JPH11147220A - Chlorinated vinyl chloride resin composition and molded body using the composition - Google Patents
Chlorinated vinyl chloride resin composition and molded body using the compositionInfo
- Publication number
- JPH11147220A JPH11147220A JP9317319A JP31731997A JPH11147220A JP H11147220 A JPH11147220 A JP H11147220A JP 9317319 A JP9317319 A JP 9317319A JP 31731997 A JP31731997 A JP 31731997A JP H11147220 A JPH11147220 A JP H11147220A
- Authority
- JP
- Japan
- Prior art keywords
- vinyl chloride
- chloride resin
- composition
- chlorinated vinyl
- resin composition
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/362—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using static mixing devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/41—Intermeshing counter-rotating screws
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/40—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、耐熱性塩素化塩化
ビニル系樹脂組成物及びそれを用いた成形体に関する。TECHNICAL FIELD The present invention relates to a heat-resistant chlorinated vinyl chloride resin composition and a molded article using the same.
【0002】[0002]
【従来の技術】塩素化塩化ビニル系樹脂(以下、CPV
Cという)は、一般に塩化ビニル系樹脂(以下、PVC
という)を塩素化して作られる。CPVCはPVCの長
所といわれる難燃性、耐薬品性の特性を残し、かつPV
Cの欠点といわれる耐熱温度が低い点を改良しているの
で広い用途が期待されている。一方PVCは熱変形温度
が低いために、60〜70℃以上では使用できないとい
う大きな欠点を持っている。これに対しCPVCは熱変
形温度がPVCより20〜40℃も高く、PVCの欠点
である耐熱性が改良されている。従って、CPVCは自
動車用途にも幅広く使用されており、例えば、窓ガラス
周りを気密にするためのウエザ−ストリップや車体の天
井や側面に取り付けられるル−フモ−ル及びサイドモ−
ル等に多く使用されている。2. Description of the Related Art Chlorinated vinyl chloride resin (hereinafter referred to as CPV)
C) is generally a vinyl chloride resin (hereinafter referred to as PVC).
Chlorination). CPVC retains flame-retardant and chemical-resistant properties, which are said to be advantages of PVC, and
C is expected to be used in a wide range of applications because it has improved the low heat resistance temperature which is said to be a disadvantage of C. On the other hand, PVC has a serious drawback that it cannot be used at temperatures of 60 to 70 ° C. or higher because of its low heat deformation temperature. On the other hand, the heat deformation temperature of CPVC is higher by 20 to 40 ° C. than that of PVC, and the heat resistance, which is a drawback of PVC, is improved. Therefore, CPVC is also widely used in automotive applications. For example, weather strips for air-tightness around window glass, and roof and side modules mounted on ceilings and side surfaces of vehicle bodies.
Is widely used for
【0003】従来、ウエザ−ストリップまたはルーフモ
ールはステンレス等の金属に軟質PVC系樹脂または、
ゴム等で組み合わせたものが用いられていた。しかし、
最近になり車の軽量化、環境問題からのリサイクル性に
問題があり、またコストダウンの要求には従来のステン
レス等のものでは対応が難しく、ステンレスを代替しう
る樹脂化の要求があった。Conventionally, a weather strip or a roof molding is made of a soft PVC resin or a metal such as stainless steel.
What was combined with rubber etc. was used. But,
In recent years, there has been a problem in terms of weight reduction of vehicles and recyclability due to environmental problems, and it has been difficult to meet cost reduction requirements with conventional stainless steel and the like, and there has been a demand for resinization that can replace stainless steel.
【0004】一般に、CPVCを使用して成形体を得る
場合、パウダー状または顆粒状にペレット化したものを
使用して成形されている。しかし、ペレット化したCP
VC組成物はパウダー状のものと比べ、加工性、熱安定
性が悪くなり問題となっていた。In general, when a molded article is obtained using CPVC, it is molded using a powder or a granulated pellet. However, pelletized CP
The VC composition has a problem in that its processability and thermal stability are inferior to those of a powdery composition.
【0005】[0005]
【発明が解決しようとする課題】本発明は、上記問題点
を解決するものであって、加工性、熱安定性に優れたC
PVC組成物及びそれを用いた成形体を提供する。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems, and is intended to improve the workability and thermal stability of C.
Provided are a PVC composition and a molded article using the same.
【0006】[0006]
【課題を解決するための手段】本発明は、塩素含有量が
60〜70重量%である塩素化塩化ビニル樹脂単体また
は塩化ビニル樹脂との混合物、安定剤、滑剤、充填剤、
及び衝撃強化剤が桟状のブレーカプレートが取り付けら
れた2軸異方向押出機によって、溶融混練されてなるこ
とを特徴とする。According to the present invention, there is provided a chlorinated vinyl chloride resin having a chlorine content of 60 to 70% by weight or a mixture thereof with a vinyl chloride resin, a stabilizer, a lubricant, a filler,
And the impact strengthening agent is melt-kneaded by a biaxially different direction extruder to which a bar-shaped breaker plate is attached.
【0007】本発明で使用されるCPVCとしては、塩
素化前のPVCの平均重合度として500〜1400が
好ましい。平均重合度が500未満では耐衝撃性が低下
し、1400を超えると溶融流動性が低下し、成形が困
難となるからである。As the CPVC used in the present invention, the average degree of polymerization of PVC before chlorination is preferably from 500 to 1400. If the average degree of polymerization is less than 500, the impact resistance decreases, and if it exceeds 1,400, the melt fluidity decreases, and molding becomes difficult.
【0008】また、CPVCの平均塩素含有量は60〜
70重量%に限定される。平均塩素含有量が60%未満
では耐熱性が低下し、70%を超えると流動性が大きく
低下し、成形が困難となるからである。また、PVCと
併用する場合も同様に、平均塩素含有量は60〜70重
量%に限定される。The average chlorine content of CPVC is 60 to
Limited to 70% by weight. If the average chlorine content is less than 60%, the heat resistance decreases, and if it exceeds 70%, the fluidity greatly decreases, and molding becomes difficult. Similarly, when used in combination with PVC, the average chlorine content is limited to 60 to 70% by weight.
【0009】上記安定剤としては、例えば、一般に使用
されている鉛系安定剤、ジブチル錫マレート、ジブチル
錫メルカプト等の錫系安定剤;ケイ酸塩、ケイ酸との複
合物;ハイドロタルサイト類等の無機安定剤などが使用
できる。Examples of the stabilizers include commonly used lead stabilizers, tin stabilizers such as dibutyltin malate and dibutyltin mercapto; silicates, composites with silicic acid; hydrotalcites And the like can be used.
【0010】上記滑剤としては、例えば、ステアリン
酸、オレイン酸及びこれらのマグネシウム、カルシウム
等の金属塩;パラフィンワックス、ポリエチレンワック
ス等の脂肪族炭化水素系;ブチルステアレート等のモノ
アルコール脂肪酸エステル系;グリセリンモノステアレ
ート、グリセリントリステアレート等の多価アルコール
脂肪酸エステル系の滑剤等が挙げられる。Examples of the lubricant include stearic acid, oleic acid and metal salts thereof such as magnesium and calcium; aliphatic hydrocarbons such as paraffin wax and polyethylene wax; monoalcohol fatty acid esters such as butyl stearate; Glycerin monostearate, glycerin tristearate, and other polyhydric alcohol fatty acid ester-based lubricants are included.
【0011】上記充填剤としては、例えば、炭酸カルシ
ウム、クレー、タルク等が挙げられ、改質剤としては、
例えば、メチルメタクリレート・ブタジエン・スチレン
共重合体のMBS樹脂、アクリルニトリル・ブタジエン
・スチレン共重合体のABS樹脂、塩素化ポリエチレン
等が挙げられる。Examples of the filler include calcium carbonate, clay, talc and the like.
For example, an MBS resin of a methyl methacrylate / butadiene / styrene copolymer, an ABS resin of an acrylonitrile / butadiene / styrene copolymer, a chlorinated polyethylene and the like can be mentioned.
【0012】本発明では上記以外の添加剤としてポリメ
チルメタクリレート系の加工助剤、酸化防止剤、紫外線
吸収剤、帯電防止剤、顔料など適宜添加されてもよい。In the present invention, as additives other than those described above, a polymethyl methacrylate-based processing aid, an antioxidant, an ultraviolet absorber, an antistatic agent, a pigment and the like may be appropriately added.
【0013】本発明のCPVC組成物をペレットとして
得る方法は、上記樹脂、安定剤、滑剤及び衝撃強化剤を
スーパーミキサーで均一に混合し2軸異方向の押出機で
桟状のブレーカプレートを用いペレット金型にて押出成
形し、ペレット金型から出た、CPVC組成物をペレッ
トカッターにてカッティングする。The method for obtaining the CPVC composition of the present invention as pellets is as follows. The above resin, stabilizer, lubricant and impact enhancer are uniformly mixed by a super mixer, and a cross-shaped extruder is used in a biaxially different direction using a cross-shaped breaker plate. Extrusion molding is performed with a pellet mold, and the CPVC composition that has come out of the pellet mold is cut with a pellet cutter.
【0014】本発明では押出機として2軸異方向押出機
が用いられる。2軸異方向押出機の大きさに制限はな
く、全ての2軸異方向の押出機が使用できる。1軸押出
機や2軸同方向押出機では熱安定性が大きく損なわれ、
加工性が低下する等の問題が生じることがある。2軸異
方向押出機のスクリューは一般的なフルフライトスクリ
ューが好ましく、バレルはパラレル、又はコニカルタイ
プのどちらでも使用できる。また、ブレーカプレートに
は図2の桟状のブレーカプレートを使用する。現在、一
般的には図3の蜂の巣状の多くの穴を持つブレーカプレ
ート(以下通常ブレーカプレートという。)が使われて
いるが圧力が大きくかかり、CPVCには適さない。桟
状のブレーカプレートを使用するとペレット製造時の押
出機の負荷が大幅に下がり、樹脂温度を低く、また押出
量も通常ブレーカプレートよりも多くなり、生産性も大
幅に向上する。In the present invention, a twin-screw extruder is used as an extruder. The size of the twin-screw extruder is not limited, and any twin-screw extruder can be used. In a single-screw extruder or a twin-screw extruder, the thermal stability is greatly impaired,
Problems such as deterioration in workability may occur. The screw of the twin-screw extruder is preferably a general full-flight screw, and the barrel may be either of a parallel type or a conical type. Moreover, the crosspiece-shaped breaker plate of FIG. 2 is used for the breaker plate. At present, generally, a breaker plate having a large number of holes in a honeycomb shape as shown in FIG. 3 (hereinafter, usually referred to as a breaker plate) is used, but a large pressure is applied, which is not suitable for CPVC. The use of a bar-shaped breaker plate greatly reduces the load on the extruder during pellet production, lowers the resin temperature, increases the extrusion rate compared to a normal breaker plate, and greatly improves productivity.
【0015】一方、1軸、2軸同方向の押出機では樹脂
温度が非常に高くなり、ウエザーストリップ等の成形体
を得ようとすると表面性が悪く、分解時間も短く、安定
して製造することができない。上記桟状のブレーカプレ
ートの材質は特には限定されず、通常の材質が使用され
る。図2の形状A部分の幅は特に限定されず、場合によ
っては幅を大きいものを使用することも可能である。但
し、基本的な形状は図2の通りである。On the other hand, in the case of a single-screw and twin-screw extruder, the resin temperature becomes extremely high, and if a molded article such as a weather strip is to be obtained, the surface properties are poor, the decomposition time is short, and the production is stable. Can not do. The material of the bar-shaped breaker plate is not particularly limited, and a usual material is used. The width of the shape A portion in FIG. 2 is not particularly limited, and a wide width may be used in some cases. However, the basic shape is as shown in FIG.
【0016】[0016]
【発明の実施の形態】以下に実施例を掲げて本発明を更
に詳しく説明するが、本発明はこれら実施例のみに限定
されるものではない。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples.
【0017】(実施例1〜4、比較例1〜5)表1、表
2に示す配合量の各成分をスーパーミキサーで均一に混
合した樹脂組成物を、シリンダー温度をそれぞれ(C
1:150℃、C2:160℃、C3:170℃、C
4:175℃)に設定し、アダプター温度170℃、ダ
イ温度170℃に設定し各押出機に供給し、ペレタイザ
ーで切断してペレットを得た。その得られたペレットを
190℃のロールにて巻き付き3分間実施し、ロールシ
ートを作成し200℃ギアオーブンにロールシートを入
れ黒化までの時間(分)を測定し老化熱安定性とした。
その結果を表1、2に示した。(Examples 1 to 4, Comparative Examples 1 to 5) A resin composition obtained by uniformly mixing the components having the compounding amounts shown in Tables 1 and 2 with a super mixer was measured at a cylinder temperature of (C
1: 150 ° C, C2: 160 ° C, C3: 170 ° C, C
4: 175 ° C.), the adapter temperature was set to 170 ° C., and the die temperature was set to 170 ° C., supplied to each extruder, and cut with a pelletizer to obtain pellets. The obtained pellets were wound around a roll at 190 ° C. for 3 minutes to prepare a roll sheet, and the roll sheet was put into a 200 ° C. gear oven, and the time (minute) until blackening was measured to determine the aging heat stability.
The results are shown in Tables 1 and 2.
【0018】次いでペレットを65mmシングル押出機
(L/D=22、フルフライトスクリュー、圧縮比=
3.0)でバレル温度をそれぞれ(B1:150℃、B
2:160℃、B3:170℃)に設定し、ダイ温度を
それぞれ(DH:175℃、D1:175℃、D2:1
85℃)に設定した条件で押出成形し、得られた成形体
の表面状態を目視にて観察し以下のようにランクをつ
け、表1、2に示した。 ◎:表面が非常に平滑で良好 ○:良好 △:若干波打
ちあり ×:大きく波打ちあり ××:非常に悪い。Next, the pellets were subjected to a 65 mm single extruder (L / D = 22, full flight screw, compression ratio =
3.0), the barrel temperature was set to (B1: 150 ° C., B
2: 160 ° C., B3: 170 ° C.), and the die temperatures are respectively (DH: 175 ° C., D1: 175 ° C., D2: 1).
Extrusion molding was performed under the conditions set at (85 ° C.), and the surface state of the obtained molded body was visually observed and ranked as shown below. ◎: Very smooth and good surface 良好: Good :: Slight undulation ×: Large undulation XX: Very bad.
【0019】表1、表2に示す原材料は以下のものを使
用した。 *1CPVC:徳山積水工業社製(原料PVC平均重合
度1,000、塩素含有量64重量%) *2PVC:徳山積水工業社製TS−1,000R(平
均重合度1,000)The following raw materials shown in Tables 1 and 2 were used. * 1 CPVC: manufactured by Tokuyama Sekisui Industry Co., Ltd. (average degree of polymerization of raw material 1,000, chlorine content 64% by weight) * 2 PVC: TS-1,000R manufactured by Tokuyama Sekisui Industry Co., Ltd. (average degree of polymerization 1,000)
【0020】 三塩基性硫酸鉛:堺化学工業社製TL−7,000 ステアリン酸鉛:堺化学工業社製SL−1,000 ケイ酸カルシウム:水澤化学社製 MBS:呉羽化学工業社製BTA−751 ポリエチレンワックス:三井石油化学工業社製三井ハイ
ワックス200P(平均分子量2,000) モンタン酸ワックス:ヘキストジャパン社製ヘキストワ
ックスOPTribasic lead sulfate: TL-7,000 manufactured by Sakai Chemical Industry Co., Ltd. Lead stearate: SL-1,000 manufactured by Sakai Chemical Industry Co., Ltd. Calcium silicate: manufactured by Mizusawa Chemical Co., Ltd. MBS: BTA- manufactured by Kureha Chemical Industry Co., Ltd. 751 polyethylene wax: Mitsui Petrochemical Industry Co., Ltd. Mitsui High Wax 200P (average molecular weight 2,000) montanic acid wax: Hoechst Wax OP manufactured by Hoechst Japan
【0021】 *3 2軸異方向押出機:東芝機械社製(TEC−6
5) *4 2軸異方向押出機:東芝機械社製(TED−95
CVA) *5 1軸押出機:株式会社池貝社製(FS−90) *6 2軸同方向押出機:株式会社社製(GT−11
0)* 3 Twin screw extruder: Toshiba Machine Co., Ltd. (TEC-6
5) * 4 Twin screw extruder: Toshiba Machine Co., Ltd. (TED-95)
CVA) * 5 Single-screw extruder: Ikegai Co., Ltd. (FS-90) * 6 Twin-screw extruder: GT-11 (GT-11)
0)
【0022】[0022]
【表1】 [Table 1]
【0023】[0023]
【表2】 [Table 2]
【0024】表1の実施例1〜4の結果から明らかなよ
うに、2軸押出機にて桟状のブレーカプレートを用いて
得られたペレットは熱安定性及び押出成型時に得られる
成形体の表面性が良好である。これに対して表2の比較
例1〜5においては、ペレット作成時の負荷(Amp)
が高く、また得られたペレットは作成時の樹脂温度が非
常に高いため熱安定性が悪く、押出成形にて得られた成
形体の表面性も悪い。As is evident from the results of Examples 1 to 4 in Table 1, the pellets obtained by using a bar-shaped breaker plate with a twin-screw extruder are heat-stable and have a good shape. Good surface properties. On the other hand, in Comparative Examples 1 to 5 in Table 2, the load (Amp) at the time of pellet preparation was used.
In addition, the obtained pellets have a very high resin temperature at the time of preparation, and thus have poor thermal stability, and the molded article obtained by extrusion has poor surface properties.
【0025】[0025]
【発明の効果】本発明のCPVC組成物は、桟状のブレ
ーカプレートを有する2軸押出機を使用することによ
り、生産時の負荷が低く、押出量が多く、熱安定性の優
れたペレットとして得られる。従って、該CPVC組成
物は、表面性が良好なウエザーストリップ、ルーフモー
ルの成形体等に好適に用いられる。The CPVC composition of the present invention can be used as pellets having a low load at the time of production, a large extrusion rate, and excellent heat stability by using a twin-screw extruder having a bar-shaped breaker plate. can get. Therefore, the CPVC composition is suitably used for weather strips having excellent surface properties, molded articles of roof moldings, and the like.
【図1】ウエザ−ストリップの模式断面図である。FIG. 1 is a schematic sectional view of a weather strip.
【図2】桟状ブレーカプレートの模式斜視図である。FIG. 2 is a schematic perspective view of a bar-shaped breaker plate.
【図3】通常ブレーカプレートの平面図である。FIG. 3 is a plan view of a normal breaker plate.
1 ステンレス、または塩素化塩化ビニル系樹脂 2 軟質塩化ビニル系樹脂 3 ガラス 1 Stainless or chlorinated vinyl chloride resin 2 Soft vinyl chloride resin 3 Glass
Claims (4)
素化塩化ビニル樹脂単体または塩化ビニル樹脂との混合
物、安定剤、滑剤、充填剤、及び衝撃強化剤が桟状のブ
レーカプレートが取り付けられた2軸異方向押出機によ
って、溶融混練されてなることを特徴とする塩素化塩化
ビニル系樹脂組成物。1. A bar-shaped breaker plate comprising a chlorinated vinyl chloride resin having a chlorine content of 60 to 70% by weight or a mixture thereof with a vinyl chloride resin alone, a stabilizer, a lubricant, a filler, and an impact reinforcing agent. A chlorinated vinyl chloride resin composition characterized by being melt-kneaded by a twin-screw, bidirectional extruder.
レットであることを特徴とする塩素化塩化ビニル系樹脂
組成物。2. A chlorinated vinyl chloride resin composition, wherein the chlorinated vinyl chloride resin composition is a pellet.
組成物または、請求項2記載のペレットを用いて得られ
る成形体。3. A molded article obtained by using the chlorinated vinyl chloride resin composition according to claim 1 or the pellet according to claim 2.
ルーフモール用途である請求項3記載の成形体4. The molded article according to claim 3, wherein the molded article is used for a weather strip or a roof molding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9317319A JPH11147220A (en) | 1997-11-18 | 1997-11-18 | Chlorinated vinyl chloride resin composition and molded body using the composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9317319A JPH11147220A (en) | 1997-11-18 | 1997-11-18 | Chlorinated vinyl chloride resin composition and molded body using the composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11147220A true JPH11147220A (en) | 1999-06-02 |
Family
ID=18086890
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9317319A Pending JPH11147220A (en) | 1997-11-18 | 1997-11-18 | Chlorinated vinyl chloride resin composition and molded body using the composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11147220A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115584097A (en) * | 2022-08-31 | 2023-01-10 | 湖北金牛管业有限公司 | CPVC power cable conduit and preparation method thereof |
-
1997
- 1997-11-18 JP JP9317319A patent/JPH11147220A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115584097A (en) * | 2022-08-31 | 2023-01-10 | 湖北金牛管业有限公司 | CPVC power cable conduit and preparation method thereof |
CN115584097B (en) * | 2022-08-31 | 2024-02-27 | 湖北金牛管业有限公司 | CPVC power cable conduit and preparation method thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP3447084B1 (en) | Polyvinyl chloride-based rigid molded products and method for manufacturing the same | |
US11613639B2 (en) | Polyvinyl chloride-based resin molded product and method for manufacturing the same | |
JPS6227438A (en) | Method for manufacturing breathable film | |
KR100521005B1 (en) | Method for manufacturing poly vinyl chloride compounds and pvc compounds | |
JPH11147220A (en) | Chlorinated vinyl chloride resin composition and molded body using the composition | |
EP0124371B1 (en) | Soft vinyl chloride resin composition | |
JPH1160868A (en) | Vinyl chloride resin composition for foam extrusion | |
JPS6218435A (en) | Production of gas-permeable film | |
JP4259630B2 (en) | Chlorinated vinyl chloride resin composition | |
US10550255B2 (en) | Polyolefine resin composition, polyolefine master batch, method of manufacturing polyolefine master batch, and article formed of the same | |
JPS6356894B2 (en) | ||
JPH07224188A (en) | Masterbatch of chemical for rubber and plastic | |
JPH11151742A (en) | Coextrusion molded product of soft/rigid vinyl chloride resin composition | |
JPH1160873A (en) | Chlorinated vinyl chloride resin composition | |
JPH11269295A (en) | Chlorinated vinyl chloride based resin composition for foaming | |
JPH11172066A (en) | Chlorinated vinyl chloride resin composition | |
JPH11209547A (en) | Vinyl chloride-based resin composition | |
CN115044133B (en) | Antistatic biaxially oriented polypropylene film-free base film and preparation method thereof | |
JPH11293071A (en) | Styrenic resin composition for extrusion molding and molded body | |
JPH0482034B2 (en) | ||
JPH09111080A (en) | Polyvinyl chloride tubular film composition for agriculture | |
JP2019073586A (en) | Polyvinyl chloride resin molding and method for producing the same | |
JPH10219065A (en) | Chlorinated vinyl chloride resin composition | |
WO1996035746A1 (en) | Biodegradable thermoplastic moulding compounds with improved processing properties and performance characteristics | |
JPS6017296B2 (en) | Thermoplastic resin molding material |