JPS5952635A - Shortening method of vulcanizing time of rubber article - Google Patents

Shortening method of vulcanizing time of rubber article

Info

Publication number
JPS5952635A
JPS5952635A JP16279282A JP16279282A JPS5952635A JP S5952635 A JPS5952635 A JP S5952635A JP 16279282 A JP16279282 A JP 16279282A JP 16279282 A JP16279282 A JP 16279282A JP S5952635 A JPS5952635 A JP S5952635A
Authority
JP
Japan
Prior art keywords
vulcanization accelerator
vulcanization
accelerator
fan
rubber
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
Application number
JP16279282A
Other languages
Japanese (ja)
Inventor
Michihito Kobayashi
小林 通人
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.)
Sumitomo Rubber Industries Ltd
Original Assignee
Sumitomo Rubber Industries Ltd
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 Sumitomo Rubber Industries Ltd filed Critical Sumitomo Rubber Industries Ltd
Priority to JP16279282A priority Critical patent/JPS5952635A/en
Publication of JPS5952635A publication Critical patent/JPS5952635A/en
Pending 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
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/02Conditioning or physical treatment of the material to be shaped by heating
    • 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
    • B29C35/00Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • B29C35/04Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using liquids, gas or steam
    • B29C35/049Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using liquids, gas or steam using steam or damp
    • 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
    • B29K2021/00Use of unspecified rubbers as moulding material

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)

Abstract

PURPOSE:To shorten the vulcanizing time of a rubber article or the like while using a conventional quantity of a conventional vulcanization accelerator, by a method wherein a vulcanization accelerator is maintained in an atmosphere of a predetermined humidity and a predetermined temperture for a predetermined period of time before being kneaded into a blended rubber. CONSTITUTION:A fan 7 is fitted to a lower side of a conveyor 2, an upper- lower pair of heaters 8, 9 are provided on the lower side of the fan 7, the lower heater 9 is immersed in water 10, water vapor generated by the heaters is forcibly fed upward by the fan 7, and the vulcanization accelerator 11 being conveyed on the conveyor 2 is heated and moistened at a relative humidity of 0- 100% and a temperature of 20-200 deg.C. After completing the moist heat treatment, the vulcanization accelerator decomposed is discharged into a container 13, and is fed to a kneading step. The quantity of the vulcanization accelerator decomposed by the moist heat treatment can be made to be constant, and the quantity is controlled between summer and winter.

Description

【発明の詳細な説明】 この発明はゴム物品の加硫時間を短縮する方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to a method of reducing the vulcanization time of rubber articles.

従来、配合ゴムの加硫反応を促進するには、加硫促進剤
が広く使われている。加硫促進剤は配合ゴム中で分解し
て加硫反応を促進する。一般に加硫反応は速く進行ずれ
は加硫時間がそれだけ短縮されるので生産性が向J二す
る。配合ゴムの加硫速度を速めるには配合ゴム中の加硫
剤の配合量を多くするとか、加硫促進剤の種類(速効性
加硫促進剤・遅効性加硫促進剤)を変えたり、2種以上
混合することが考えられるが、この方法は加硫促西己合
量増加によるコスト高や加硫促進剤の使用銘柄増加によ
るコスト率の低F及びコスト高の問題がある。従って加
硫促進剤などの尼合量を増すことには限度がある。
Conventionally, vulcanization accelerators have been widely used to accelerate the vulcanization reaction of compounded rubber. The vulcanization accelerator decomposes in the compounded rubber and accelerates the vulcanization reaction. Generally, the vulcanization reaction progresses quickly, and the vulcanization time is shortened accordingly, which improves productivity. To increase the vulcanization speed of compounded rubber, increase the amount of vulcanizing agent in compounded rubber, change the type of vulcanization accelerator (fast-acting vulcanization accelerator, slow-acting vulcanization accelerator), etc. Although it is conceivable to mix two or more types, this method has problems such as high cost due to an increase in the amount of vulcanization accelerator combined, and a low cost rate and high cost due to an increase in the brands of vulcanization accelerators used. Therefore, there is a limit to increasing the amount of vulcanization accelerator and the like.

この発明は、従来使用されている加硫促進剤を使用し、
またその1配合着も従来と同程度の配合量のままで、加
硫時間を短縮できるニジストマー又はゴム物品の加硫時
間短縮法を提供することを目的とする。
This invention uses a conventionally used vulcanization accelerator,
Another object of the present invention is to provide a method for shortening the vulcanization time of a nidistomer or rubber article, which can shorten the vulcanization time while maintaining the same amount of compounding as before.

この発、明の方法の概要は、加硫促進剤を配合ゴム中に
混練する前に、所定の湿度及びr都度の囲気中に所定時
間保持することを特徴とするーL記加硫促弦剤としては
、N−シクロへキシル−2−ベンゾチアゾリルスルフェ
ンアミド、2−メルカプトベンゾチアゾール、テトラメ
チルチウラムジスルフィド、N−7チルアクンデヒドア
ニリン、、N、N−ジフェニルチオ尿素、1.3−ジフ
ェニルグアニジ7等が挙げられるが、これ等に限定され
ない。この加硫促進剤を単独で所ボの湿熱条件下で予め
分解させた後をこ配合ゴム中に混練すると、配合ゴム中
の促進助剤(亜鉛華)と直ちに反応してZn塩化片物を
作り、これが硫黄の分子のリングな開環し、その結果硫
黄は配合ゴム中の炭素原イと加熱(加硫工程)下で直ち
に結合(架橋)可能状態となるので、従ってこの状態が
加硫工程に入る段階ですでに生成1・ているから、加硫
工程に移ると直ちに架橋反応が焦付し、それだけ加硫時
間は短縮されることになる。しかし、従来の方式では、
加硫促進剤は配合ゴム中において、加硫J程に入り昇l
晶によって始めて本格的Vこ分解して加硫を促進する。
The outline of the method of the present invention is that before kneading the vulcanization accelerator into the compounded rubber, it is kept in a predetermined humidity and an ambient atmosphere for a predetermined period of time. As the agent, N-cyclohexyl-2-benzothiazolyl sulfenamide, 2-mercaptobenzothiazole, tetramethylthiuram disulfide, N-7 tylacandehyde aniline, N,N-diphenylthiourea, 1.3 -diphenylguanidi 7, etc., but are not limited to these. When this vulcanization accelerator is decomposed in advance under moist heat conditions and then kneaded into this compounded rubber, it immediately reacts with the accelerator (zinc white) in the compounded rubber to form Zn chloride flakes. This causes the ring-opening of sulfur molecules, and as a result, the sulfur becomes ready to bond (crosslink) with the carbon atoms in the compounded rubber under heating (vulcanization process). Therefore, this state is called vulcanization. Since the product 1 has already been formed at the beginning of the process, the crosslinking reaction is immediately scorched when the vulcanization process begins, and the vulcanization time is shortened accordingly. However, in the conventional method,
The vulcanization accelerator enters the vulcanization stage in the compounded rubber and rises to 1.
Vulcanization is promoted by full-fledged V-decomposition and vulcanization.

上記湿熱り囲気としては、例えば第1図に原理的に示す
ように、温度と湿度をコントロールされたオーブン1と
、このオーブンを1’通し、例えば混練工程に通ずるベ
ルトコンベア2とからなる湿熱装置を用いる。オー7ン
11こはコンベア2tの上段に測温部3と測温部4とが
取付けられ、これらは湿熱記録部5と湿熱制御部6とに
電気的に連結されている。コンベア2の下段tこファン
7を取付け、ファン7の下段にJ二下−対(7) ヒー
ター8,9を設け、下方のヒーター9は水10内に水没
させ、ヒーターにより発生した水味気はファン7により
F方に強制的に送うレ、コンベア2上を移送される加硫
促進剤11を加熱加湿した後、ダクト12を通って循環
するようになっている。湿度は0〜1004であり、ま
た温度は一般的には20〜200を程度−である。尚、
液状の加硫促進剤は容器に入れてコンベアFを移送され
る。湿熱制御部6の湿熱制御の動作ステップは大要次の
肖りである。
The above-mentioned moist heat environment is, for example, as shown in principle in Fig. 1, a moist heat device consisting of an oven 1 whose temperature and humidity are controlled, and a belt conveyor 2 that passes through the oven 1' and leads to, for example, a kneading process. Use. In this case, a temperature measurement section 3 and a temperature measurement section 4 are attached to the upper stage of the conveyor 2t, and these are electrically connected to a heat and humidity recording section 5 and a heat and humidity control section 6. A fan 7 is installed on the lower stage of the conveyor 2, and heaters 8 and 9 are installed on the lower stage of the fan 7. The lower heater 9 is submerged in water 10, and the water taste generated by the heater is removed. The vulcanization accelerator 11 that is forcibly sent in the F direction by the fan 7 and transferred on the conveyor 2 is heated and humidified and then circulated through the duct 12. Humidity is between 0 and 100°C, and temperature is generally between 20 and 200°C. still,
The liquid vulcanization accelerator is placed in a container and transported on a conveyor F. The operation steps of the heat and humidity control by the heat and humidity control section 6 are summarized as follows.

乾湿温度計の原理を利用し、制御部6で設定した。乾球
温度と湿球温度が3,4で測定された温度と等しくなる
ようにヒーター8,9が作動するものである。
Settings were made using the control unit 6 using the principle of a psychrometric thermometer. The heaters 8 and 9 operate so that the dry bulb temperature and wet bulb temperature become equal to the temperatures measured in steps 3 and 4.

例えば、測温部5の温度が設定より低いとヒーター8が
作動し、II+11湿部4の湿度が設定より低ければヒ
ーター9が作動する。
For example, if the temperature of the temperature measuring section 5 is lower than the setting, the heater 8 is activated, and if the humidity of the II+11 humidity section 4 is lower than the setting, the heater 9 is activated.

湿熱処理を終了した分解した加硫促進剤はコンテナ15
に排出され、混練工程に移送されaこの湿度及び温度を
各々所′Ji!lll’fとすること、並びをこその湿
度雰囲気中に所尼時間保持することは、こ111こまっ
て加硫促進剤の分1!1vffiを一定に−することが
でき、又、夏と冬で分解量をコントロールする、例えは
、夏少なく冬多くすることにより、同種同量の加硫促進
剤において夏と冬の加硫時間の差をな(することができ
る。更には例えば、遅効性加硫促進剤を厚朴ゴムに対し
、例えば10%混練するよりも起動性促進剤/速効性促
進剤を847214混練するほうが加硫が速くなるので
、遅効性促進剤を混練前に20係分解させでおけば速効
性促進剤を混練する必要がない。従って本発明方法によ
れば使用量の節約、使用銘柄の減少、ひいては作業の省
力化が可能となる。
The decomposed vulcanization accelerator that has been subjected to the moist heat treatment is stored in container 15.
The humidity and temperature are controlled at each location and transferred to the kneading process. By keeping the vulcanization accelerator in a humid atmosphere for a certain period of time, it is possible to keep the vulcanization accelerator component 1!1 vffi constant. For example, by controlling the amount of decomposition in the summer and increasing the amount in the winter, the difference in vulcanization time between summer and winter can be made for the same type and amount of vulcanization accelerator. Vulcanization will be faster by kneading 847214 start-up accelerator/quick-acting accelerator than by kneading, for example, 10% of vulcanization accelerator into hard rubber, so mix the slow-acting accelerator by 20% before kneading. If left to stand, there is no need to knead the quick-acting accelerator.Therefore, according to the method of the present invention, it is possible to save the amount used, reduce the number of brands used, and save labor.

なお、加硫促進剤の水分率が0憾〜6.0%になるよう
に酸部に水を溜めた室内中に加硫促進剤を一定時間放置
することにより水分調整を施こした後、CMちに20C
〜200Cて公知構造の予熱オーブン中で加熱して加硫
促進剤を分解することも可能である。水分率はカールフ
イシャ〜法で測定できる。
In addition, after adjusting the moisture content by leaving the vulcanization accelerator in a room filled with water in the acid part for a certain period of time so that the moisture content of the vulcanization accelerator is 0 to 6.0%, CM Chini 20C
It is also possible to decompose the vulcanization accelerator by heating in a preheated oven of known construction to ~200C. Moisture content can be measured by the Karl-Huischer method.

次にこの発明の実施例及び比較例を示す。Next, examples and comparative examples of the present invention will be shown.

加(iltc 促a 剤N−シクロへキシル−2−ベン
ゾチアゾリルスルフェンアミドを+?+J記4I熱装置
を用いて温度50℃、湿度80係にて10時間湿熱処理
をしたものI P HRを表1に示す配合ゴム中tこバ
ンバリーミキサ−により混練して配合ゴム組成物Aを得
た。又、同じ加硫促進剤を水分率が3幅になるように水
分調整をした後に直ちに80℃で5時間予熱オーブンで
加熱して分解し、これを表1に示す配合ゴム中に混練し
て配合ゴム組成物Bを得た。他方、同じ加硫促進剤を予
め温熱処理を施こすことなく表1に示す配合ゴム中に混
練して配合ゴム組成物Cを得た。
Additive (ILTC) Accelerator N-cyclohexyl-2-benzothiazolyl sulfenamide +? The compounded rubber composition shown in Table 1 was kneaded in a Banbury mixer to obtain compounded rubber composition A.Also, the same vulcanization accelerator was immediately mixed with water after adjusting the moisture content so that the moisture content was in the 3 range. It was decomposed by heating in a preheated oven at ℃ for 5 hours and kneaded into the compounded rubber shown in Table 1 to obtain compounded rubber composition B.On the other hand, the same vulcanization accelerator was subjected to heat treatment in advance. The mixture was kneaded into the compounded rubber shown in Table 1 to obtain a compounded rubber composition C.

」1記配合ゴム組成物A + ’B +及びCをJSR
型キュラストメーターを用い−C加硫(基準条件、試料
寸法42グmy+ X 2絹厚、±3° 60PM)し
て、160℃で11J’A加硫時間における加硫速度(
スコーチタイム)を求めた。結果は、表2に示す通り、
湿熱処理を施こしたものが、湿熱処理を施こさないもの
に比し20係も加硫速度が速く、従って大幅に加硫時間
が短縮されることが判る。
” 1 Compounded rubber composition A + 'B + and C by JSR
-C vulcanization using a type Curalastometer (standard conditions, sample size 42g my +
Scorch Time). The results are shown in Table 2.
It can be seen that the vulcanization rate of those subjected to moist heat treatment is 20 times faster than those not subjected to moist heat treatment, and therefore the vulcanization time is significantly shortened.

L記実施例はタイヤに関するものであるが、このほかに
ゴムホース、ゴムベルト、 防舷tt 。
Example L relates to tires, but also includes rubber hoses, rubber belts, and fenders.

ゴムマット等のゴム物品の製ii:H,pこおいて実施
可能である。
It can be carried out in the production of rubber articles such as rubber mats.

」二連したように、この発明によるときは、加硫促進剤
を混練前に単ちり1で湿熱処」」(!を行うだけで加硫
反応を促萌させて加硫時間を短縮できて高価な加硫設備
の稼働効率を向上させることができ、又、加硫促進剤の
使用オ等を減少させることができる。
``As mentioned above, when using this invention, the vulcanization accelerator can be treated with a single layer of moist heat before kneading.'' (!) The vulcanization reaction can be accelerated and the vulcanization time can be shortened. The operational efficiency of expensive vulcanization equipment can be improved, and the use of vulcanization accelerators can be reduced.

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

図はこの発明の方法に使用する湿熱処理装置の1例を示
す概略構成図である。 1・・・オーブン、2・・・ベルトコンベア、5イ・・
1lll IFin部、4・・・測湿部、5・・・湿熱
記録部、6・・・湿熱制御部、7・・・ファン、8.9
・・・ヒーター、10・・・水、11・・・加硫促進剤
、12−・・ダクト、13・・・コンテナ特許出−1人
 住友ゴム工業株式会社 ]]1−系15ネ市j]ニー1 ■、小件の表示 昭和57年特許願162792薯 2、発明の名称 ゴム物品の加硫時間短縮方法I3 3、補正をする者 事イ11との関係 44j許出願人 4、補正命令の1」仁1 (自  発  ) 5、補正の対象 明細書の発明の詳細な説明の1開。 6、補正の内容 手 続 袖 正 p)(方式) 1事件の表示 昭和57年特許願第362792号 2発明の名称 ゴム物品の加硫時間短縮方法 6補正をする者 事件との関係 特許出願人 昭和58年1月25日(発送日) 5袖正の対象 願書及び明細書の発明の名称の欄 6袖正の内容 [+1*fi書 別紙の通り。 (2)明細書の発明の名称の欄の記載「ゴム精品の加硫
時間短縮法」とあるを「ゴム物品の加硫時間短縮方17
6−
The figure is a schematic configuration diagram showing an example of a moist heat treatment apparatus used in the method of the present invention. 1... Oven, 2... Belt conveyor, 5...
1llll IFin section, 4...Humidity measurement section, 5...Moisture heat recording section, 6...Moisture heat control section, 7...Fan, 8.9
...Heater, 10...Water, 11...Vulcanization accelerator, 12-...Duct, 13...Container patent issued - 1 person Sumitomo Rubber Industries, Ltd.]] 1-Series 15 Ne city j ] Ni 1 ■, Indication of minor matters 1982 Patent Application No. 162792, No. 2, Name of the invention Method for shortening vulcanization time of rubber articles I3 3. Person making the amendment Relationship with I11 44j Applicant 4, Order for amendment No. 1” Jin 1 (spontaneous) 5. 1. Detailed explanation of the invention in the specification subject to amendment. 6. Contents and Procedures for Amendments Sode Tadashi p) (Method) 1. Indication of the case Patent Application No. 362792 of 1982 2. Name of the invention Method for shortening the vulcanization time of rubber articles 6. Person making the amendment Relationship with the case Patent applicant January 25, 1981 (shipment date) 5. Name of the invention in the subject application and specification column 6. Contents of the sleeve correction [+1*fi document as attached. (2) In the title of the invention column of the specification, the statement ``Method for shortening the vulcanization time of rubber products'' was replaced with ``Method for shortening the vulcanization time of rubber articles 17''.
6-

Claims (1)

【特許請求の範囲】[Claims] (1)ゴム物品の製造工程において、加硫促進剤を配合
コム中tこ混練する前に、所定の湿度及び温度のP囲気
中に所定時間保持することを特徴とするゴム物品の加硫
時間短縮法。
(1) In the manufacturing process of rubber articles, before kneading the vulcanization accelerator in the compound comb, the vulcanization time of rubber articles is characterized by keeping the vulcanization accelerator in a P atmosphere at a predetermined humidity and temperature for a predetermined period of time. shortening method.
JP16279282A 1982-09-18 1982-09-18 Shortening method of vulcanizing time of rubber article Pending JPS5952635A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16279282A JPS5952635A (en) 1982-09-18 1982-09-18 Shortening method of vulcanizing time of rubber article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16279282A JPS5952635A (en) 1982-09-18 1982-09-18 Shortening method of vulcanizing time of rubber article

Publications (1)

Publication Number Publication Date
JPS5952635A true JPS5952635A (en) 1984-03-27

Family

ID=15761290

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16279282A Pending JPS5952635A (en) 1982-09-18 1982-09-18 Shortening method of vulcanizing time of rubber article

Country Status (1)

Country Link
JP (1) JPS5952635A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011069702A1 (en) * 2009-12-09 2011-06-16 Continental Reifen Deutschland Gmbh Method and device for activating a bonding system for spikes
CN110027143A (en) * 2019-04-29 2019-07-19 柴绍栋 A kind of weather strip for automobile vulcanizing equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011069702A1 (en) * 2009-12-09 2011-06-16 Continental Reifen Deutschland Gmbh Method and device for activating a bonding system for spikes
CN110027143A (en) * 2019-04-29 2019-07-19 柴绍栋 A kind of weather strip for automobile vulcanizing equipment

Similar Documents

Publication Publication Date Title
PL371820A1 (en) Method and apparatus for stabilizing plaster
JPS5952635A (en) Shortening method of vulcanizing time of rubber article
JP2006123272A (en) Method for kneading unvulcanized rubber
US6313212B1 (en) Continuous process for producing semi-finished rubber products with a silica reinforcing filler, for tyres, and tyres thus produced
JP2006213751A (en) Natural rubber and method for producing the same
EP0911359B1 (en) Continuous process for producing rubber material containing silica filler and tyres incorporating this material
US4247441A (en) Process for preparing a silicone molding composition
JPS58183237A (en) Shortening method for vulcanizing time of rubber article
CN106633217B (en) The preparation method of high-performance rubber
US1636569A (en) Douglas william kent-jones and charles woodland chitty
JP2006232880A (en) Rubber composition
JPS55152041A (en) Production of air tire for vehicles
ES468275A1 (en) Vulcanisates containing siliceous fillers
US1209643A (en) Method of drying materials.
US1734639A (en) Method of vulcanizing rubber and resulting products
US1814287A (en) Process for controlling the vulcanization of rubber and similar materials and products obtained thereby
US1523755A (en) Production of vulcanized-rubber products
GB191316997A (en) Improvements in or relating to the Manufacture of Starch or Starch Containing Material.
JPS6058002B2 (en) Method for shortening vulcanization time of rubber articles
US1613572A (en) Vulcanization of caoutchouc
US1698715A (en) Process for controlling the vulcanization of rubber and similar materials and products obtained thereby
US597283A (en) Maxime hocquet
US1734640A (en) Method of vulcanizing rubber and resulting products
SU242387A1 (en) METHOD FOR PRODUCING HETEROSILOXANE RUBBERS
US1943570A (en) Accelerator for the vulcanization of rubber