存在下でゲル状物の状態に保持し
ておくことが本発明の必須条件であり、加圧する
前にアセチレン重合体を乾燥しては成形が困難と
なる。 After the polymerization of acetylene is completed, it is perfectly acceptable to remove a part of the polymerization solvent by a conventional method or to wash the acetylene polymer with an organic solvent to remove the catalyst, but it is not necessary to wash the acetylene polymer until pressurization. It is an essential condition of the present invention that the acetylene polymer be maintained in a gel state in the presence of an organic solvent, and if the acetylene polymer is dried before being pressurized, it will be difficult to mold it.
本発明で用いられるゲル状物中のアセチレン高
重合体は5〜95重量%の範囲である。ゲル状物中
のアセチレン高重合体が5重量%未満では膜厚の
均一な成形品を製造することが困難であり、又、
95重量%を越えると可塑性が不足して加圧成形が
困難となる。 The amount of acetylene high polymer in the gel material used in the present invention is in the range of 5 to 95% by weight. If the acetylene high polymer content in the gel-like material is less than 5% by weight, it is difficult to produce a molded product with a uniform film thickness;
If it exceeds 95% by weight, the plasticity will be insufficient and pressure molding will become difficult.
加圧成形時の圧力範囲は10〜1000Kg/cm2であ
り、圧力が10Kg/cm2未満では次のロール加工時に
ひび割れや切断が起り、一方、圧力が1000Kg/cm2
を越えると次のロール加工時に延伸することが不
可能となり、機械的強度の充分大きい成形品を得
ることが不可能である。加圧成形時に有機溶媒の
大部分はアセチレン重合体から除去されるが、少
量の有機溶媒は残る。この段階で残存有機溶媒を
除去することはその次のロール加工が困難となる
ので好ましくない。 The pressure range during pressure forming is 10 to 1000Kg/ cm2 , and if the pressure is less than 10Kg/ cm2 , cracking or cutting will occur during the next rolling process, while on the other hand, if the pressure is 1000Kg/ cm2
If it exceeds this, it becomes impossible to stretch during the next roll processing, making it impossible to obtain a molded product with sufficiently high mechanical strength. During pressing, most of the organic solvent is removed from the acetylene polymer, but a small amount of organic solvent remains. It is not preferable to remove the residual organic solvent at this stage because it will make the subsequent roll processing difficult.
カレンダー加工は当該業者の間で広く行なわれ
ているロールを用いての成形法であり、ロールの
間げきや圧力は得られる膜状アセチレン高重合体
の要求される厚や、ゲル状物中のアセチレン高重
合体の濃度によつてかわるので、一概に限定する
わけにはいかない。 Calender processing is a forming method using rolls that is widely used in the industry, and the gap and pressure of the rolls are determined by the required thickness of the resulting film-like acetylene polymer and the content of the gel-like material. Since it depends on the concentration of the acetylene high polymer, it cannot be absolutely limited.
アセチレン高重合体と有機溶媒のゲル状物を2
本以上のロールの間にはさんでおしのばし、均一
な膜厚のアセチレン高重合体のシートやフイルム
を連続的に製造することが出来るので従来の成形
品の製造法に比較して格段に優れている。 2 gels of acetylene high polymer and organic solvent
It is possible to continuously produce acetylene polymer sheets or films with a uniform thickness by rolling them between rolls larger than a book, making it much more effective than conventional molded product production methods. Are better.
本発明で用いることのできるアセチレン高重合
体はシス含量が50%以上のものであり、シス含量
が50%未満のものではアセチレン高重合体の可撓
性が低下し、均一な成形品を得ることができな
い。 The acetylene high polymer that can be used in the present invention has a cis content of 50% or more; if the cis content is less than 50%, the flexibility of the acetylene high polymer decreases, resulting in a uniform molded product. I can't.
アセチレン高重合体のシス含量は重合温度や触
媒調製条件によつて制御することができる。 The cis content of the acetylene polymer can be controlled by the polymerization temperature and catalyst preparation conditions.
ロールの圧力は1Kg/cm2以上、好ましくは5
Kg/cm2であり、圧力が1Kg/cm2未満では機械的強
度の充分大きい成形品を得ることが出来ない。 The pressure of the roll is 1Kg/cm2 or more, preferably 5
Kg/cm 2 , and if the pressure is less than 1 Kg/cm 2 , a molded product with sufficiently high mechanical strength cannot be obtained.
カレンダー成形時に残存有機溶媒の大部分はア
セチレン重合体から除去されるが、少量の有機溶
媒が残る場合もある。残存有機溶媒はそのままで
も実用上一向差し支えない場合もあろうが、真空
乾燥等の方法で除去してもよい。 Although most of the residual organic solvent is removed from the acetylene polymer during calendering, a small amount of organic solvent may remain. Although there may be no practical problem with the remaining organic solvent as it is, it may be removed by a method such as vacuum drying.
以上の方法により、機械的強度が強く所定の膜
厚の均一な成形品を得ることができる。このよう
にして得られるアセチレン高重合体の成形品の電
気抵抗は非常に低く、いわゆる半導体に特有な諸
電気的性質を示す。 By the above method, it is possible to obtain a molded product with strong mechanical strength and a uniform film thickness. The acetylene polymer molded product thus obtained has a very low electrical resistance and exhibits various electrical properties characteristic of so-called semiconductors.
室温での比抵抗はシス構造の多いものでは108
Ω・cm程度であるが、トランス構造が多くなるに
従つて低下し、トランス構造のみのものでは104
〜103Ω・cm程度となり、また光伝導性も示す。
このアセチレン高重合体は前記の諸電気的性質を
利用することにより、たとえば電気抵抗素子、感
熱素子、感光素子などの電気機器部品を製造する
ための有機半導体材料として使用できる。 The specific resistance at room temperature is 10 8 for those with many cis structures.
It is about Ω・cm, but it decreases as the number of transformer structures increases, and for a transformer structure only, it is about 10 4
~10 3 Ω·cm, and also exhibits photoconductivity.
By utilizing the various electrical properties described above, this acetylene polymer can be used as an organic semiconductor material for manufacturing electrical equipment parts such as electrical resistance elements, heat-sensitive elements, and photo-sensitive elements.
以下に実施例を挙げて本発明をさらに詳細に説
明する。 The present invention will be explained in more detail with reference to Examples below.
実施例 1
窒素ガスで完全に置換した1のガラス製反応
器に重合溶媒として常法に従つて精製したトルエ
ンを200ml、触媒としてテトラブトキシチタニウ
ムを2.94ミリモル及びトリエチルアルミニウム
7.34ミリモルをこの順序に室温で仕込んで触媒を
調製した。触媒は均一溶媒であつた。反応器を液
体窒素で冷却して系中の窒素ガスを真空ポンプで
排気した。−78℃に反応器を冷却して1気圧の圧
力の精製アセチレンガスを吹き込んだ。Example 1 In a glass reactor 1 completely purged with nitrogen gas, 200 ml of toluene purified according to a conventional method was added as a polymerization solvent, and 2.94 mmol of tetrabutoxytitanium and triethylaluminum were added as catalysts.
The catalyst was prepared by charging 7.34 mmol in this order at room temperature. The catalyst was a homogeneous solvent. The reactor was cooled with liquid nitrogen, and the nitrogen gas in the system was exhausted using a vacuum pump. The reactor was cooled to -78°C and purified acetylene gas was blown at a pressure of 1 atmosphere.
アセチレンガス圧を1気圧に保つたままで4時
間重合反応をそのまま継続した。重合終了後未反
応のアセチレンガスを除去し、系の温度を−78℃
に保つたまま200mlの精製トルエンで4回繰り返
し洗滌した。洗滌後も溶液はやや褐色をおび触媒
は完全に除去されなかつた。トルエン中で膨潤し
たゲル状アセチレン重合体は、フイブリルが絡み
合つた均一な膜状であり、粉末状や塊状のポリマ
ーは生成していなかつた。 The polymerization reaction was continued for 4 hours while maintaining the acetylene gas pressure at 1 atm. After polymerization, unreacted acetylene gas was removed and the system temperature was lowered to -78℃.
It was washed four times with 200 ml of purified toluene while maintaining the temperature. Even after washing, the solution turned slightly brown and the catalyst was not completely removed. The gel-like acetylene polymer swollen in toluene was in the form of a uniform film with entangled fibrils, and no powder or lump-like polymer was produced.
上記の膜状ゲル状物(アセチレン高重合体含量
37重量%)をクロロメツキしたフエロ板にはさん
で徐々に圧力をあげて100Kg/cm2の圧力でトルエ
ンを除きながらプレス成形して膜厚が1.2mmの可
撓性のある強靭な膜状成形品を得た。この成形品
中の残存トエン量は13重量%であつた。 The above film-like gel material (acetylene high polymer content
37% by weight) was sandwiched between chloroplated ferro plates and press-molded while gradually increasing the pressure to 100 kg/cm 2 while removing toluene to form a flexible and strong film with a thickness of 1.2 mm. I got the item. The amount of toene remaining in this molded article was 13% by weight.
この加圧成形品を室温で2本ロール(ロール温
度は室温、ロール間隙0.1mm、ロール径3イン
チ、ロール面はクロムメツキ)を通してカレンダ
ー加工して膜厚が0.12mmの均一なアセチレン高重
合体のシートを得た。この様にして得られたフイ
ルムには約1重量%のトルエンがまだ残存してお
り、室温で真空乾燥して残存トルエンを除去し
た。 This pressure-molded product was calendered at room temperature through two rolls (roll temperature is room temperature, roll gap 0.1 mm, roll diameter 3 inches, roll surface is chrome plating) to form a uniform film of acetylene high polymer with a thickness of 0.12 mm. Got a sheet. Approximately 1% by weight of toluene still remained in the film thus obtained, and the remaining toluene was removed by vacuum drying at room temperature.
得られたアセチレン高重合体のシートはシス含
量が94%で電気伝導度(直流四端子法で測定)が
2.1×10-7Ω-1・cm-1のp型半導体であつた。ま
た、このアセチレン高重合体の引張強度(試片
JIS 2号1/2、引張速度5mm/分)は1520Kg/
cm2であつた。 The resulting acetylene polymer sheet has a cis content of 94% and an electrical conductivity (measured by the DC four-probe method).
It was a p-type semiconductor of 2.1×10 -7 Ω -1 ·cm -1 . In addition, the tensile strength of this acetylene high polymer (sample
JIS No. 2 1/2, tensile speed 5mm/min) is 1520Kg/
It was warm in cm2 .
比較例 1
実施例1でプレス成形して得られた加圧成形品
を真空乾燥して得た膜状成形品を実施例1と同じ
条件で引張り試験を行なつたところその引張強度
は415Kg/cm2であつた。Comparative Example 1 A film-like molded product obtained by vacuum drying the pressure-formed product obtained by press molding in Example 1 was subjected to a tensile test under the same conditions as in Example 1, and the tensile strength was 415 kg/ It was warm in cm2 .
比較例 2
実施例1で重合して得られたゲル状アセチレン
高重合体を室温で真空乾燥して残存トルエンの一
部を除去してアセチレン高重合体中のトルエン含
量を21重量%にまでして実施例1と同様の方法で
ロールによりカレンダー加工して膜厚が0.21mmの
均一なアセチレン高重合体のシートを得た。この
成形品を真空乾燥して実施例1と同じ条件で引張
り試験を行つたところ、その引張強度は747Kg/
cm2であつた。Comparative Example 2 The gel-like acetylene high polymer obtained by polymerization in Example 1 was vacuum-dried at room temperature to remove a portion of the residual toluene, and the toluene content in the acetylene high polymer was reduced to 21% by weight. Then, calendering was performed using a roll in the same manner as in Example 1 to obtain a uniform acetylene polymer sheet having a thickness of 0.21 mm. When this molded product was dried in vacuum and subjected to a tensile test under the same conditions as in Example 1, its tensile strength was 747 kg/
It was warm in cm2 .
実施例 2
実施例1で得られた膜状ゲル状物を室温で真空
乾燥してトルエン溶媒の一部を除去してアセチレ
ン高重合体の含量を62重量%にしたゲル状物を用
いて実施例1と同様な方法に加圧及びカレンダー
加工して膜厚が0.14mmのアセチレン高重合体のシ
ートを得た。真空乾燥後、引張り試験を行い引張
強度は1770Kg/cm2であつた。Example 2 The film-like gel obtained in Example 1 was vacuum-dried at room temperature to remove part of the toluene solvent and the acetylene high polymer content was 62% by weight. A sheet of acetylene polymer having a thickness of 0.14 mm was obtained by pressing and calendering in the same manner as in Example 1. After vacuum drying, a tensile test was performed and the tensile strength was 1770 Kg/cm 2 .
実施例 3
実施例1で加圧成形した得られたトルエンを13
重量%含有する成形品を室温で真空乾燥してトル
エンの一部を除去して残存トルエン含量5重量%
とした以外は実施例1と全く同様にカレンダー加
工して膜厚が0.11mmの均一なアセチレン高重合体
のシートを得た。このシートを室温で真空乾燥
後、引張り試験を行い、その引張り強度は1650
Kg/cm2であつた。Example 3 The toluene obtained by pressure molding in Example 1 was
Part of the toluene was removed by vacuum drying the molded product containing 5% by weight at room temperature, resulting in a residual toluene content of 5% by weight.
A uniform acetylene polymer sheet having a thickness of 0.11 mm was obtained by calendering in exactly the same manner as in Example 1, except for the following. After drying this sheet under vacuum at room temperature, a tensile test was conducted and the tensile strength was 1650.
It was Kg/ cm2 .
Claims (1)
〜95重量%と不活性有機溶媒95〜5重量%からな
るゲル状物を、温度50℃以下、圧力10〜1000Kg/
cm2の範囲で加圧成形し、次いで得られた加圧成形
品を50℃以下の温度でカレンダー加工することを
特徴とするアセチレン高重合体成形品の製造方
法。1 Acetylene polymer with a cis content of 50% or more 5
A gel-like material consisting of ~95% by weight and 95~5% by weight of an inert organic solvent is heated at a temperature of 50°C or less and a pressure of 10~1000kg/
1. A method for producing an acetylene polymer molded article, which comprises pressure molding in a range of cm 2 and then calendering the obtained pressure molded article at a temperature of 50°C or less.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3468780A JPS56133133A (en) | 1980-03-21 | 1980-03-21 | Manufacture of acetylene high polymar molding |
US06/222,905 US4362680A (en) | 1980-03-21 | 1981-01-05 | Process for production of molded articles of acetylene polymer |
GB8101514A GB2072197B (en) | 1980-03-21 | 1981-01-19 | Process for producing molded articles of acetylene polymers |
FR8105503A FR2478525A1 (en) | 1980-03-21 | 1981-03-19 | PROCESS FOR MANUFACTURING A MOLDED ARTICLE IN A HIGH POLYMER OF ACETYLENE |
DE3111031A DE3111031C2 (en) | 1980-03-21 | 1981-03-20 | Process for the production of a molded article from a high polymer of acetylene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3468780A JPS56133133A (en) | 1980-03-21 | 1980-03-21 | Manufacture of acetylene high polymar molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56133133A JPS56133133A (en) | 1981-10-19 |
JPS6225084B2 true JPS6225084B2 (en) | 1987-06-01 |
Family
ID=12421301
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3468780A Granted JPS56133133A (en) | 1980-03-21 | 1980-03-21 | Manufacture of acetylene high polymar molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56133133A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5818227A (en) * | 1981-07-27 | 1983-02-02 | Toray Ind Inc | Manufacture of acetylene copolymer film excellent in electrical property |
-
1980
- 1980-03-21 JP JP3468780A patent/JPS56133133A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS56133133A (en) | 1981-10-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3726834A (en) | Thermoplastic copolyimides | |
EP0472630B1 (en) | Elongated object made of a copolymer of carbon monoxide and an olefinically unsaturated monomer, and method for the production thereof | |
JP3299598B2 (en) | Conductive polyurethane foam and method for producing the same | |
EP0026235B1 (en) | Process for molding an acetylene high polymer and process for fabrication thereof | |
GB2072197A (en) | Process for producing molded articles of acetylene polymers | |
JPS6019745B2 (en) | Peroxide composition, its production method, its use | |
JPS6225084B2 (en) | ||
US3228910A (en) | Process for preparing solid poly-1, 4-phenylene ethers | |
JPS5954014B2 (en) | Method for producing acetylene high polymer molded product | |
CN111636112A (en) | Graphene composite antibacterial and antiviral polypropylene filament and preparation method thereof | |
US4579921A (en) | Process for the manufacture of polyacetylene | |
JPH01178510A (en) | Polyalcohol homopolymer | |
JPS6028300B2 (en) | Method for producing porous acetylene polymer with fibrillar structure | |
JPS6342565B2 (en) | ||
JPS6226652B2 (en) | ||
JPS6114924B2 (en) | ||
US5204423A (en) | Process for the preparation of polythiophenes by use of ferric salts and alkyl halides | |
JP3723844B2 (en) | Method for producing carbon material from polyvinyl alcohol | |
JPS62283504A (en) | Highly conductive film-like polyacetylene and manufacture thereof | |
JPS6261059B2 (en) | ||
JPS6120412B2 (en) | ||
JPS6148542B2 (en) | ||
JPS6160844B2 (en) | ||
KR100665090B1 (en) | Method for Preparing Polyvinylalcohol Film from Waste Polyvinylalcohol and product therefrom | |
JPS6017348B2 (en) | Method for producing acetylene polymer with high electrical conductivity |