JPS61284407A - Manufacture of polyamide resin composite - Google Patents

Manufacture of polyamide resin composite

Info

Publication number
JPS61284407A
JPS61284407A JP60126925A JP12692585A JPS61284407A JP S61284407 A JPS61284407 A JP S61284407A JP 60126925 A JP60126925 A JP 60126925A JP 12692585 A JP12692585 A JP 12692585A JP S61284407 A JPS61284407 A JP S61284407A
Authority
JP
Japan
Prior art keywords
polyamide
water
weight
vent
polyamide 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.)
Granted
Application number
JP60126925A
Other languages
Japanese (ja)
Other versions
JPH0367540B2 (en
Inventor
Katsuya Okada
岡田 勝也
Akira Hirai
陽 平井
Noriyoshi Kotani
小谷 宣義
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP60126925A priority Critical patent/JPS61284407A/en
Publication of JPS61284407A publication Critical patent/JPS61284407A/en
Publication of JPH0367540B2 publication Critical patent/JPH0367540B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/84Venting or degassing ; Removing liquids, e.g. by evaporating components
    • B29B7/842Removing liquids in liquid form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/88Adding charges, i.e. additives
    • B29B7/94Liquid charges
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2077/00Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0005Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
    • B29K2105/0044Stabilisers, e.g. against oxydation, light or heat

Abstract

PURPOSE:To make the mixing of a stabilizing agent with polyamide uniform, by a method wherein water is removed through a vent port of a specific melting and extruding machine by adding the specific stabilizing agent into the polyamide to be melted and kneaded in a form of a water solution. CONSTITUTION:A molten state polyamide resin composite obtained by loading 100wt part polyamide resin and a 0.1-1.0wt part water solution, containing 5-150wt part potassium halide and 0-50wt part copper balide in 100wt part water, into a hopper 3 of a meting and extruding machine 1 provided with a vent hole and mixing up and melting within a cylinder 2 is transferred to a discharge port 6 by a screw 4; as a vent 5 is provided in the midst of the cylinder 2, there surplus water is eliminated out of the molten state polyamide. Therefore, it is desirable to make the inside of the cylinder 2, to which the vent 5 is fitted, into a depressurized atmosphere. Such a degree of subatmospheric pressure as to become the water in the polyamide composite obtainable from the discharge port 6 of an extruding machine into less than 0.2wt% and a passing period of time of its atmosphere are adopted.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリアミド樹脂組成物の製造方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a polyamide resin composition.

〔従来の技術〕[Conventional technology]

従来ポリアミドに対する安定剤としてハロゲン化銅等の
銅化合物およびハロゲン化カリウムが有効であることは
すでに知られている(特公昭57−23962号公報)
It is already known that copper compounds such as copper halides and potassium halides are effective as stabilizers for conventional polyamides (Japanese Patent Publication No. 57-23962).
.

これらの安定剤をポリアミドに添加するに際し、溶融混
線機等を用いてポリアミド中に前記安定剤を分散させる
方法が通常用いられる。
When adding these stabilizers to polyamide, a method is usually used in which the stabilizers are dispersed in the polyamide using a melt mixer or the like.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところが、前記方法では、これら安定剤、特にハロゲン
化カリウムをポリアミド中に均一に分散させることは、
非常に困難であり、十分に分散しなかった安定剤が物性
低下の原因となる他、射出成型後の製品の表面に斑点と
して顕われ、製品の価値を著しく低減させる。
However, in the above method, it is difficult to uniformly disperse these stabilizers, especially potassium halides, in the polyamide.
It is very difficult to do so, and the stabilizer that is not sufficiently dispersed not only causes a decline in physical properties, but also appears as spots on the surface of the product after injection molding, significantly reducing the value of the product.

そこで、安定剤の分散性をより改良する方法として特−
開田59−27949号公報記載の方法がある。この方
法はポリアミド粉末にヨウ化カリウムおよびヨウ化銅の
水溶液を混合した後、乾燥してポリアミド樹脂に添加す
る方法であり、相応の効果をあげている。
Therefore, as a method to further improve the dispersibility of the stabilizer,
There is a method described in Kaida No. 59-27949. This method involves mixing polyamide powder with an aqueous solution of potassium iodide and copper iodide, drying the mixture, and then adding the mixture to the polyamide resin, which has been shown to be quite effective.

しかしながら、この方法は前記ポリアミド粉末の乾燥が
必要であり、この乾燥は実際は非常に困難で、作業性が
悪いという問題がある。
However, this method requires drying of the polyamide powder, which is actually very difficult and has the problem of poor workability.

本発明の目的は安定剤が均一に分散されたポリアミド樹
脂組成物の製造方法を提供することにある。
An object of the present invention is to provide a method for producing a polyamide resin composition in which a stabilizer is uniformly dispersed.

〔問題点を解決するための手段〕[Means for solving problems]

すなわち、本発明の上記の目的はポリアミド樹脂100
重量部と、水100重量部にハロゲン化カリウム5〜1
50重量部およびハロゲン化銅0〜50重量部を含有さ
せた水溶液0.1〜10重量部とをベント付き溶融押出
機に供給して溶融混練し、次いで溶融混練された樹脂組
成物の含水率が0.2重量%以下になるまでベント孔を
介して水分を除去することを特徴とするポリアミド樹脂
組成物の製造方法から成る手段を採用することによって
達成される。
That is, the above object of the present invention is to obtain polyamide resin 100
parts by weight and 5 to 1 part by weight of potassium halide in 100 parts by weight of water.
50 parts by weight and 0.1 to 10 parts by weight of an aqueous solution containing 0 to 50 parts by weight of copper halide are supplied to a vented melt extruder and melt-kneaded, and then the water content of the melt-kneaded resin composition is determined. This is achieved by employing a method for producing a polyamide resin composition characterized in that water is removed through a vent hole until the amount of water becomes 0.2% by weight or less.

以下、本発明の構成と、発明の詳細な説明する。Hereinafter, the structure of the present invention and the detailed description of the invention will be explained.

本発明に使用されるポリアミド樹脂は公知のポリアミド
で、例えば、ポリカプロラクタム、?リヘキサメチレン
アジバミド等がある。
The polyamide resin used in the present invention is a known polyamide, such as polycaprolactam, ? Examples include lihexamethyleneazibamide.

ハロゲン化カリウムとしてはヨウ化カリウムを使用する
ことが望ましく、水100重量部に対してそれを5〜1
50、好ましくは50〜120重量部の割合で溶解させ
る。150重量部以上ではヨウ化カリウムが析出するた
めに好マシくナイ。ハロゲン化銅としてはヨウ化銅を使
用することが望ましく、ヨウ化カリウム水溶液100重
量部に対して、O〜50、好ましくは10〜40重量部
の割合で溶解させる。50重量部以上ではヨウ化カリウ
ム中にヨウ化銅が均一に分散しないため好ましくない。
As the potassium halide, it is preferable to use potassium iodide;
50, preferably 50 to 120 parts by weight. If it exceeds 150 parts by weight, potassium iodide will precipitate, so it is not good. As the copper halide, it is desirable to use copper iodide, and it is dissolved at a ratio of O to 50, preferably 10 to 40 parts by weight, per 100 parts by weight of an aqueous potassium iodide solution. If it exceeds 50 parts by weight, copper iodide will not be uniformly dispersed in potassium iodide, which is not preferable.

前記の安定剤をポリアミドに添加する具体的な方法は、
添付の図面に記載のベント付溶融押出機(1)のシリン
ダー口)内に前記水溶液とポリアミド樹脂とのブレンド
物を供給する方法である。
A specific method for adding the above stabilizer to polyamide is as follows:
This is a method of supplying a blend of the aqueous solution and polyamide resin into a vented melt extruder (1) (cylinder mouth) shown in the accompanying drawings.

前記ブレンド物は、あらかじめ、ポリアミドと前記水溶
液とを混合することによって得られたものでもよいし、
(例えば)ポツパー(3)内にポリアミド樹脂と前記水
溶液を連続計量しそれぞれ供給してもよいが、好ましく
は、後者の方法がよい。シリンダー(2)内で混合溶解
して、得られた溶融状のポリアミド樹脂組成物は、スク
リュー(4)によって、吐出口(6)に移送されるが、
シリンダー(2)の途中にベント(5)が設けられてい
るので、そこで、溶融状のポリアミド中から、過剰の水
分が除去される。従って、ベント(5)の取り付けられ
ているシリンダー内を減圧雰囲気にすることが望ましい
。減圧雰囲気は一般に公知の手段、例えば、ナツシュポ
ンプ等の減圧手段によって作られるが、減圧の程度は本
発明においては、−650txHg/d以下が好ましく
、更に好ましくは、−700mHg/d以下である。
The blend may be obtained by mixing the polyamide and the aqueous solution in advance, or
(For example) the polyamide resin and the aqueous solution may be continuously metered and supplied into the potper (3), but the latter method is preferred. The molten polyamide resin composition obtained by mixing and dissolving in the cylinder (2) is transferred to the discharge port (6) by the screw (4).
Since a vent (5) is provided in the middle of the cylinder (2), excess water is removed from the molten polyamide there. Therefore, it is desirable to create a reduced pressure atmosphere inside the cylinder to which the vent (5) is attached. The reduced pressure atmosphere is generally created by a known means, for example, a reduced pressure means such as a nutsch pump, and in the present invention, the degree of reduced pressure is preferably -650 txHg/d or less, more preferably -700 mHg/d or less.

しかも、押出機の吐出口(6)から得られるポリアミド
組成物中の水分が0.2重量%以下、好ましくは、0.
1重量%以下となるような減圧度とその雰囲気の通過時
間を採用する。水分率が0.2重量%より多いとポリア
ミド組成物が発泡し、吐出口から溶融押出しされたスト
ランドをペレタイズすることが困難になる。
Moreover, the water content in the polyamide composition obtained from the discharge port (6) of the extruder is 0.2% by weight or less, preferably 0.2% by weight or less.
The degree of pressure reduction and the passage time of the atmosphere are adopted so that the pressure becomes 1% by weight or less. If the moisture content is more than 0.2% by weight, the polyamide composition will foam, making it difficult to pelletize the strands melt-extruded from the discharge port.

なお、本発明の樹脂組成物には上記安定剤の他に公知の
補強材、例えばガラス繊維、マイカ、炭素繊維、顔料、
染料、タルク、ワラステナ9イト等を添加することがで
きる。以下、実施例により本発明の詳細な説明する。
In addition to the above-mentioned stabilizers, the resin composition of the present invention may contain known reinforcing materials such as glass fiber, mica, carbon fiber, pigments,
Dyes, talc, wollastenate, etc. can be added. Hereinafter, the present invention will be explained in detail with reference to Examples.

〔実施例〕〔Example〕

本発明の実施例、比較例に共通する内容につき説、明す
る。
Contents common to the Examples and Comparative Examples of the present invention will be explained and explained.

ヨウ化カリウム、ヨウ化銅水溶液の調製については、8
0℃の温水100重量部に対してヨウ化カリウム100
重量部を溶解し、更にヨウ化銅25重量部を溶解した。
For the preparation of potassium iodide and copper iodide aqueous solutions, see 8.
100 parts by weight of potassium iodide per 100 parts by weight of warm water at 0°C
Part by weight was dissolved, and further 25 parts by weight of copper iodide was dissolved.

ペレタイズ後の処理は温度70℃の脱湿空気(露点−2
0℃)中にペレットを5時間さらすことにより乾燥する
Processing after pelletizing is performed using dehumidified air at a temperature of 70°C (dew point -2).
Dry the pellet by exposing it to 0° C. for 5 hours.

評価の方法は得られたペレットを3オンス射出成型機で
成型した後、成形物の表面を切□削し、その表面10d
中にある白い斑点の個数で評価した。斑点の大きさにつ
いては大蔵省造弊局発行「きよう雑物判定法」により区
別した。
The evaluation method is to mold the obtained pellets with a 3-ounce injection molding machine, cut the surface of the molded product, and remove 10 d of the surface.
The evaluation was based on the number of white spots inside. The size of the spots was determined based on the ``Method for Judging Miscellaneous Items'' published by the Ministry of Finance.

実施例1〜3.比較例1〜2 表1に示す条件で実験を行ない、表2に示す結果を得た
Examples 1-3. Comparative Examples 1 and 2 Experiments were conducted under the conditions shown in Table 1, and the results shown in Table 2 were obtained.

表  2 〔発明の効果〕 本発明は特定の安定剤を水溶液の形で溶融混練されるポ
リアミド中に添加し、特定の溶融押出機のベントロから
水分を除去しているので、安定剤の、ポリアミド中への
混入が均一になるという効果を発揮する。しかもその操
作は極めて簡単であるので、工業的に有利な方法である
Table 2 [Effects of the Invention] In the present invention, a specific stabilizer is added in the form of an aqueous solution to polyamide that is melt-kneaded, and water is removed from the vent of a specific melt extruder. It has the effect of making the mixture evenly mixed inside. Moreover, since the operation is extremely simple, it is an industrially advantageous method.

【図面の簡単な説明】[Brief explanation of drawings]

図面は本発明に使用されるベント付溶融押出機の概略図
を示す。 1:ベント付溶融押出機 2ニジリンダ 3:ホッパー 4:スクリュ 5:ベントポート 6:吐出口
The drawing shows a schematic diagram of a vented melt extruder used in the present invention. 1: Melt extruder with vent 2 Niji cylinder 3: Hopper 4: Screw 5: Vent port 6: Discharge port

Claims (1)

【特許請求の範囲】[Claims] ポリアミド樹脂100重量部と、水100重量部にハロ
ゲン化カリウム5〜150重量部およびハロゲン化銅0
〜50重量部を含有させた水溶液0.1〜1.0重量部
とをベント付き溶融押出機に供給して溶融混練し、次い
で溶融混練された樹脂組成物の含水率が0.2重量%以
下になるまでベント孔を介して水分を除去することを特
徴とするポリアミド樹脂組成物の製造方法。
100 parts by weight of polyamide resin, 5 to 150 parts by weight of potassium halide and 0 parts by weight of copper halide in 100 parts by weight of water.
0.1 to 1.0 parts by weight of an aqueous solution containing ~50 parts by weight is supplied to a vented melt extruder and melt-kneaded, and then the water content of the melt-kneaded resin composition is 0.2% by weight. A method for producing a polyamide resin composition, characterized in that water is removed through a vent hole until the amount of water is reduced to below.
JP60126925A 1985-06-11 1985-06-11 Manufacture of polyamide resin composite Granted JPS61284407A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60126925A JPS61284407A (en) 1985-06-11 1985-06-11 Manufacture of polyamide resin composite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60126925A JPS61284407A (en) 1985-06-11 1985-06-11 Manufacture of polyamide resin composite

Publications (2)

Publication Number Publication Date
JPS61284407A true JPS61284407A (en) 1986-12-15
JPH0367540B2 JPH0367540B2 (en) 1991-10-23

Family

ID=14947292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60126925A Granted JPS61284407A (en) 1985-06-11 1985-06-11 Manufacture of polyamide resin composite

Country Status (1)

Country Link
JP (1) JPS61284407A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5578700A (en) * 1995-05-01 1996-11-26 Hunt Industries Inc. Continuous vacuum microwave rubber crumb reclamation unit
JPH08333209A (en) * 1995-06-05 1996-12-17 Matsushita Electric Ind Co Ltd Antimicrobial composition and production of antimicrobial material by using the composition
JP2005225994A (en) * 2004-02-13 2005-08-25 Teijin Chem Ltd Method for producing transparent thermoplastic resin composition, and transparent thermoplastic resin composition produced by the method
JP2007084747A (en) * 2005-09-26 2007-04-05 Nippon Polypenco Ltd Heat-resistant and dimensionally stable monomer-cast nylon molded form

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10292107A (en) * 1997-04-18 1998-11-04 Asahi Chem Ind Co Ltd Antimicrobial polyamide resin molding

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5578700A (en) * 1995-05-01 1996-11-26 Hunt Industries Inc. Continuous vacuum microwave rubber crumb reclamation unit
JPH08333209A (en) * 1995-06-05 1996-12-17 Matsushita Electric Ind Co Ltd Antimicrobial composition and production of antimicrobial material by using the composition
JP2005225994A (en) * 2004-02-13 2005-08-25 Teijin Chem Ltd Method for producing transparent thermoplastic resin composition, and transparent thermoplastic resin composition produced by the method
JP2007084747A (en) * 2005-09-26 2007-04-05 Nippon Polypenco Ltd Heat-resistant and dimensionally stable monomer-cast nylon molded form

Also Published As

Publication number Publication date
JPH0367540B2 (en) 1991-10-23

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